References

  1. 2013 ASHRAE Handook. Fundamentals (SI Edition).

  2. Aalto, M., Keskinen, K.I.; Liquid Densities at High Pressures. Fluid Phase Equilibria 166 (1999) 183-205, http://dx.doi.org/10.1016/s0378-3812(99)00300-3

  3. Aalto, M., Keskinen, K.I., Aittamaa, J., Liukkonen, S.; An Improved Correlation for Compressed Liquid Densities of Hydrocarbons. Part 1. Pure Compounds. Fluid Phase Equilibria 114 (1996) 1-19, http://dx.doi.org/10.1016/0378-3812(95)02822-6

  4. Aalto, M., Keskinen, K.I., Aittamaa, J., Liukkonen, S.; An Improved Correlation for Compressed Liquid Densities of Hydrocarbons. Part 2. Mixtures. Fluid Phase Equilibria 114 (1996) 21-35, http://dx.doi.org/10.1016/0378-3812(95)02824-2

  5. Abushammala, O., Hreiz, R., Lamaître, C., Favre, E.; Laminar flow friction factor in highly curved helical pipes: Numerical investigation, predictive correlation and experimental validation using a 3D-printed model. Chem. Eng. Sci. 207(7) (2019) 1030-1039, http://dx.doi.org/10.1016/j.ces.2019.07.018

  6. Adachi, Y., Lu, B.C.-Y., Sugie, H.; A Four-Parameter Equation of State. Fluid Phase Equilibria 11 (1983) 29-48, http://dx.doi.org/10.1016/0378-3812(83)85004-3

  7. Adler, M.; Strömung in gekrümmten Rohren. Z. Angew. Math. Mech. 14(5) 257-275, http://dx.doi.org/10.1002/zamm.19340140502

  8. Agarwal, S.K., Raja Rao, M.; Heat transfer augmentation for the flow of a viscous liquid in circular tubes using twisted tape inserts. Int. J. Heat Mass Transfer 39(17) (1996) 3547-3557, http://dx.doi.org/10.1016/0017-9310(96)00039-7

  9. Ahmed, T.; Equations of State and PVT Analysis: Applications forImproved Reservoir Modeling, 2nd Edition. Gulf Professional Publishing, 2016, ISBN 9780128015704,, http://dx.doi.org/10.1016/B978-0-12-801570-4.00002-7

  10. Ahmed, T.; Hydrocarbon Phase Behavior. Gulf Publishing, Houston, TX, 1989.

  11. Ahmed, T., Cady, G., Story, A.; A Generalized Correlation for Characterizing theHydrocarbon Heavy Fractions.. Paper SPE 14266, presented at the 60th Annual TechnicalConference of the Society of Petroleum Engineers, Las Vegas,September 22–25, 1985.

  12. Ahrendts, J., Baehr, H.D.; The Thermodynamic Properties of Ammonia. VDI-Forsch., Number 596, 1979.

  13. Akasaka, R.; New Fundamental Equations of State with a Common Functional Form for 2,3,3,3-Tetrafluoropropene (R-1234yf) and trans-1,3,3,3-Tetrafluoropropene (R-1234ze(E)). Int. J. Thermophys. 32(6) (2011) 1125-1147, http://dx.doi.org/10.1007/s10765-011-0992-0

  14. Akasaka, R.; Recent trends in the development of Helmholtz energy equations of state and their application to 3,3,3-trifluoroprop-1-ene (R-1243zf). Sci. Tech. Built Env. 22(8) (2016) 1136-1144, http://dx.doi.org/10.1080/23744731.2016.1208000

  15. Akasaka, R.; A Reliable and Useful Method to Determine the Saturation State from Helmholtz Energy Equations of State. J. Thermal Sci. Tech. 3(3) (2008) 442-451, http://dx.doi.org/10.1299/jtst.3.442

  16. Akasaka, R., Fukushima, M., Lemmon, E.W.; A Helmholtz Energy Equation of State for Trifluoroethylene (R-1123). International Refrigeration and Air Conditioning Conference at Purdue, July 11-14, 2016, http://docs.lib.purdue.edu/iracc/1698.

  17. Akasaka, R., Fukushima, M., Lemmon, E.W.; A Helmholtz Energy Equation of State for cis‐1‐Chloro‐2,3,3,3‐tetrafluoro‐1‐propene [R‐1224yd(Z)]. Int. J. Thermophysics 44 (2023) 166, http://dx.doi.org/10.1007/s10765-023-03266-3

  18. Akasaka, R., Fukushima, M., Lemmon, E.W.; A Helmholtz Energy Equation of State for Cis-1-chloro-2,3,3,3-tetrafluoropropene (R-1224yd(Z)). 21st European Conference on Thermophysical Properties, Graz, Austria, September 3-8, 2017

  19. Akasaka, R., Higashi, Y., Akoda, N., Fukuda, S., Lemmon, E.W.; Thermodynamic properties of trifluoroethene (R1123): (p, ρ, T) behavior and fundamental equation of state. Int. J. Refrig. 119 (2020) 457-467, http://dx.doi.org/10.1016/j.ijrefrig.2020.07.011

  20. Akasaka, R., Higashi, Y., Miyara, A., Koyama, S.; A fundamental equation of state for cis-1,3,3,3-tetrafluoropropene (R-1234ze(Z)). Int. J. Refrig. 44 (2014) 168-176, http://dx.doi.org/10.1016/j.ijrefrig.2013.12.018

  21. Akasaka, R., Huber, M.L., Simoni, L.D., Lemmon, E.W.; A Helmholtz Energy Equation of State for trans-1,1,1,4,4,4-Hexafluoro-2-butene [R-1336mzz(E)] and an Auxiliary Extended Corresponding States Model for the Transport Properties. Int. J. Thermophys 44(4) (2023) 50, http://dx.doi.org/10.1007/s10765-022-03143-5

  22. Akasaka, R., Kayukawa, Y.; A fundamental equation of state for trifluoromethyl methyl ether (HFE-143m) and its application to refrigeration cycle analysis. Int. J. Refrig., 35(4) (2012) 1003-1013, http://dx.doi.org/10.1016/j.ijrefrig.2012.01.003

  23. Akasaka, R., Lemmon, E.W.; Fundamental Equations of State for cis-1,3,3,3-Tetrafluoropropene [R-1234ze(Z)] and 3,3,3-Trifluoropropene (R-1243zf). J. Chem. Eng. Data 64(11) (2019) 4679-4691, http://dx.doi.org/10.1021/acs.jced.9b00007

  24. Akasaka, R., Lemmon, E.W.; A Helmholtz Energy Equation of State for 3,3,3‐Trifluoroprop‐1‐ene (R‐1243zf). Int. J. Thermophysics 46 (2025) 23, http://dx.doi.org/10.1007/s10765-024-03481-6

  25. Akasaka, R., Lemmon, E.W.; An International Standard Formulation for trans-1-Chloro-3,3,3-trifluroprop-1-ene [R1233zd(E)] Covering Temperatures from theTriple-Pont Temperature to 450K and Pressuresup to 100 MPa. J. Phys. Chem. Ref. Data 51(2) (2022) 023101, http://dx.doi.org/10.1063/5.0083026

  26. Akasaka, R., Lemmon, E.W.; A Helmholtz Energy Equations of State for Calculations of Thermodynamic Properties of trans-1,2-Difluoroethene [R-1132(E)]. Int. J. Thermophys. 45(12) (2024) 174, http://dx.doi.org/10.1007/s10765-024-03447-8

  27. Akasaka, R.; Zhou, Y.; Lemmon, E.W.; Fundamental Equation of State for 1,1,1,3,3-Pentafluoropropane (R-245fa). J. Phys. Chem. Ref. Data 44(1) (2015) 013104, http://dx.doi.org/10.1063/1.4913493

  28. Aleksandrov, I.S., Gerasimov, A.A., Grigor’ev, B.A.; Using Fundamental Equations of State for Calculating the Thermodynamic Properties of Normal Undecane. Thermal Engineering, 58(8) (2011) 691-698, http://dx.doi.org/10.1134/S0040601511080027

  29. Ali, S.; Pressure drop correlations for flow through regular helical coil tubes. Fluid Dyn. Research 28 (2001) 295-310, http://dx.doi.org/10.1016/s0169-5983(00)00034-4

  30. Almedeij, J.; Drag Coefficient of Flow around a Sphere: Matching Asymptotically the Wide Trend. Powder Technology 186(3) (2008) 218-223, http://dx.doi.org/10.1016/j.powtec.2007.12.006

  31. Almeida, G.S., Aznar, M., Silva Telles, A.; Uma Nova Forma de Dependência com a Temperatura do Termo Atrativo de Equaçöes de Estado Cúbicas. Cad. Eng. Quim., 8 (1991) 95-123

  32. Ambrose, D.; Correlation and Estimation of Vapor-Liquid Critical Properties: I. Critical Temperatures of Organic Compounds. National Physical Laboratory, Teddington, NPL Rep. Chern. 92, 1978, corrected 1980.

  33. Ambrose, D.; Correlation and Estimation of Vapor-Liquid Critical Properties: II. Critical Pressures and Volumes of Organic Compounds. National Physical Laboratory, Teddington, NPL Rep. 98, 1979

  34. Ambrose, D., Walton, J.; Vapour Pressures up to Their Critical Temperatures of Normal Alkanes and 1-Alkanols. Pure & Appl. Chem. 61(8) 1395-1403 (1989), http://dx.doi.org/10.1351/pac198961081395

  35. Angus, S., Armstrong, B., de Reuck, K.M.; International Thermodynamic Tables of the Fluid State-7: Propylene (Propene). IUPAC Chemical Data Series nº25, Pergamon Press, 1980

  36. Antoine, C.; Tensions des Vapeurs: Nouvelle Relation Entre les Tensions et les Tempé. Compt.Rend. 107:681-684 (1888)

  37. API; Technical Data book: Petroleum Refining 6th Edition.

  38. ASHRAE; Designation and Safety Classification of Refrigerants. Standard 34-2010

  39. Assael, M.J., Assael. J.-A.M., Huber, M.L., Perkins, R.A., Takata, Y.; Correlation of the Thermal Conductivity of Normal and Parahydrogen from the Triple Point to 1000 K and up to 100 MPa. J. Phys. Chem. Ref. Data 40(3) (2011) 033101, http://dx.doi.org/10.1063/1.3606499

  40. Assael, M.J., Bogdanou, I., Mylona, S.K., Huber, M.L. Huber, Perkins, R.A., Vesovic, V.; Reference Correlation of the Thermal Conductivity of n-Heptane from the Triple Point to 600 K and up to 250 MPa. J. Phys. Chem. Ref. Data 42(2) (2013) 023101, http://dx.doi.org/10.1063/1.4794091

  41. Assael, M.J., Koini, I.A., Anoniadis, K.D., Huber, M.L., Abdulagatov, I.M., Perkins, R.A.; Reference Correlation of the Thermal Conductivity of Sulfur Hexafluoride from the Triple Point to 1000 K and up to 150 MPa. J. Phys. Chem. Ref. Data 41(2) (2012) 023104, http://dx.doi.org/10.1063/1.4708620

  42. Assael, M.J., Koutian, A., Huber, M.L., Perkins, R.A.; Reference Correlations of the Thermal Conductivity of Ethene and Propene. J. Phys. Chem. Ref. Data 45(3) (2016) 033104, http://dx.doi.org/10.1063/1.4958984

  43. Assael, M.J., Mihailidou, E., Huber, M.L., Perkins, R.A.; Reference Correlation of the Thermal Conductivity of Benzene from the Triple Point to 725 K and up to 500 MPa. J. Phys. Chem. Ref. Data 41(4) (2012) 043102, http://dx.doi.org/10.1063/1.4755781

  44. Assael, M.J., Monogenidou, S.A., Huber, M.L., Perkins, R.A., Sengers, J.V.; New International Formulation for the Viscosity of Heavy Water. J. Phys. Chem. Ref. Data 50(3) (2021) 033102, http://dx.doi.org/10.1063/5.0048711

  45. Assael, M.J., Mylona, S.K., Huber, M.L., Perkins, R.A.; Reference Correlation of the Thermal Conductivity of Toluene from the Triple Point to 1000 K and up to 1000 MPa. J. Phys. Chem. Ref. Data 41(2) (2012) 023101, http://dx.doi.org/10.1063/1.3700155

  46. Assael, M.J., Mylona, S.K., Tsiglifisi, Ch.A., Huber, M.L., Perkins, R.A.; Reference Correlation of the Thermal Conductivity of n-Hexane from the Triple Point to 600 K and up to 500 MPa. J. Phys. Chem. Ref. Data 42(1) (2013) 013106, http://dx.doi.org/10.1063/1.4793335

  47. Assael, M.J., Papalas, T.B., Huber, M.L.; Reference Correlations for the Viscosity and Thermal Conductivity of n-Undecane. J. Phys. Chem. Ref. Data 46(3) (2017) 033103, http://dx.doi.org/10.1063/1.4996885

  48. Assael, M.J., Sykioti, E.A., Huber, M.L., Perkins, R.A.; Reference Correlation of the Thermal Conductivity of Ethanol from the Triple Point to 600 K and up to 245 MPa. J. Phys. Chem. Ref. Data 42(2) (2013) 023102, http://dx.doi.org/10.1063/1.4797368

  49. Astina, I.M., Budiarso, G., Harrison, R.; New Helmholtz Equation of State for HFO-1234ze(E) with Comprehensive Assessment. Fluid Phase Equilibria 531 (2021) 112921, http://dx.doi.org/10.1016/j.fluid.2020.112921

  50. Astina, I.M., Firmansyah, J.; Thermodynamic Property Model of Wide-Fluid Phase Propane. ITB J.Eng.Sci. 39(1) (2007) 43-65, http://dx.doi.org/10.5614/itbj.eng.sci.2007.39.1.4

  51. Astina, I.M., Sato, H.; A Rational Helmholtz Fundamental Equation of State for Difluoromethane with an Intermolecular Potential Background. Int. J. Thermophys. 24(4) (2003) 963-990, http://dx.doi.org/10.1023/A:1025096716493

  52. Astina, I.M., Sato, H.; A Rational Fundamental Equation of State for Pentafluoroethane with Theoretical and Experimental Bases. Int. J. Thermophys., 25(1) (2004) 113-131, http://dx.doi.org/10.1023/B:IJOT.0000022330.46522.68

  53. Astina, I.M., Sato, H.; A Fundamental Equation of State for 1,1,1,2-tetrafluoroethane with an Intermolecular Potential Energy Background and Relialbe Ideal-Gas Properties. Fluid Phase Equilib., 221 (2004) 103-111, http://dx.doi.org/10.1016/j.fluid.2004.03.004

  54. Astina, I.M., Sato, H.; A Rigorous Thermodynamic Property Model for Fluid-Phase 1,1-Difluoroethane (R-152a). Int. J. Thermophys., 25(6) (2004) 1713-1733, http://dx.doi.org/10.1007/s10765-004-7731-8

  55. ASTM; Annual Book of Standards. ASTM International, West Conshohocken, PA, 2002

  56. ASTM D2161-05; Standard Practice for Conversion of Kinematic Viscosity to Saybolt Universal Viscosity or to Saybolt Furol Viscosity. ASTM International, West Conshohocken, PA 2005, www.astm.org, http://dx.doi.org/10.1520/D2161-05

  57. Avci, A., Karagoz, I.; A Novel Explicit Equation for Friction Factor in Smooth andRough Pipes. J. Fluids Eng 131(6) (2009) 061203, http://dx.doi.org/10.1115/1.3129132

  58. Avgeri, S., Assael, M.J., Huber, M.L., Perkins, R.A; Reference Correlation of the Viscosity of Benzene from the Triple Point to 675K and up to 300MPa. J. Phys. Chem. Ref. Data 43 (2014) 033103, http://dx.doi.org/10.1063/1.4892935

  59. Avgeri, S., Assael, M.J., Huber, M.L., Perkins, R.A.; Reference Correlation of the Viscosity of Toluene from the Triple Point to 675 K and up to 500 MPa. J. Phys. Chem. Ref. Data 44(3) (2015) 033101, http://dx.doi.org/10.1063/1.4926955

  60. Azizi N, Behbahani R, Isazadeh M A.; An efficient correlation for calculating compressibility factor of natural gases. Journal of Natural Gas Chemistry 19 (2010) 642-645, http://dx.doi.org/10.1016/s1003-9953(09)60081-5

  61. Aznar, M., Silva Telles, A.; A Data Bank of Parameters for the Attractive Coefficient of the Peng-Robinson Equation of State. Braz. J. Chem. Eng. 14(1) (1997), http://dx.doi.org/10.1590/S0104-66321997000100003

  62. Baehr, H.D., Tillner-Roth, R.; Thermodynamic Properties of Environmentally Acceptable Refrigerants: Equations of State and Tables for Ammonia, R22, R134a, R152a, and R123. Springer-Verlag, Berlin, 1994., http://dx.doi.org/10.1007/978-3-642-79400-1

  63. Bahadori, A., Mokhatab, S., Towler, B.F.; Rapidly estimating natural gas compressibility factor. J. Nat. Gas Chem. 16 (4) 2007, 349-353., http://dx.doi.org/10.1016/s1003-9953(08)60003-1

  64. Balogun, B., Riesco, N., Vesovic, V.; Reference Correlation of the Viscosity of para-Xylene from the Triple Point to 673K and up to 110 MPa. J. Phys. Chem. Ref. Data 44(1) (2015) 013103, http://dx.doi.org/10.1063/1.4908048

  65. Barati, R., Neyshabouri, S.A.A.S, Ahmadi, G.; Development of Empirical Models with High Accuracy for Estimation of Drag Coefficient of Flow around a Smooth Sphere: An Evolutionary Approach. Powder Technology 257 (2014) 11-19, http://dx.doi.org/10.1016/j.powtec.2014.02.045

  66. Barr, D.I.H.; Solutions of the Colebrook-White functions for resistance to uniform turbulent flows.. Proc Inst Civil Eng 71, 1981, 529-536., http://dx.doi.org/10.1680/iicep.1981.1895

  67. Barreiros, S.F., Calado, J.C.G., Nunes da Ponte, M.; The melting curve of carbon monoxide. J. Chem. Thermodynamics 14 (1982) 1197-1198, http://dx.doi.org/10.1016/0021-9614(82)90044-1

  68. Barua, S.N.; On Secondary Flow in Stationary Curved Pipes. Quart. J. Mech. Appl. Math. 16(1) (1963) 61-77, http://dx.doi.org/10.1093/qjmam_16.1.61

  69. Bas, H., Ozceyhan, V.; Heat transfer enhancement in a tube with twisted tape inserts placed separately from the tube wall. Exp. Thermal Fluid Sci. 41 (2012) 51-58, http://dx.doi.org/10.1016/j.expthermflusci.2012.03.008

  70. Beckmüller, R., Span, R., Lemmon, E.W., Thol, M.; A Fundamental Equation of State for the Calculation of Themodynamic Properties of n-Octane. J. Phys. Chem. Ref. Data 51 (2022) 043103, http://dx.doi.org/10.1063/5.0104661

  71. Bell, I.H., Jäger, A.; Helmholtz Energy Transformations of Common Cubic Equations of State for Use with Pure Fluids and Mixtures. J. Res. of NIST 121 (2016) 236-263, http://dx.doi.org/10.6028/jres.121.011

  72. Bell, I.H., Wronski, J., Quoilin, S., Lemort, V.; Pure and Pseudo-pure Fluid Thermophysical PropertyEvaluation and the Open-Source Thermophysical PropertyLibrary CoolProp. Ind. Eng. Chem. Res. 53(6) (2014) 2498-2508, http://dx.doi.org/10.1021/ie4033999

  73. Bender, E.; Equation of state of normal hydrogen in the range 18 to 700 K and 1 to 500 bar. VDI-Forschungsheft, no. 609, 1982, p. 15-20

  74. Bergman, D.F., Tek, M.R., Katz, D.L.; Retrograde Condensation in Natural Gas Pipelines. Project PR 2-29 of Pipelines Research Committee, AGA, January 1977

  75. Bergman, T.L., Lavine, A.S., Incropera, F.P., DeWitt, D.P.; Introduction to Heat Transfer. 6th Ed.. Wiley, 2011.

  76. Betken, B., Beckmüller, R., Javed, M.A., Baumhögger, E., Span, R. Vrabec, J., Thol, M.; Thermodynamic properties fo 1-hexene - Measurements and Modeling. J. Chem. Thermo., 176 (2023) 106881, http://dx.doi.org/10.1016/j.jct.2022.106881

  77. Bhattacharjee, J.K., Ferrell, R.A., Basu, R.S., Sengers, J.V.; Crossover function for the critical viscosity of a classical fluid. Physical Review A 24(3) (1981) 1469-1475, http://dx.doi.org/10.1103/PhysRevA.24.1469

  78. Bhirud, V.L.; Saturated Liquid Densities of Normal Fluids. AIChE Journal 24(6) (1978) 1127-1131, http://dx.doi.org/10.1002/aic.690240630

  79. Blackham, T.M., Lemmon, E.W.; to be published in Int. J. Thermophys., 2011.

  80. Boston, J.F., Mathias, P.M.; Phase Equilibria in a Third-Generation Process Simulator. Presented at: ‘Phase Equilibria and Fluid Properties in the Chemical Industries’, Berlin, March 17-21, 1980.

  81. Brill, J.P., Beggs, H.D.; Two-Phase Flow in Pipes. University of Tulsa, INTERCOMP Course, The Hague, 1974

  82. Brkić, D.; An Explicit Approximation of Colebrook’s equation for fluidflow friction factor. Petroleum Science and Technology 29 (15): 1596–1602. , http://dx.doi.org/10.1080/10916461003620453

  83. Brock, J.R., Bird, R.B.; Surface Tension and the Principle of Corresponding States. AIChE Journal 1(2) (1955) 174-177, http://dx.doi.org/10.1002/aic.690010208

  84. Brokaw, R.S.; Predicting Transport Properties of Dilute Gases. I&EC Process Design and Development 8(22) (1969) 240-253, http://dx.doi.org/10.1021/i260030a015

  85. Brown, P.P., Lawler, D.F.; Sphere Drag and Settling Velocity Revisited. J. Env. Eng. 129(3) (2003) 222-231, http://dx.doi.org/10.1061/(ASCE)0733-9372(2003)129:3(222)

  86. Brulé, M.R., Starling, K.E.; Thermophysical Properties of Complex Systems: Applications of Multiproperty Analysis. Ind. Eng. Chem. Process Dev. 23 (1984) 833-845, http://dx.doi.org/10.1021/i200027a035

  87. Burnett, R.R.; Calculator gives compressibility factors. Oil & Gas Journal, June 11, 1979, pp. 70-74.

  88. Buzzelli, D.; Calculating friction in one step. Machine Design, 80 (2008), 54–55.

  89. Bücker, D., Wagner, W.; A Reference Equation of State for the Thermodynamic Properties of Ethane for Temperatures from the Melting Line to 675 K and Pressures up to 900 MPa. J. Phys. Chem. Ref. Data 35(1) (2006) 205-266, http://dx.doi.org/10.1063/1.1859286

  90. Bücker, D., Wagner, W.; Reference Equations of State for the Thermodynamic Properties of Fluid Phase n-Butane and Isobutane. J. Phys. Chem. Ref. Data 35(2) (2006) 929-1019, http://dx.doi.org/10.1063/1.1901687

  91. Calvert, S., Lundgren, D., Mehta, D.S.; Venturi Scrubber Performance. J. Air Pollution Control Assoc., 22(7) (1972) 529-532, http://dx.doi.org/10.1080/00022470.1972.10469674

  92. Cao, F.L., Meng, X.Y., Wu, J.T., Vesovic, V.; Reference Correlation of the Viscosity of ortho-Xylene from 273 to 673 K and up to 110 MPa. J. Phys. Chem. Ref. Data 45(2) (2016) 023102, http://dx.doi.org/10.1063/1.4945663

  93. Cao, F.L., Meng, X.Y., Wu, J.T., Vesovic, V.; Reference Correlation of the Viscosity of meta-Xylene from 273 to 673 K and up to 110 MPa. J. Phys. Chem. Ref. Data 45(1) (2016) 013103, http://dx.doi.org/10.1063/1.4941241

  94. Capes, C.E., Nakamura, K.; Vertical Pneumatic Conveying: An Experimental Study with Particles in the Intermediate and Turbulent Flow Regimes. Can. J. Chem. Eng. 51(1) (1973) 31-38, http://dx.doi.org/10.1002/cjce.5450510106

  95. Cavett, R.H.; Physical data for distillation calculations, vapor-liquidequilibrium.. Proceedings of the 27th Meeting, API, San Francisco, Issue 3,351-366.

  96. Ceylan, K., Altunbaş, A., Kelbaliyev, G.; A New Model for Estimation of Drag Force in the Flow of Newtonian Fluids around Rigid or Deformable Particles. Powder Technology 119 (2001) 250-56, http://dx.doi.org/10.1016/s0032-5910(01)00261-3

  97. Chang, C.H., Zhao, X.M.; A New Generalized Equation for Predicting Volume of Compressed Liquids. Fluid Phase Equilibria, 58 (1990) 231-238, http://dx.doi.org/10.1016/0378-3812(90)85134-v

  98. Chang, S.W., Guo, M.H.; Thermal perfomances of enhanced smooth and spiky twisted tapes for laminar and turbulent tubular flows. Int. J. Heat Mass Transfer 55(25-26) (2012) 7651-7667, http://dx.doi.org/10.1016/j.ijheatmasstransfer.2012.07.077

  99. Chang, S.W., Jan, Y.J., Liou, J.S.; Turbulent heat transfer and pressure drop in tube fittedwith serrated twisted tape. Int. J. Thermal Sci. 46(5) (2007) 506-518, http://dx.doi.org/10.1016/j.ijthermalsci.2006.07.009

  100. Chang, S.W., Yang, T.L., Liou, J.S.; Heat transfer and pressure drop in tube with broken twisted tape insert. Exp. Thermal Fluid Sci. 32(2) (2007) 489-501, http://dx.doi.org/10.1016/j.expthermflusci.2007.06.002

  101. Chankalani, A., Mae’soumi, A., Sameni, A.; An Intelligent Approach for Optimal Prediction of Gas Deviation Factor Using Particle Swarm Optimization and Genetic Algorithm. Journal of Natural Gas Science and Engineering 14(2013) 132-143, http://dx.doi.org/10.1016/j.jngse.2013.06.002

  102. Chao, K.C., Seader, J.D.; A General Correlation of Vapor-Liquid Equilibria in Hydrocarbon Mixtures. AIChE J. 7(4) (1961) 598-605, http://dx.doi.org/10.1002/aic.690070414

  103. Chen, H.J.; An Explicit Equation for Friction Factor in Pipe. Ind. Eng. Chem. Fundam. 18(3) (1979) 296-297, http://dx.doi.org/10.1021/i160071a019

  104. Chen, H.J.; An Exact Solution to the Colebrook Equation. Chem. Eng. 94(2) (1987) 196-198

  105. Cheng, N.-S.; Comparison of Formulas for Drag Coefficient and Settling Velocity of Spherical Particles. Powder Technology 189(3) (2009) 395-398, http://dx.doi.org/10.1016/j.powtec.2008.07.006

  106. Chueh, P.L., Prausnitz, J.M.; Vapor-Liquid Equilibria at High Pressures: Calculation of Partial Molar Volumes in Nonpolar Liquid Mixtures. AIChE Journal 13(6) (1967) 1099-1107, http://dx.doi.org/10.1002/aic.690130612

  107. Chueh, P.L., Prausnitz, J.M.; Vapor-Liquid Equilibria at High Pressures: Calculation of Critical Temperatures, Volumes and Pressures of Nonpolar Mixtures. AIChE Journal 13(6) (1967) 1107-1113, http://dx.doi.org/10.1002/aic.690130613

  108. Chung, T.H., Ajlan, M., Lee, L.L., Starling, K.E.; Generalized Multiparameter Correlation for Nonpolar and Polar Fluid Transport Properties. Ind. Eng. Chem. Res. 27(4) (1988) 671-679, http://dx.doi.org/10.1021/ie00076a024

  109. Chung, T.H., Lee, L.L., Starling, K.E.; Applications of Kinetic Gas Theories and Multiparameter Correlation for Prediction of Dilute Gas Viscosity and Thermal Conductivity. Ind. Eng. Chem. Fundam. 23(1) (1984) 8-13, http://dx.doi.org/10.1021/i100013a002

  110. Churchill, S.W.; Friction-factor equation spans all fluid-flow regimes. Chem. Eng. 84 (1977) 94-95

  111. Churchill, S.W., Chu, H.H.S.; Correlating Equations for Laminar and Turbulent Free Convection from a Vertical Plate. Int. J. Heat Mass Transfer 18(11) (1975) 1323-29, http://dx.doi.org/10.1016/0017-9310(75)90243-4

  112. Ciencolini, A., Santini, L.; An experimental investigation regarding the laminar to turbulent flow transition in helically coiled pipes. Exp. Thermal Fluid Sci. 30 (2006) 367-380, http://dx.doi.org/10.1016/j.expthermflusci.2005.08.005

  113. Clift, R., Grace, J.R., Weber, M.E.; Bubbles, Drops, and Particles. Academic Press, 1978.

  114. Coetzee, H., Liebenberg, L., Meyer, J.P.; Heat Transfer and Pressure Drop Characteristics of Angled Spiraling Tape Inserts in a Heat Exchanger Annulus. Heat Transfer Engineering 24(6) (2003) 29-39, http://dx.doi.org/10.1080/714044412

  115. Colebrook, C.F., White, C.M.; Experiments with Fluid Friction in Roughened Pipes. Proc. R. Soc. Lond. A 161 (1937) 367-381., http://dx.doi.org/10.1098/rspa.1937.0150

  116. Collins, W.M., Dennis, S.C.R.; The Steady Motion of a Viscous Fluid in a Curved Tube. Q. J. Mech. Appl. Math. 28(2) (1975) 133-156, http://dx.doi.org/10.1093/qjmam_28.2.133

  117. Colonna, P., Nannan, N.R., Guardone, A.; Multiparameter equations of state for siloxanes: [(CH3)3-Si-O1/2]2-[O-Si-(CH3)2]i=1,…,3, and [O-Si-(CH3)2]6. Fluid Phase Equilibria 263:115-130, 2008, http://dx.doi.org/10.1016/j.fluid.2007.10.001

  118. Colonna, P., Nannan, N.R., Guardone, A., Lemmon, E.W.; Multiparameter Equations of State for Selected Siloxanes. Fluid Phase Equilibria, 244 (2006) 193-211, http://dx.doi.org/10.1016/j.fluid.2006.04.015

  119. Concha, F., Barrientos, A.; Settling Velocities of Particulate Systems, 3. Power Series Expansion for the Drag Coefficient of A Sphere and Prediction of the Settling Velocity. Int. J. Miner. Process. 9 (1982) 167-172, http://dx.doi.org/10.1016/0301-7516(82)90025-4

  120. Constantinou, L., Gani, R.; New Group Controbution Method for Estimating Properties of Pure Compounds. AIChE J. 40(10) (1994) 1697-1710, http://dx.doi.org/10.1002/aic.690401011

  121. Constantinou, L., Gani, R., O’Connell, J.P.; Estimation of the Acentric Factor and the Liquid Molar Volume at 298K Using a New Group Contribution Method. Fluid Phase Equilibria 103 (1995) 11-22, http://dx.doi.org/10.1016/0378-3812(94)02593-p

  122. Coquelet, C., Chapoy, A., Richon, D.; Development of a New Alpha Function for the Peng-Robinson Equation of State: Comparative Study of Alpha Function Models for Pure Gases (Natural Gas Components) and Water-Gas Systems. Int. J. Thermophys. 25(1) (2004) 133-158, http://dx.doi.org/10.1023/b_ijot.0000022331.46865.2f

  123. Crane; Flow of Fluids Through Valves, Fittings, and Pipe. Crane CO, 1982

  124. Crookston, R.B., Rothfus, R.R., Kermode, R.I.; Turbulent Heat Transfer in Annuli with Small Cores. Int. J. Heat Mass Transfer 11(3) (1968) 415-426, http://dx.doi.org/10.1016/0017-9310(68)90086-0

  125. Cui, J., Yan, S., Bi, S., Wu, J.; Saturated Liquid Dynamic Viscosity and Surface Tension of trans-1-Chloro-3,3,3-trifluropropene and Dodecafluoro-2-methylpentan-3-one. J. Chem. Eng. Data 63(3) (2018) 751-756, http://dx.doi.org/10.1063/1.4848698

  126. Cui, J.W., Gao, K.H., Wu, J.T.; Reference Correlation of the Viscosity of n-Propyl Alcohol from 153 to 618 K and up to 118 MPa. J. Phys. Chem. Ref. Data 54(3) (2025) 033106, http://dx.doi.org/10.1063/5.0280205

  127. Czop, V., Barbier, D., Dong, S.; Pressure drop, void fraction and shear stress measurements in an adiabatic two-phase flow in a coiled tube. Nuclear Eng. Design 149 (1994) 323-333, http://dx.doi.org/10.1016/0029-5493(94)90298-4

  128. Darby, R., Chhabra, R.P.; Chemical Engineering Fluid Mechanics, 3rd Edition. CRC Press, 2017

  129. Datchi, F., Loubeyre, P., LeToullec, R.; Extended and accuracy determination of the melting curves of argon, helium, ice (H2O), and hydrogen (H2). Physical Review B, 61(10) (2000) 6535-6546, http://dx.doi.org/10.1103/PhysRevB.61.6535

  130. Date, A.W., Gaitonde, U.N.; Development of Correlations for Predicting Characteristics of Laminar Flow in a Tube Fitted with Regularly Spaced Twisted-Tape Elements. Exp. Thermal Fluid Sci. 3(4) (1990) 373-382, http://dx.doi.org/10.1016/0894-1777(90)90035-6

  131. Daubert, T.E.; Petroleum Fraction Distillation Interconversion. Hydrocarbon Processing 73(9) (1994) 75-78

  132. de Reuck, K.M.; International thermodynamic tables of the fluid state: Vol. 11 - fluorine. Pergamon Press, Oxford, 1990.

  133. de Reuck, K.M., Craven, R.J.B.; Methanol, International Thermodynamic Tables of the Fluid State - 12. IUPAC, Blackwell Scientific Publications, London, 1993.

  134. de Reuck, K.M., Craven, R.J.B., Cole, W.A.; Report on the Development of an Equation of State for Sulphur Hexafluoride. IUPAC Thermodynamic Tables Project Centre, 1991.

  135. de Visscher, A.; Air Dispersion Modeling: Foundations and Applications. John Wiley & Sons, 2014

  136. de Vries, B., Tillner-Roth, R., Baehr, H.D.; Thermodynamic Properties of HCFC 124,. 19th International Congress of Refrigeration, The Hague, The Netherlands, IIR, IVa:582-589, 1995

  137. Dean, D.E., Stiel, L.I.; The Viscosity of Nonpolar Gas Mixtures at Moderate and High Pressures. AIChE Journal 11(3) (1965) 526-532 , http://dx.doi.org/10.1002/aic.690110330

  138. Dean, W.R.; The stream-line motion of fluid in a curved pipe (Second paper). London Edinburgh Dublin Phil. Mag. J. Sci. Serie 7 5(30) (1928) 673-695, http://dx.doi.org/10.1080/14786440408564513

  139. Dennis, S.C.R.; Calculation of the steady flow through a curved tube using a new finite-difference method. J. Fluid Mech. 99(3) (1980) 449-467, http://dx.doi.org/10.1017/S0022112080000705

  140. Di Nicola, G., Ciarrocchi, E., Coccia, G., Pierantozzi, M.; Correlations of Thermal Conductivity for Liquid Refrigerants at Atmospheric Pressure or near Saturation. International Journal of Refrigeration, 2014, http://dx.doi.org/10.1016/j.ijrefrig.2014.06.003

  141. Dillon, H.E., Penoncello, S.G.; A Fundamental Equation for Calculation of the Thermodynamic Properties of Ethanol. Int. J. Thermophys., 25(2) (2004) 321-335, http://dx.doi.org/10.1023/B:IJOT.0000028470.49774.14

  142. Dirker, J., Meyer, J.P.; Convective Heat Transfer Coefficients in Concentric Annuli. Heat Transfer Eng. 26(2) (2005) 38-44, http://dx.doi.org/10.1080/01457630590897097

  143. Dong, Y., Huixiong, L., Tingkuan, C.; Pressure drop, heat transfer and performance of single-phase turbulent flow in spirally corrugated tubes. Exp. Thermal Fluid Sci. 24(3-4) (2001) 131-138, http://dx.doi.org/10.1016/S0894-1777(01)00047-4

  144. Dranchuk, P.M., Abu-Kassem, J.H.; Calculate of Z factors for Natural Gases Using Equations of State. Journal of Canadian Petroleum Technology (July–September 1975): 34-36, http://dx.doi.org/10.2118/75-03-03

  145. Dranchuk, P.M., Purvis, R.A., Robinson, D.B.; Computer Calculations of Natural Gas Compressibility Factors Using the Standing and Katz Correlation. Technical Series, no. IP 74–008. Institute of Petroleum, Alberta, Canada, 1974., http://dx.doi.org/10.2118/73-112

  146. Dranchuk, P.M., Quon, D.; A General Solution of the Equations Describing Steady StateTurbulent Compressible Flow in Circular Conduits. Journal of Canadian Petroleum Technology 3(2):60-65, 1964, http://dx.doi.org/10.2118/64-02-04

  147. Dravid, A.N., Smith, K.A., Merrill, E.W., Brian, P.L.T.; Effect of Secondary Fluid Motion on Laminar Flow Heat Transfer in Helically Coiled Tubes. AIChE J. 17(5) (1971) 1114-1122, http://dx.doi.org/10.1002/aic.690170517

  148. du Plessis, J.P., Kröger, D.G.; Friction factor prediction for fully developed laminar twisted-tape flow. Int. J. Heat Mass Transfer 27(11) (1984) 2095-2100, http://dx.doi.org/10.1016/0017-9310(84)90196-0

  149. du Plessis, J.P., Kröger, D.G.; Heat transfer correlation for thermally developing laminar flow in a smooth tube with a twisted-tape insert. Int. J. Heat Mass Transfer 30(3) (1987) 509-515, http://dx.doi.org/10.1016/0017-9310(87)90265-1

  150. Dymond, J.H., Marsh, K.N., Wilhoit, R.C., Wong, K.C., Frenkel, M.; Virial Coefficients of Pure Gases (Landolt-Börnstein - Group IV Physical Chemistry 21A). Springer-Verlag, http://dx.doi.org/10.1007/10693952_16

  151. Dymond, J.H., Marsh, K.N., Wilhoit, R.C., Wong, K.C., Frenkel, M.; Virial Coefficients of Mixtures (Landolt-Börnstein - Group IV Physical Chemistry 21B). Springer-Verlag, http://dx.doi.org/10.1007/10754889

  152. Eck, B.; Technische Stromungslehre. Springer, New York, 1973.

  153. Edmister, W.C.; Applied Hydrocarbon Thermodynamics, Part 4, CompressibilityFactors and Equations of State. Petroleum Refiner. 37 (April, 1958), 173–179

  154. Edmister, W.C., Okamoto, K.K.; Applied Hydrocarbon Thermodynamics, Part 13: Equilibrium Flash Vaporization Correlations for Heavy Oils Under Subatmospheric Pressures. Petroleum Refiner 38(9) (1959) 271-288

  155. Edwards, T.J., Newman, J., Prausnitz, J.M.; Thermodynamics of Aqueous Solutions Containing Volatile Weak Electrolytes. AIChE Journal 21(2) (1975) 248-259, http://dx.doi.org/10.1002/aic.690210205

  156. Eiamsa-ard, P., Piriyarungrod, N., Thianpong, C., Eiamsa-ard, S.; A case study on thermal performance assessment of a heat exchanger tube equipped with regularly-spaced twisted tapes as swirl generators. Case Studies Thermal Eng. 3 (2014) 86-102, http://dx.doi.org/10.1016/j.csite.2014.04.002

  157. Eiamsa-ard, S., Promvonge, P.; Performance assessment in a heat exchanger tube with alternate clockwise and counter-clockwise twisted-tape inserts. Int. J. Heat Mass Transfer 53(7-8) (2010) 1364-1372, http://dx.doi.org/10.1016/j.ijheatmasstransfer.2009.12.023

  158. Eiamsa-ard, S., Promvonge, P.; Thermal characteristics in round tube fitted with serrated twisted tape. Applied Thermal Engineering 30(13) (2010) 1673-1682, http://dx.doi.org/10.1016/j.applthermaleng.2010.03.026

  159. Eiamsa-ard, S., Promvonge, P.; Influence of Double-sided Delta-wing Tape Insert with Alternate-axes on Flow and Heat Transfer Characteristics in a Heat Exchanger Tube. Chinese J. Chem. Eng. 19(3) (2011) 410-423, http://dx.doi.org/10.1016/S1004-9541(11)60001-3

  160. Eiamsa-ard, S., Seemawute, P., Wongcharee, K.; Influences of peripherally-cut twisted tape insert on heat transfer and thermal performance characteristics in laminar and turbulent tube flows. Exp. Thermal Fluid Sci. 34(6) (2010) 711-719, http://dx.doi.org/10.1016/j.expthermflusci.2009.12.013

  161. Eiamsa-ard, S., Somkleang, P., Nuntadusit, C., Thianpong, C.; Heat transfer enhancement in tube by inserting uniform/non-uniform twisted-tapes with alternate axes: Effect of rotated-axis length. Applied Thermal Eng. 54 (2013) 289-309, http://dx.doi.org/10.1016/j.applthermaleng.2013.01.041

  162. Eiamsa-ard, S., Thianpong, C., Eiamsa-ard, P.; Turbulent heat transfer enhancement by counter/co-swirling flow in a tube fitted with twin twisted tapes. Exp. Thermal Fluid Sci. 34(1) (2010) 53-62, http://dx.doi.org/10.1016/j.expthermflusci.2009.09.002

  163. Eiamsa-ard, S., Thianpong, C., Eiamsa-ard, P., Promvonge, P.; Thermal characteristics in a heat exchanger tube fitted with dual twisted tape elements in tandem. Int. Comm. Heat Mass Transfer 37(1) (2010) 39-46, http://dx.doi.org/10.1016/j.icheatmasstransfer.2009.08.010

  164. Eiamsa-ard, S., Wongcharee, K.,; Heat transfer enhancement by twisted tapes with alternate-axes and triangular, rectangular and trapezoidal wings. Chem. Eng. Processing 50(2) (2011) 211-219, http://dx.doi.org/10.1016/j.cep.2010.11.012

  165. Eiamsa-ard, S., Wongcharee, K., Eiamsa-ard, P., Thianpong, C.; Heat transfer enhancement in a tube using delta-winglet twisted tape inserts. Applied Thermal Eng. 30(4) (2010) 310-318, http://dx.doi.org/10.1016/j.applthermaleng.2009.09.006

  166. Eiamsa-ard, S., Wongcharee, K., Eiamsa-ard, P., Thianpong, C.; Thermohydraulic investigation of turbulent flow through a round tube equipped with twisted tapes consisting of centre wings and alternate-axes. Exp. Thermal Fluid Sci. 34(8) (2010) 1151-1161, http://dx.doi.org/10.1016/j.expthermflusci.2010.04.004

  167. Eisenbach, T., Scholz, C., Span, R., Cristancho, D., Lemmon, E.W., Thol, M.; Speed-of-Sound Measurements and a Fundamental Equation of State for Propylene Glycol. J. Phys. Chem. Ref. Data 50(2) (2021) 023105, http://dx.doi.org/10.1063/5.0050021

  168. El-Genk, M.S., Timothy, M.S.; A Review and Correlations for Convection Heat Transfer and Pressure Losses in Toroidal and Helically Coiled Tubes. Heat Transfer Eng. 38(5) (2017) 447-474, http://dx.doi.org/10.1080/01457632.2016.1194693

  169. Elsharkawy, A.M.; Efficient methods for calculations of compressibility, density and viscosity of natural gases. Fluid Phase Equilibria 218:1 (2004) 1-13, http://dx.doi.org/10.1016/j.fluid.2003.02.003

  170. Ely, J.F.; An Enskog Correction for Size and Mass Difference Effects in Mixture Viscosity Prediction. J. Res. Natl. Bur. Stand. 86(6) (1981) 597-604, http://dx.doi.org/10.6028/jres.086.028

  171. Ely, J.F., Hanley, H.J.M.; A Computer Program for the Prediction of Viscosity and Thermal Condcutivity in Hydrocarbon Mixtures. NBS Technical Note 1039 (1981)

  172. Ely, J.F., Magee, J.W., Haynes, W.M.; Thermophysical properties for special high CO2 content mixtures. Research Report RR-110, Gas Processors Association, Tulsa, OK, 1987.

  173. Estela-Uribe, J.F.; Fundamental multiparameter and association equation of state for ethanol. Fluid Phase Equilib. 452 (2017) 74-93, http://dx.doi.org/10.1016/j.fluid.2017.08.018

  174. Estela-Uribe, J.F., Trusler, J.P.M.; Extended corresponding states model for fluids and fluidmixtures I. Shape factor model for pure fluids. Fluid Phase Equilibria 204 (2003) 15-40, http://dx.doi.org/10.1016/s0378-3812(02)00190-5

  175. Fang, X,, Xu, Y., Zhou, Z.; New correlations of single-phase friction factor forturbulent pipe flow and evaluation of existing single-phasefriction factor correlations.. Nucl. Eng. Des. 241 (2011) 897-902, http://dx.doi.org/10.1016/j.nucengdes.2010.12.019

  176. Fenghour, A., Wakeham, W.A., Vesovic, V.; The Viscosity of Carbon Dioxide. J. Phys. Chem. Ref. Data 27(1) (1998) 31-44, http://dx.doi.org/10.1063/1.556013

  177. Fenghour, A., Wakeham, W.A., Vesovic, V., Watson, J.T.R., Millat, J., Vogel, E.; The Viscosity of Ammonia. J. Phys. Chem. Ref. Data 24(5) (1995) 1649-1667, http://dx.doi.org/10.1063/1.555961

  178. Fiedler, F., Karog, J., Lemmon, E.W., Thol, M.; Fundamental Equation of State for Fluid Tetrahydrofuran. Int. J. Thermophysics 44 (2023) 153, http://dx.doi.org/10.1007/s10765-023-03258-3

  179. Flemmer, R.L.C., Banks, C.L.; On the Drag Coefficient of a Sphere. Powder Technology 48(3) (1986) 217-221., http://dx.doi.org/10.1016/0032-5910(86)80044-4

  180. Friend, D.G., Ely, J.F., Ingham, H.; Thermophysical Properties of Methane. J. Phys. Chem. Ref. Data 18(2) (1989) 583-638, http://dx.doi.org/10.1063/1.555828

  181. Friend, D.G., Ingham, H., Ely, J.F.; Thermophysical Properties of Ethane. J. Phys. Chem. Ref. Data 20(2) (1991) 275-347, http://dx.doi.org/10.1063/1.555881

  182. Friend, D.G., Ingham, H., Ely, J.F.; Thermophysical Properties of Ethane. J. Phys. Chem. Ref. Data 20, 275 (1991), http://dx.doi.org/10.1063/1.555881

  183. Gao, K., Köster, A., Thol, M., Wu, J., Lemmon, E.W.; Equations of State for the Thermodynamic Properties of n-Perfluorobutane, n-Perfluoropentane, and n-Perfluerohexane. Ind. Eng. Chem. Res. 60(47) (2021) 17207-17227, http://dx.doi.org/10.1021/acs.iecr.1c02969

  184. Gao, K., Wu, J., Bell, I.H., Harvey, A.H., Lemmon E.W.; A Reference Equation of State with an Associating Term for the Thermodynamic Properties of Ammonia. J. Phys. Chem. Ref. Data 52 (2023) 013102, http://dx.doi.org/10.1063/5.0128269

  185. Gao, K., Wu, J., Lemmon, E.W.; Equations of State for the Thermodynamic Properties of Three Hexane Isomers: 3-Methylpantane, 2,2-Dimethylbutane, and 2,3-Dimethylbutane. J. Phys. Chem. Ref. Data 50(3) (2021) 033103, http://dx.doi.org/10.1063/1.5093644

  186. Gao, K., Wu, J., Zhang, P., Lemmon, E.W.; A Helmholtz Energy Equation of State for Sulfur Dioxide. J. Chem. Eng. Data, 61(6) (2016) 2859-2872, http://dx.doi.org/10.1021/acs.jced.6b00195

  187. García, A., Vicente, P.G., Viedma, A.; Experimental study of heat transfer enhancement with wire coil inserts in laminar-transition-turbulent regimes at different Prandtl numbers. Int. J. Heat Mass Transfer 48(21-22) (2005) 4640-4651, http://dx.doi.org/10.1016/j.ijheatmasstransfer.2005.04.024

  188. Gasem, K.A.M., Gao, W., Pan, R.L., Robinson Jr, R.L.; A modified temperature dependence for the Peng-Robinson equation of state. Fluid Phase Equilibria 181 (2001) 113-125, http://dx.doi.org/10.1016/s0378-3812(01)00488-5

  189. Gedanitz, H., Davila, M.J., Lemmon, E.W.; Speed of Sound Measurements and a Fundamental Equation of State for Cyclopentane. J. Chem. Eng. Data, 60(5) (2015) 1331-1337, http://dx.doi.org/10.1021/je5010164

  190. Geller, V.Z., Nemzer, B.V., Cheremnykh, U.V.; Thermal Conductivity of the Refrigerant Mixtures R404A, R407C, R410A and R507A. Int. J. Termophysics 22(4) (2001) 1035-1043, http://dx.doi.org/10.1023/a_1010691504352

  191. Geller, V.Z., Nemzer, B.V., Cheremnykh, U.V.; Thermal Conductivity of the Refrigerant Mixtures R404A, R407C, R410A and R507A. Int. J. Thermophysics 22(4) (2001) 1035-1043, http://dx.doi.org/10.1023/a_1010691504352

  192. Georgeton, G.K., Smith, R.L.Jr., Teja, A.S; Application of Cubic Equations of State to Polar Fluids and Fluid Mixtures. in Chao, K.C., Robinson, R.L. Equations of State. Theories and Applications, 1985, ACS Svmposium 300, pp. 434-451

  193. Ghanbari, A., Farshad, F., Rieke, H.H.; Newly developed friction factor correlation for pipe flow and flow assurance. J Chem Eng Mat Sci 2 (2011), 83-86.

  194. Gharagheizi, F., Eslamimanesh, A., Sattari, M., Mohammadi, A.H., Richon, D.; Corresponding States Method for Determination of the Viscosity of Gases at Atmospheric Pressure. I&EC Research 51(7) (2012) 3179-3185, http://dx.doi.org/10.1021/ie202591f

  195. Gharagheizi, F., Ilani-Kashkouli, P., Sattari, M., Mohammadi, A.H., Ramjugernath, D., Richon, D.; Development of a General Model for Determination of Thermal Conductivity of Liquid Chemical Compounds at Atmospheric Pressure. AIChE Journal 59 (2013) 1702-1708, http://dx.doi.org/10.1002/aic.13938

  196. Ghobadi, M., Muzychka, Y.S.; A Review of Heat Transfer and Pressure Drop Correlations for Laminar Flow in Curved Circular Ducts. Heat Transfer Eng. 37(10) (2016) 815-839, http://dx.doi.org/10.1080/01457632.2015.1089735

  197. Gnielinski, V.; Berechnung des Druckverlustes in glatten konzentrischen Ringspalten bei ausgebildeter laminarer und turbulenter isothermer Strömung. Chemie Ingenieur Technik 79(1-2) (2007) 91-95, http://dx.doi.org/10.1002/cite.200600126

  198. Gnielinski, V.; Heat Transfer Coeffients for Turbulent Flow in ConcentricAnnular Ducts. Heat Transfer Eng. 30(6) (2009) 431-436, http://dx.doi.org/10.1080/01457630802528661

  199. Goossens, A.G.; Prediction of the Hydrogen Content of Petroleum Fractions. Ind. Eng. Chem. Res. 36(6) (1997) 2500-2504, http://dx.doi.org/10.1021/ie960772x

  200. Goossens, A.G.; Prediction of Molecular Weight of Petroleum Fractions. Ind. Eng. Chem. Res. 35(3) (1996) 985-988, http://dx.doi.org/10.1021/ie950484l

  201. Gopal, V.N.; Gas Z-Factor Equations Developed for Computer. Oil and Gas J. (Aug. 8, 1977) 58-60

  202. Goudar, C.T., Sonnad J.R.; Comparison of the iterative approximations of the Colebrook-White equation. Hydrocarb. Process. 87 (2008) 79-83

  203. Graboski, M.S., Daubert, T.E.; A Modified Soave Equation of State for Phase Equilibrium Calculations. 1. Hydrocarbon Systems. Ind. Eng. Chem. Process Des. Dev. 17(4) (1978) 443-448, http://dx.doi.org/10.1021/i260068a009

  204. Graboski, M.S., Daubert, T.E.; A Modified Soave Equation of State for Phase Equilibrium Calculations. 2. Systems Containing CO₂, H₂S, N₂ and CO. Ind. Eng. Chem. Process Des. Dev. 17(4) (1978) 448-454, http://dx.doi.org/10.1021/i260068a010

  205. Graboski, M.S., Daubert, T.E.; A Modified Soave Equation of State for Phase Equilibrium Calculations. 3. Systems Containing Hydrogen. Ind. Eng. Chem. Process Des. Dev. 18(2) (1979) 300-306, http://dx.doi.org/10.1021/i260070a022

  206. Grayson, H.G., Streed, C.W.; Vapor-Liquid Equilibria for High Temperature, High Pressure Hydrogen-Hydrocarbon Systems. 6th World Petroleum Congress, Frankfurt am Main, Germany, 19-26 June (1963) 169-181

  207. Guder, C., Wagner, W.; A Reference Equation of State for the Thermodynamic Properties of Sulfur Hexafluoride (SF6) for Temperatures from the Melting Line to 625 K and Pressures up to 150 MPa. J. Phys. Chem. Ref. Data 38(1) (2009) 33-94, http://dx.doi.org/10.1063/1.3037344

  208. Gunes, S., Ozceyhan, V., Buyukalaca, O.; Heat transfer enhancement in a tube with equilateral triangle cross sectioned coiled wire inserts. Exp. Thermal Fluid Sci. 34(6) (2010) 684-691, http://dx.doi.org/10.1016/j.expthermflusci.2009.12.010

  209. Gunn, R.D., Yamada, T.; A Corresponding States Correlation of Saturated Liquid Volumes. AIChE Journal 17(6) (1971) 1341-1345, http://dx.doi.org/10.1002/aic.690170613

  210. Guo, L., Chen, X., Feng, Z., Bai, B.; Transie:nt convective heat transfer in a helical coiled tube with pulsatile fully developed turbulent flow. Int. J. Heat Mass Transfer 41() (1998) 2867-2875, http://dx.doi.org/10.1016/s0017-9310(98)80003-3

  211. Guo, L., Feng, Z, Chen, X.; An experimental investigation of the frictional pressure drop of steam–water two-phase flow in helical coils. Int. J. Heat Mass Transfer 44(14) (2001): 2601-2610, http://dx.doi.org/10.1016/S0017-9310(00)00312-4

  212. Gupte, N.S., Date, A.W.; Friction and Heat Transfer Characteristics of Helical Turbulent Air Flow in Annuli. J. Heat Transfer 111(2) (1989) 337-344, http://dx.doi.org/10.1115/1.3250682

  213. Haaland, S.E.; Simple and explicit formulas for the friction factor inturbulent flow. J. Fluids Eng., 105(1) (1983) 89-90., http://dx.doi.org/10.1115/1.3240948

  214. Haider, A., Levenspiel, O.; Drag Coefficient and Terminal Velocity of Spherical and Nonspherical Particles. Powder Technology 58(1) (1989) 63-70, http://dx.doi.org/10.1016/0032-5910(89)80008-7

  215. Hakim, D.I., Steinberg, D., Stiel, L.I.; Generalized Relationship for the Surface Tension of Polar Fluids. I&EC Fundamentals 10(1) (1971) 174-75., http://dx.doi.org/10.1021/i160037a032

  216. Hall, K.R., Iglesias-Silva, G.A.; Improved equations for the StandingeKatz tables. Hydrocarb. Process 86 (4), 2007. 107-110

  217. Hall, K.R., Yarborough, L.; A New Equation of State for Z-factor Calculations. Oil and Gas Journal (June 18, 1973): 82–92.

  218. Hall, K.R., Yarborough, L.; New Simple Correlation for Predicting Critical Volume. Chemical Engineering (November 1971): 76

  219. Han, M.S., Starling, K.E.; Thermo Data Refined for LPG. Part 14. Mixtures. Hydrocarbon Processing 51(5) (1972) 129

  220. Hands, B.A., Arp, V.D.; A Correlation of Thermal Conductivity Data for Helium. Cryogenics, 21(12) (1981) 697-703, http://dx.doi.org/10.1016/0011-2275(81)90211-3

  221. Hankinson, R.W., Thomson, G.H.; A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE Journal 25(4) (1979) 653-663, http://dx.doi.org/10.1002/aic.690250412

  222. Hanley H.J.M., McCarty, R.D., Haynes, W.M.; The Viscosity and Thermal Conductivity Coefficient for Dense Gaseous and Liquid Argon, Krypton, Xenon, Nitrogen and Oxigen. J. Phys. Chem. Ref. Data 3(4) (1974) 979-1018, http://dx.doi.org/10.1063/1.3253152

  223. Hardik, B.K., Baburajan, P.K., Prabhu, S.V.; Local heat transfer coefficient in helical coils with single phase flow. Int. J. Heat Mass Transf. 89 (2015) 522-538, http://dx.doi.org/10.1016/j.ijheatmasstransfer.2015.05.069

  224. Hart, J., Ellenberger, J., Hamersma, P.J.; Single- and Two-Phase Flow Through Helically Coiled Tubes. Chem. Eng. Sci. 43(4) (1988) 775-783, http://dx.doi.org/10.1016/0009-2509(88)80072-1

  225. Harvey, A.H.; On the Melting Curve of Sulfur Hexafluoride. J. Phys. Chem. Ref. Data 46(4) (2017) 043102, http://dx.doi.org/10.1063/1.5005537

  226. Harvey, A.H., Huang, P.H.; First-Principles Calculation of the Air-Water Second Virial Coefficient. Int. J. Thermophisics 28(2) (2007) 556-565, http://dx.doi.org/10.1007/s10765-007-0197-8

  227. Harvey, A.H., Lemmon, E.W.; Method for Estimating the Dielectric Constant of Natural Gas Mixtures . Int. J. Thermophys. 26(1) (2005) 31-46, http://dx.doi.org/10.1007/s10765-005-2351-5

  228. Harvey, A.H., Mountain, R.D.; Correlations for the Dielectric Constants of H2S, SO2 and SF6. Int. J. Thermophys. 38 (2017) 147, http://dx.doi.org/10.1007/s10765-017-2279-6

  229. Haynes, W.M.; Thermophysical Properties of HCFC Alternatives. NIST, Boulder, Colorado, Final Report for ARTI MCLR Project Number 660-50800, 1996. Pag. A-82

  230. He, Y., Liu, L., Li, P., Ma, L.; Experimental study on Heat transfer enhancement characteristics of tube with cross hollow twisted tape . Applied Thermal Eng. 131 (2018) 743-749, http://dx.doi.org/10.1016/j.applthermaleng.2017.12.029

  231. Heidaryan E, Moghadasi J, Rahimi M.; New correlations to predict natural gas viscosity and compressibility factor.. Journal of Petroleum Science and Engineering 73 (2010):67-72, http://dx.doi.org/10.1016/j.petrol.2010.05.008

  232. Heidaryan, E., Salarabadi, A., Moghadasi, J.; A novel correlation approach for prediction of natural gas compressibility factor.. J. Nat. Gas Chem. 19 (2) 2010, 189–192., http://dx.doi.org/10.1016/s1003-9953(09)60050-5

  233. Henley, E.J., Seader, J.D.; Equilibrium-Stage Separation Operations in Chemical Engineering. John Wiley & Sons, 1981

  234. Herrig, S.; New Helmholtz-Energy Equations of State for Pure Fluids and CCS-Relevant Mixtures. Ph.D. thesis. Bochum: Ruhr-Universität Bochum, 2018.

  235. Herrig, S., Thol, M., Harvey, A.H., Lemmon, E.W.; A Reference Equation of State for Heavy Water. J. Phys. Chem. Ref. Data 47(4) (2018) 043102, http://dx.doi.org/10.1063/1.5053993

  236. Herrmann, S., Hellmann, R., Vogel, E.; Update: Reference Correlation for the Viscosity of Ethane [J. Phys. Chem. Ref. Data 44, 043101 (2015)]. J. Phys. Chem. Ref. Data 44(4) (2015) 043101, http://dx.doi.org/10.1063/1.4930838

  237. Herrmann, S., Kretzschmar, H.-J., Gatley, D.P.; Thermodynamic Properties of Real Moist Air, Dry Air, SteamWater, and Ice. ASHRAE RP-1485

  238. Herrmann, S., Vogel, E.; New Formulation for the Viscosity of n-Butane. J. Phys. Chem. Ref. Data 47(1) (2018) 013104, http://dx.doi.org/10.1063/1.5020802

  239. Herrmann, S., Vogel, E.; New Formulation for the Viscosity of Isobutane. J. Phys. Chem. Ref. Data 47(4) (2018) 043103, http://dx.doi.org/10.1063/1.5057413

  240. Hesketh, H.E.; Fine Particle Collection Efficiency Related to Pressure Drop, Scrubbant and Particle Properties, and Contact Mechanism. J. Air Pollution Control Assoc., 24(10) (1974) 939-942, http://dx.doi.org/10.1080/00022470.1974.10469992

  241. Hill, P.G., MacMillan, R.D.C., Lee, V.; A Fundamental Equation of State for Heavy Water. J. Phys. Chem. Ref. Data 11, 1 (1982), http://dx.doi.org/10.1063/1.555661

  242. Holland, P.M., Eaton, B.E., Hanley, H.J.M.; A Correlation of the Viscosity and Thermal Conductivity Data of Gaseous and Liquid Ethylene. J. Phys. Chem. Ref. Data 12(4) (1983) 917-932, http://dx.doi.org/10.1063/1.555701

  243. Hong, S.W., Bergles, A.E.; Augmenttion of Laminar Flow Heat Transfer in Tubes by Means of Twisted-Tape Inserts. J. Heat Transfer 98(2) (1976) 251-256, http://dx.doi.org/10.1115/1.3450527

  244. Horstmann, S., Jabloniec, A., Krafczyk, J., Fischer, K., Gmehling, J.; PSRK group contribution equation of state: comprehensive revision and extension IV, including critical constants and α-function parameters for 1000 components. Fluid Phase Equilibria 227 (2005) 157-164, http://dx.doi.org/10.1016/j.fluid.2004.11.002

  245. Hougen, O.A., Watson, K.M., Ragatz, R.A.; Chemical Process Principles, 2nd ed.. New York: Wiley, 1959, p. 577.

  246. HTRI Design Manual.

  247. Huber, M.L.; Models for Viscosity, Thermal Conductivity, and Surface Tension of Selected Pure Fluids as Implemented in REFPROP v10.0. NISTIR 8209, http://dx.doi.org/10.6028/NIST.IR.8209

  248. Huber, M.L., Assael, M.J.; Correlation for the Viscosity of 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) and trans-1,3,3,3-tetrafluropropene (R1234ze(E)). Int. J. Refrigeration 71 (2016) 39-45, http://dx.doi.org/10.1016/j.ijrefrig.2016.08.007

  249. Huber, M.L., Bruno, T.J., Chirico, R.D., Diky, V., Kazakov, A.F., Lemmon, E.W., Muzny, C.D., Frenkel, M.; Equations of State on Demand: Application for Surrogate Fuel Development. Int. J. Thermophys. 32(3) (2011) 596-613, http://dx.doi.org/10.1007/s10765-010-0909-3

  250. Huber, M.L., Ely, J.F.; An Equation of State Formulation of the Thermodynamic Properties of R134a (1,1,1,2-Tetrafluoroethane). Int. J. Refrig. 15(6) (1992) 393-400, http://dx.doi.org/10.1016/0140-7007(92)90024-o

  251. Huber, M.L., Kazakov, A.F., Lemmon, E.W.; Equation of State for the Thermodynamic Properties of Trans-1,2-dichloroethene [R-1130(E)]. Int. J. Thermophys. 46 (2025) 76, http://dx.doi.org/10.1007/s10765-025-03535-3

  252. Huber, M.L., Laesecke, A.; Correlation for the Viscosity of Pentafluoroethane (R125) from the Triple Point to 500 K at Pressures up to 60 MPa. Ind. Eng. Chem. Res. 45(12) (2006) 4447-4453, http://dx.doi.org/10.1021/ie051367l

  253. Huber, M.L., Laesecke, A. Xiang, H.W.; Viscosity correlations for minor constituent fluids in natural gas: n-octane, n-nonane and n-decane. Fluid Phase Equilibria 224 (2004) 263-270, http://dx.doi.org/10.1016/j.fluid.2004.07.012

  254. Huber, M.L., Laesecke, A., Perkins, R.A.; Transport Properties of n-Dodecane. Energy & Fuels 18(4) (2004) 968-975., http://dx.doi.org/10.1021/ef034109e

  255. Huber, M.L., Laesecke, A., Perkins, R.A.; Model for the Viscosity and Thermal Conductivity of Refrigerants, Including a New Correlation for the Viscosity of R134a. Ind. Eng. Chem. Res., 42(13) (2003) 3163-3178, http://dx.doi.org/10.1021/ie0300880

  256. Huber, M.L., Lemmon, E.W., Bell, I.H., McLinden, M.O.; The NIST REFPROP Database for Highly Accurate Properties of Industrially Importants Fluids. Ind. Eng. Chem. Res. 61(42) (2022) 15449-15472, http://dx.doi.org/10.1021/acs.iecr.2c01427

  257. Huber, M.L., Lemmon, E.W., Kazakov, A., Ott, L.S., Bruno, T.J.; Model for the Thermodynamic Properties of a Biodiesel Fuel. Energy Fuels, 23 (7) (2009) 3790–3797, http://dx.doi.org/10.1021/ef900159g

  258. Huber, M.L., McLinden, M.O.; Thermodynamic Properties of R134a (1,1,1,2-tetrafluoroethane). International Refrigeration and Air Condictioning Conference, Paper 184, pag. 453-462, 1992.

  259. Huber, M.L., Perkins, R.A.; Thermal conductivity correlations for minor constituent fluids in natural gas: n-octane, n-nonane and n-decane. Fluid Phase Equilibria 227 (2005) 47-55, http://dx.doi.org/10.1016/j.fluid.2004.10.031

  260. Huber, M.L., Perkins, R.A., Assael, M.J., Monogenidou, S.A., Hellmann, R., Sengers, J.V.; New International Formulation for the Thermal Conductivity of Heavy Water. J. Phys. Chem. Ref. Data 51(1) (2022) 013102, http://dx.doi.org/10.1063/5.0084222

  261. Huber, M.L., Perkins, R.A., Friend, D.G., Sengers, J.V., Assael, M.J., Metaxa, I.N., Miyagawa, K., Hellmann, R., Vogel, E.; New International Formulation for the ThermalConductivity of H20. J. Phys. Chem. Ref. Data 41(3) (2012) 033102, http://dx.doi.org/10.1063/1.4738955

  262. Huber, M.L., Perkins, R.A., Lasecke, A., Friend, D.G., Sengers, J.V., Assael, M.J., Metaxa, I.N.,Vogel, E., Mareš, R., Miyagawa, K.; New International Formulation for the Viscosityof H2O. J. Phys. Chem. Ref. Data 38(2) (2009) 101-125, http://dx.doi.org/10.1063/1.3088050

  263. Huber, M.L., Perkins, R.A., Lemmon, E.W.; Reference Correlationo for the Viscosity of Nitrogen from the Triple Point to 1000 K and Pressures up to 2200 MPa. Int. J. Thermophys., 45(10) (2024) 146, http://dx.doi.org/10.1007/s10765-024-03440-1

  264. Huber, M.L., Sykioti, E.A., Assael, M.J., Perkins, R.A.; Reference Correlation of the Thermal Conductivity of Carbon Dioxide from the Triple Point to 1100 K and up to 200 MPa. J. Phys. Chem. Ref. Data 45(1) (2016) 013102, http://dx.doi.org/10.1063/1.4940892

  265. IAPWS; Revised Release on the Surface Tension of Ordynary Water Substance. 2014

  266. IAPWS; Release on the Values of Temperature, Pressure and Density of Ordynary and Heavy Water Substances at their Respectives Critical Points. 1992

  267. IAPWS; Revised Release on Viscosity and Thermal Conductivity of Heavy Water Substance. 2007

  268. IAPWS; Release on Surface Tension of Heavy Water Substance. 1994

  269. IAPWS; Revised Release on the IAPWS Formulation 1995 for the Thermodynamic Properties of Ordinary Water Substance for General and Scientific Use. 2006

  270. IAPWS; Revised Release on the IAPWS Industrial Formulation 1997 for the Thermodynamic Properties of Water and Steam. 2012

  271. IAPWS; Release on the Static Dielectric Constant of Ordinary WaterSubstance for Temperatures from 238 K to 873 K and Pressures up to 1000 MPa. 1997

  272. IAPWS; Release on the Refractive Index of Ordinary Water Substance as a Function of Wavelength, Temperature and Pressure. 1997

  273. IAPWS; Revised Release on the Equation of State 2006 for H2O Ice Ih. 2009

  274. IAPWS; Release on the Ionization Constant of H2O. 2019

  275. IAPWS; Release on the IAPWS Formulation 2008 for the Viscosity of Ordinary Water Substance. 2008

  276. IAPWS; Release on the IAPWS Formulation 2008 for the Thermodynamic Properties of Seawater. 2008

  277. IAPWS; Revised Release on the Pressure along the Melting and Sublimation Curves of Ordinary Water Substance. 2011

  278. IAPWS; Release on the IAPWS Formulation 2011 for the Thermal Conductivity of Ordinary Water Substance. 2011

  279. IAPWS; Release on the IAPWS Formulation 2017 for the Thermodynamic Properties of Heavy Water. 2017

  280. IAPWS; Revised Supplementary Release on Saturation Properties of Ordinary Water Substance. 1992

  281. IAPWS; Revised Supplementary Release on Backward Equations for Pressure as a Function of Enthalpy and Entropy p(h,s) for Regions 1 and 2 of the IAPWS Industrial Formulation 1997 for the Thermodynamic Properties of Water and Steam. 2014

  282. IAPWS; Revised Supplementary Release on Backward Equations for the Functions T(p,h), v(p,h), and T(p,s), v(p,s) for Region 3 of the IAPWS Industrial Formulation 1997 for the Thermodynamic Properties of Water and Steam. 2014

  283. IAPWS; Revised Supplementary Release on Backward Equations p(h,s) for Region 3, Equations as a Function of h and s for the Region Boundaries, and an Equation Tsat(h,s) for Region 4 of the IAPWS Industrial Formulation 1997 for the Thermodynamic Properties of Water and Steam. 2014

  284. IAPWS; Revised Supplementary Release on Backward Equations for Specific Volume as a Function of Pressure and Temperature v(p,T) for Region 3 of the IAPWS Industrial Formulation 1997 for the Thermodynamic Properties of Water and Steam. 2016

  285. IAPWS; Revised Supplementary Release on Properties of Liquid Water at 0.1 MPa. 2011

  286. IAPWS; Supplementary Release on a Computationally Efficient Thermodynamic Formulation for Liquid Water for Oceanographic Use. 2009

  287. IAPWS; Electrolytic Conductivity (Specific Conductance) of Liquid and Dense Supercritical Water from 0°C to 800°C and Pressures up to 1000 MPa. 1990

  288. IAPWS; Solubility of Sodium Sulfate in Aqueous Mixtures of Sodium Chloride and Sulfuric Acid from Water to Concentrated Solutions, from 250 °C to 350 °C. 1994

  289. IAPWS; Revised Guideline on the Critical Locus of Aqueous Solutions of Sodium Chloride. 2012

  290. IAPWS; Guideline on the IAPWS Formulation 2001 for the Thermodynamic Properties of Ammonia-Water Mixtures. 2001

  291. IAPWS; Guideline on the Use of Fundamental Physical Constants and Basic Constants of Water. 2016

  292. IAPWS; Guideline on the Henry’s Constant and Vapor-Liquid Distribution Constant for Gases in H2O and D2O at High Temperatures. 2004

  293. IAPWS; Guideline on an Equation of State for Humid Air in Contact with Seawater and Ice, Consistent with the IAPWS Formulation 2008 for the Thermodynamic Properties of Seawater. 2010

  294. IAPWS; Guideline on a Low-Temperature Extension of the IAPWS-95 Formulation for Water Vapor. 2012

  295. IAPWS; Guideline on the Thermal Conductivity of Seawater. 2015

  296. IAPWS; Guideline on a Virial Equation for the Fugacity of H2O in Humid Air. 2015

  297. IAPWS; Guideline on Thermodynamic Properties of Supercooled Water. 2015

  298. IAPWS; Thermodynamic Derivatives from IAPWS Formulations. 2014

  299. IAPWS; Industrial Calculation of the Thermodynamic Properties of Seawater. 2016

  300. Ibrahim, E.Z.; Augmentation of laminar flow and heat transfer in flat tubes by means of helical screw-tape inserts. Energy Conv. Management 52(1) (2011) 250-257, http://dx.doi.org/10.1016/j.enconman.2010.06.065

  301. Iglesias-Silva, G.A., Hall K.R.; An Equation for Prediction and/or Correlation of Second Virial Coefficients. Ind. Eng. Chem. Res. 40(8) (2001) 1968-1974, http://dx.doi.org/10.1021/ie0006817

  302. Ihmels, E.C., Lemmon, E.W.; Experimental densities, vapor pressures, and critical point, and a fundamental equation of state for dimethyl ether. Fluid Phase Equilibria 260(1) (2007) 36-48, http://dx.doi.org/10.1016/j.fluid.2006.09.016

  303. Inaba, H., Ozaki, K., Kanaoka, S.; A Fundamental Study of Heat-Transfer Enhancement and Flow-Drag Reduction in Tubes by Means of Wire Coil Insert. Trans. Jpn. Soc. Mech. Eng. 60 (1994) 240-247, http://dx.doi.org/10.1299/kikaib.60.240

  304. Ito, H.; Friction Factors for Turbulent Flow in Curved Pipes. J. Basic Eng. 81 (1959) 123-134, http://dx.doi.org/10.1115/1.4008390

  305. Ito, H.; Laminar Flow in Curved Pipes. Z. Angew. Math. Mech. 11 (1969) 653-663, http://dx.doi.org/10.1002/zamm.19690491104

  306. Iwasaki, S., Kondou, C., Higashi, Y.; Correlation Assessment and Temperature Dependence Check of Surface Tension and Parachor for New Low-GWP Pure Refrigerants. Trans. JSRAE 37(1) (2020) 73-80, http://dx.doi.org/10.11322/tjsrae.19-36TG_EM_OA

  307. Jacobsen, R.T, Penoncello, S.G., Beyerlein, S.W., Clarke, W.P., Lemmon, E.W.; A Thermodynamic Property Formulation for Air. Fluid Phase Equilibria, 79 (1992) 113-124, http://dx.doi.org/10.1016/0378-3812(92)85124-Q

  308. Jacobsen, R.T, Penoncello, S.G., Lemmon, E.W.; A Fundamental Equation for Trichlorofluoromethane (R-11). Fluid Phase Equilibria, 80 (1992) 45-56, http://dx.doi.org/10.1016/0378-3812(92)87054-Q

  309. Jacobsen, R.T, Stewart, R.B., Jahangiri, M.; Thermodynamic Properties of Nitrogen from the Freezing Line to 2000K at Pressures to 1000MPa. J. Phys. Chem. Ref. Data, 15(2) (1986) 735-908, http://dx.doi.org/10.1007/BF00502385

  310. Jaeschke, M., Schley, P.; Ideal-Gas Thermodynamic Properties for Natural Gas Applications. Int. J. Thermophys. 16(6) (1995) 1381-1392, http://dx.doi.org/10.1007/bf02083547

  311. Jahangiri, M., Jacobsen, R.T, Stewart, R.B., McCarty, R.D.; Thermodynamic properties of ethylene from the freezing line to 450 K at pressures to 260 MPa. J. Phys. Chem. Ref. Data 15(2) (1986) 293-734, http://dx.doi.org/10.1063/1.555753

  312. Jain, A.K.; Accurate Explicit Equation for Friction Factor. J. Hydraulics Division 102(5) (1976) 674-77

  313. Jaisankar, S., Radhakrishnan, T.;., Sheeba, K.N.; Experimental studies on heat transfer and friction factor characteristics of forced circulation solar water heater system fitted with helical twisted tapes. Solar Energy 83(11) (2009) 1943-1952, http://dx.doi.org/10.1016/j.solener.2009.07.006

  314. Janssen, L.A.M., Hoogendoorn, C.J.; Laminar Convective Heat Transfer in Helical Coiled Tubes. Int. J. Heat Mass Transfer 21(9) (1978) 1197-1206, http://dx.doi.org/10.1016/0017-9310(78)90138-2

  315. Jaubert, J.-N., Mutelet, F.; VLE predictions with the Peng–Robinson equation of state and temperature dependent kij calculated through a group contribution method. Fluid Phase Equilibria 224 (2004) 285-304, http://dx.doi.org/10.1016/j.fluid.2004.06.059

  316. Jaubert, J.-N., Vitu, S., Mutelet, F., Corriou, J.-P.; Extension of the PPR78 model (predictive 1978, Peng-Robinson EOS with temperature dependent kij calculated through a group contribution method) to systems containing aromatic compounds. Fluid Phase Equilibria 237 (2005) 193-211, http://dx.doi.org/10.1016/j.fluid.2005.09.003

  317. Jayakumar, J.S., Mahajani, S.M., Mandal, J.C., Vijayan, P.K., Bhoi, R.; Experimental and CFD estimation of heat transfer in helically coiled heat exchangers. Chem. Eng. Res. Design 86(3) (2008) 221-232, http://dx.doi.org/10.1016/j.cherd.2007.10.021

  318. Jenkins, G.I., Walsh, R.E; Quick Measure of Jet Fuel Properties. Hydrocarbon Processing 47(5) (1968) 161-164

  319. Jennings, S.G.; The Mean Free Path in Air. J. Aerosol Sci. 19(2) (1988) 159-16619(2):159-166, http://dx.doi.org/10.1016/0021-8502(88)90219-4

  320. Joback, K.G., Reid, R.C.; Estimation of Pure-Component Properties from Group-Contributions.. Chemical Engineering Communications, 57 (1987) 233-243, http://dx.doi.org/10.1080/00986448708960487

  321. Joffe, J.; Vapor-Liquid Equilibria by the Pseudocritical Method. Ind. Eng. Chem. Fundam. 15(4) (1976) 298-303, http://dx.doi.org/10.1021/i160060a013

  322. John Pye; Open source steam property routines in C. Implements the IAPWS-IF97 steam tables from the International Association for the Properties of Water and Steam . https://sourceforge.net/projects/freesteam/

  323. Johnstone, H.F., Feild, R.B., Tassler, M.C.; Gas Absorption and Aerosol Collection in a Venturi Atomizer. Ind. Eng. Chemistry 46(8) (1954) 1601-1608, http://dx.doi.org/10.1021/ie50536a028

  324. Jossi, J.A., Stiel, L.I., Thodos, G.; The Viscosity of Pure Substances in the Dense Gaseous and Liquid Phases. AIChE Journal 8(1) (1962) 59-63, http://dx.doi.org/10.1002/aic.690080116

  325. Ju, H., Huang, Z., Xu, Y., Duan, B, Yu, Y.; Hydraulic Performance of Small Bending Radius Helical Coil-Pipe. J. Nuclear Sci. Eng. 38(10) (2001) 826-831, http://dx.doi.org/10.1080/18811248.2001.9715102

  326. Kadhem, Q.M.A, Al-Sahhaf, T.A., Hamam, S.E.M.; Parameters of the Modified Soave-Redlich-Kwong Equation of State for Some Chlorofluorocarbons, Hydrofluorocarbons andFluorocarbons. J. Fluorine Chem. 43(1) (1989) 87-104, http://dx.doi.org/10.1016/s0022-1139(00)81638-3

  327. Kalb, C.E., Seader, J.D.; Heat and Mass Transfer Phenomena for Viscous Flow in Curved Circular Tubes. Int. J. Heat Mass TRansfer 15() (1972) 801-817, http://dx.doi.org/10.1016/0017-9310(72)90122-6

  328. Kamei, A., Beyerlein, S.W., Jacobsen, R.T.; Application of Nonlinear Regression in the Development of a Wide Range Formulation for HCFC-22. Int. J. Thermophysics, 16(5) (1995) 1155-1164, http://dx.doi.org/10.1007/BF02081283

  329. Kanitkar, D., Thodos, G.; The Thermal Conductivity of Liquid Hydrocarbons. Can. J. Chem. Eng. 47 (1969) 427-430, http://dx.doi.org/10.1002/cjce.5450470502

  330. Karamanev, D.G.; Equations for Calculation of the Terminal Velocity and Drag Coefficient of Solid Spheres and Gas Bubbles. Chem. Eng. Comm. 147(1) (1996) 75-84, http://dx.doi.org/10.1080/00986449608936496

  331. Katti, R.S., Jacobsen, R.T, Stewart, R.B., Jahangiri, M.; Thermodynamic Properties of Neon for Temperatures from the Triple Point to 700 K at Pressures up to 700 MPa. Adv. Cryo. Eng. 31 (1986) 1189-1197, http://dx.doi.org/10.1007/978-1-4613-2213-9_132

  332. Katz, D.L., Firoozabadi, A.; Predicting Phase Behavior of Condensate/Crude-oil SystemsUsing Methane Interaction Coefficients. Journal of Petroleum Technology 30(11) (1978) 1649-1655, http://dx.doi.org/10.2118/6721-pa

  333. Kendall, J., Monroe, P.; The Viscosity of Liquids II. The Viscosity-Composition Curve for Ideal Liquid Mixtures. J. Am. Chem. Soc. 39(9) (1917) 1787-1802, http://dx.doi.org/10.1021/ja02254a001

  334. Kesler, M.G., Lee, B.I.; Improve Prediction of Enthalpy of Fractions. Hydrocarbon Processing 55(3) (1976) 153-158

  335. Khan, A.R., Richardson, J.F.; The Resistance to Motion of a Solid Sphere in a Fluid.. Chem. Eng. Comm. 62 (1987) 135-150, http://dx.doi.org/10.1080/00986448708912056

  336. Kidd, G.J. Jr.; Heat Transfer and Pressure Drop for Nitrogen Flowing in Tubes Containing Twisted Tapes. AIChE J. 15(4) (1969) 581-585., http://dx.doi.org/10.1002/aic.690150420

  337. Kim, Y., Borgnakke, C., Sonntag, R.E.; Equation of State for 1,1-difluoroethane (R152a). Int. J. Energy Res 21(7) (1997) 575-589, http://dx.doi.org/10.1002/(sici)1099-114x(19970610)21:7<575::aid-er272>3.0.co;2-f

  338. Kiselev, S. B., Ely, J. F., Abdulagatov, I. M., Huber, M. L.; Generalized SAFT-DFT/DMT Model for the Thermodynamic, Interfacial, and Transport Properties of Associating Fluids: Application for n-Alkanols. Ind. Eng. Chem. Res. 44(17) (2005) 6916-6927, http://dx.doi.org/10.1021/ie050010e

  339. Klaczak, A.; Heat transfer by laminar flow in a vertical pipe with twisted-tape inserts. Heat Mass Transfer 36 (2000) 195-199, http://dx.doi.org/10.1007/s002310050384

  340. Klaczak, A.; Heat Transfer in Tubes With Spiral and Helical Turbulators. J. Heat Transfer 95(4) (1973) 557-559, http://dx.doi.org/10.1115/1.3450114

  341. Klein, S.A., McLinden, M.O., Laesecke, A.; An improved extended corresponding states method for estimation of viscosity of pure refrigerants and mixtures. Int. J. Refrig. 20(3) (1997) 208-217, http://dx.doi.org/10.1016/s0140-7007(96)00073-4

  342. Klincewicz, K.M., Reid, R.C.; Estimation of Critical Properties with Group Contribution Methods. AIChE J. 30(1) (1984) 137-142, http://dx.doi.org/10.1002/aic.690300119

  343. Kondou, C., Nagata, R., Nii, N., Koyama, S., Higashi, Y; Surface Tension of low GWP refrigerants R1243zf, R1234ze(Z) and R1233zd(E). Int. J. Refrigeration 53 (2015) 80-89, http://dx.doi.org/10.1016/j.ijrefrig.2015.01.005

  344. Konno, H., Saito, S.; Pneumatic Conveying of Solids Through Straight Pipes. J. Chem. Eng. Japan 2(2) (1969) 211-217, http://dx.doi.org/10.1252/jcej.2.211

  345. Korsten, H.; Internally Consistent Prediction of Vapor Pressure and Related Properties. Ind. Eng. Chem. Res. 39(3) (2000) 813-820, http://dx.doi.org/10.1021/ie990579d

  346. Koutian, A., Assael, M.J., Huber, M.L., Perkins, R.A.; Reference Correlation of the Thermal Conductivity of Cyclohexane from the Triple Point to 640 K and up to 175 MPa. J. Phys. Chem. Ref. Data 46(1) (2017) 013102, http://dx.doi.org/10.1063/1.4974325

  347. Kozlov A.D.; Private communication with Dr. Alexander D. Kozlov, Director, VNITs SMV Russian Research Center for Standartization Information and Certification of Materials.

  348. Krauss, R., Stephan, K.; Thermal Conductivity of Refrigerants in a Wide Range of Temperature and Pressure. J. Phys. Chem. Ref. Data 18(1) (1989) 43-76, http://dx.doi.org/10.1063/1.555842

  349. Krauss, R., Weiss, V.C., Edison, T.A., Sengers, J.V., Stephan, K.; Transport Properties of 1,1-Difluoroethane (R152a). Int. J. Thermophysics 17:731-757, 1996., http://dx.doi.org/10.1007/BF01439187

  350. Kubair, V., Kuloor, N.R.; Heat Transfer to Newtonian Fluids in Coiled Pipes in Laminar Flow. Int. J. Heat Mass Transfer 9 (1966) 63-75, http://dx.doi.org/10.1016/0017-9310(66)90057-3

  351. Kubic, W.L.; A Modification of the Martin Equation of State for Calculating Vapour-Liquid Equilibria. Fluid Phase Equilibria 9 (1982) 79-97, http://dx.doi.org/10.1016/0378-3812(82)85006-1

  352. Kumar, N.; Compressibility factors for natural and sour reservoir gases by correlations and cubic equations of state. Thesis of master of science in Petroleum Engineering, 2004, Texas Tech University.

  353. Kume, D., Sakoda, N., Uematsu, M.; An equation of State for Thermodynamic Properties for Methanol.

  354. Kunz, O., Klimeck, R., Wagner, W., Jaeschke, M.; The GERG-2004 Wide-Range Equation of State for Natural Gases and Other Mixtures. GERG TM15 2007

  355. Kunz, O., Wagner, W.; The GERG-2008 Wide-Range Equation of State for Natural Gases and Other Mixtures: An Expansion of GERG-2004. J. Chem.Eng. Data 57(11) (2012) 3032-3091, http://dx.doi.org/10.1021/je300655b

  356. Kutateladze, S.S., Borishanskii, V.M. ; A Concise Encyclopedia of Heat Transfer. Pergamon Press (1966)

  357. Laesecke, A., Krauss, R., Stephan, K., Wagner, W.; Transport Properties of Fluid Oxygen. J. Phys. Chem. Ref. Data 19(5) (1990) 1089-1122, http://dx.doi.org/10.1063/1.555863

  358. Laesecke, A., Muzny, C.D.; Reference Correlation for the Viscosity of Carbon Dioxide. J. Phys. Chem. Ref. Data 46(1) (2017) 013107, http://dx.doi.org/10.1063/1.4977429

  359. Laesecke, A., Perkins, R.A., Howley, J.B.; An improved correlation for the thermal conductivity of HCFC123 (2,2-dichloro-1,1,1-trifluoroethane). Int. J. Refrigeration 19(4) (1996) 231-238, http://dx.doi.org/10.1016/0140-7007(96)00019-9

  360. Lakshmi, D.S., Prasad, D.H.L.; A Rapid Estimation Method for Thermal Conductivity of Pure Liquids. The Chemical Engineering Journal 48 (1992) 211-14, http://dx.doi.org/10.1016/0300-9467(92)80037-b

  361. Leachman, J.W., Jacobsen, R.T, Penoncello, S.G., Lemmon, E.W.; Fundamental equations of state for Parahydrogen, Normal Hydrogen, and Orthohydrogen. J. Phys. Chem. Ref. Data, 38(3) (2009) 721-748, http://dx.doi.org/10.1063/1.3160306

  362. Lee, B.I., Kesler, M.G.; A Generalized Thermodynamic Correlation Based on Three-Parameter Corresponding States. AIChE Journal 21(3) (1975) 510-527, http://dx.doi.org/10.1002/aic.690210313

  363. Lemmon, E.W.; unpublished equation, 2007

  364. Lemmon, E.W.; preliminary equation, 2005..

  365. Lemmon, E.W.; Pseudo-Pure Fluid Equations of State for the Refrigerant Blends R-410A, R-404A, R-507A, and R-407C. Int. J. Thermophys., 24(4) (2003) 991-1006, http://dx.doi.org/10.1023/A:1025048800563

  366. Lemmon, E.W. Jacobsen, R.T; A New Functional Form and New Fitting Techniques for Equations of State with Application to Pentafluoroethane (HFC-125). J. Phys. Chem. Ref. Data 34(1) (2005) 69-108, http://dx.doi.org/10.1063/1.1797813

  367. Lemmon, E.W., Akasaka, R.; An International Standard Formulation for 2,3,3,3-Tetrafluoroprop-1-ene (R1234yf) Covering Temperatures from the Triple Point Temperature to 410 K and Pressures Up to 100 MPa. Int. J. Thermophys. 43(8) (2022) 119, http://dx.doi.org/10.1007/s10765-022-03015-y

  368. Lemmon, E.W., Huber, M.L.; Thermodynamic Properties of n-Dodecane. Energy & Fuels, 18(4) (2004) 960-967, http://dx.doi.org/10.1021_ef0341062

  369. Lemmon, E.W., Huber, M.L., McLinden, M.O.; NIST Standard Reference Database 23: Reference FluidThermodynamic and Transport Properties-REFPROP, Version9.1, National Institute of Standards and Technology,Standard Reference Data Program, Gaithersburg, 2013..

  370. Lemmon, E.W., Ihmels, E.C.; Thermodynamic properties of the butenes: Part II. Short fundamental equations of state. Fluid Phase Equilibria 228-229 (2005) 173-187, http://dx.doi.org/10.1016/j.fluid.2004.09.004

  371. Lemmon, E.W., Jacobsen, R.T, Penoncello, S.G., Friend, D.G.; Thermodynamic Properties of Air and Mixtures of Nitrogen, Argon, and Oxygen From 60 to 2000 K at Pressures to 2000 MPa. J. Phys. Chem. Ref. Data 29(3) (2000) 331-385, http://dx.doi.org/10.1063/1.1285884

  372. Lemmon, E.W., Jacobsen, R.T.; Viscosity and Thermal Conductivity Equations for Nitrogen, Oxygen, Argon, and Air. Int. J. Thermophys., 25(1) (2004) 21-69, http://dx.doi.org/10.1023/B:IJOT.0000022327.04529.f3

  373. Lemmon, E.W., Jacobsen, R.T.; An International Standard Formulation for the Thermodynamic Properties of 1,1,1-Trifluoroethane (HFC-143a) for Temperatures From 161 to 450 K and Pressures to 50 MPa. J. Phys. Chem. Ref. Data 29(4) (2000) 521-552, http://dx.doi.org/10.1063/1.1318909

  374. Lemmon, E.W., McLinden, M.O., Wagner, W.; Thermodynamic Properties of Propane. III. A Reference Equation of State for Temperatures from the Melting Line to 650 K and Pressures up to 1000 MPa. J. Chem. Eng. Data, 54(12) (2009) 3141-3180, http://dx.doi.org/10.1021/je900217v

  375. Lemmon, E.W., Overhoff, U., McLinden, M.O., Wagner, W.; A Reference Equation of State for the Thermodynamic Properties of Propene for Temperatures from the Melting Line to 575 K and Pressures up to 1000 MPa. to be submitted to J. Phys. Chem. Ref. Data

  376. Lemmon, E.W., Span, R.; Short Fundamental Equations of State for 20 Industrial Fluids. J. Chem. Eng. Data 51(3) (2006) 785-850, http://dx.doi.org/10.1021/je050186n

  377. Lemmon, E.W., Span, R.; Short Fundamental Equations of State for 20 Industrial Fluids. J. Chem. Eng. Data, 2006, 51 (3), pp 785–850, http://dx.doi.org/10.1021/je050186n

  378. Lemmon, E.W., Span, R.; Thermodynamic Properties of R-227ea, R-365mfc, R-115, and R-13I1. J. Chem. Eng. Data, 60(12) (2015) 3745-3758, http://dx.doi.org/10.1021/acs.jced.5b00684

  379. Lemmon, E.W., Span, R.; Short Fundamental Equations of State for 20 Industrial Fluids. J. Chem. Eng. Data, 51(3) (2006) 785-850, http://dx.doi.org/10.1021/je050186n

  380. Lenoir, J.M.; Effect of Pressure on Thermal Conductivity of Liquids. Petroelum Refiner 36(8) 1508

  381. Letsou, A., Stiel, L.I.; Viscosity of Saturated Nonpolar Liquids at Elevated Pressures. AIChE Journal 19(2) (1973) 409-411, http://dx.doi.org/10.1002/aic.690190241

  382. Li, C.C.; Thermal Conductivity of Liquid Mixtures. AIChE Journal 22(5) (1976) 927-930, http://dx.doi.org/10.1002/aic.690220520

  383. Li, J., Tillner-Roth, R., Sato, H., Watanabe, K.; An Equation of State for 1,1,1-Trifluoroethane (R-143a). Int. J. Thermophys., 20(6) (1999) 1639-1651, http://dx.doi.org/10.1023/A:1022645626800

  384. Li, J., Xia, L., Xiang, S.; A New Method Based on Elements and Chemical Bonds for Organic Compounds Critical Properties Estimation. Fluid Phase Equil. 417 (2016) 1-6, http://dx.doi.org/10.1016/j.fluid.2016.01.008

  385. Lin, H., Duan, Y.-Y.; Empirical Correction to the Peng-Robinson Equation of State for the Saturated Region. Fluid Phase Equilibria 233 (2005) 194-203, http://dx.doi.org/10.1016/j.fluid.2005.05.008

  386. Lin, H., Duan, Y.-Y.; Empirical correction to the Peng-Robinson equation of state for the saturated region. Fluid Phase Equilibria 233 (2005) 194-203, http://dx.doi.org/10.1016/j.fluid.2005.05.008

  387. Lindsay, A.L., Bromley, L.A.; Thermal Conductivity of Gas Mixtures. Ind. & Eng. Chem. 42(8) (1950) 1508-1511, http://dx.doi.org/10.1021/ie50488a017

  388. Liu, D.X., Xiang, H.W.; Corresponding-States Correlation and Prediction of Third Virial Coefficients for a Wide Range of Substances. Int. J. Thermophysics 24(6) (2003) 1667-1680, http://dx.doi.org/10.1023/b_ijot.0000004098.98614.38

  389. Liu, S., Masliyah, J.H.; Axially invariant laminar flow in helical pipes with a finite pitch. J. Fluid Mech. 251 (1993) 315-353, http://dx.doi.org/10.1017/S002211209300343X

  390. Livingston, J.k Morgan, R., Griggs, M.A.; The Properties of Mixed Liquids III. The Law of Mixtures I. J. Am. Chem. Soc. 39 (1917) 2261-2275, http://dx.doi.org/10.1021/ja02256a002

  391. Londono, F.E., Archer, R.A., Blasingame, T.A.; Correlations for hydrocarbon-gas viscosity and gas density-validation and correlation of behavior using a large-scale database. SPE Reserv. Evalu. Eng. 8 (6) 2005, 561–572., http://dx.doi.org/10.2118/75721-PA

  392. Lopina, R.F., Bergles, A.E.; Heat Transfer and Pressure Drop in Tape-Generaged Swirl Flow of Single-Phase Water. ASME J. Heat Transfer 91(3) (1969) 434-442, http://dx.doi.org/10.1115/1.3580212

  393. Lucas, K.; Die Druckabhängigheit der Viskosität von Flüssigkeiten, eine Einfache Abschätzung. Chem. Ing. Tech. 46(4) (1981) 959-960, http://dx.doi.org/10.1002/cite.330531209

  394. Lydersen, A. L.; Estimation of Critical Properties of Organic Compounds. Coll. Eng. Univ. Wisconsin, Engineering Experimental Station Rept. 3, Madison, WI (1955)

  395. Magee, J.W., Outcalt, S.L., Ely, J.F.; Molar Heat Capacity Cv, Vapor Pressure, and (p, ρ, T) Measurements from 92 to 350 K at Pressures to 35 MPa and a New Equation of State for Chlorotrifluoromethane (R13). Int. J. Thermophys., 21(5):1097-1121, 2000., http://dx.doi.org/10.1023/A:1026446004383

  396. Magoulas, S., Tassios, D.; Predictions of phase behavior of HT-HP reservoir fluids.. Paper SPE 37294, Society of Petroleum Engineers, Richardson,TX, 1990.

  397. Manadilli, G.; Replace implicit equations with signomial functions.. Chem. Eng. 104 (1997) 129-132.

  398. Mandal, M. M., Nigam, K.D.P.; Experimental Study on Pressure Drop and Heat Transfer of Turbulent Flow in Tube in Tube Helical Heat Exchanger. Ind. Eng. Chem. Res. 48(20) (2009) 9318-9324, http://dx.doi.org/10.1021/ie9002393

  399. Manglik, R.M., Bergles, A.E.; Heat Transfer and Pressure Drop Correlations for Twisted-Tape Inserts in Isothermal Tubes: Part I - Laminar Flows. J. Heat Transfer 115(4) (1993) 881-889, http://dx.doi.org/10.1115/1.2911383

  400. Manglik, R.M., Bergles, A.E.; Heat Transfer and Pressure Drop Correlations for Twisted-Tape Inserts in Isothermal Tubes: Part II - Transition and Turbulent Flows. J. Heat Transfer 115(4) (1993) 890-896, http://dx.doi.org/10.1115/1.2911384

  401. Manlapaz, R.L., Churchill, S.W.; Fully Developed Laminar Flow in a Helically Coiled Tube of Finite Pitch. Chem. Eng. Communications 7 (1980) 57-78, http://dx.doi.org/10.1080/00986448008912549

  402. Manlapaz, R.L., Churchill, S.W.; Fully Developed Laminar Convection From a Helical Coil. Chem. Eng. Commun. 9 (1981) 185-200, http://dx.doi.org/10.1080/00986448108911023

  403. Marrero, J.; Gani, R.; Group-contribution based estimation of pure component properties. Fluid Phase Equilib. 183-184 (2001), 183-208., http://dx.doi.org/10.1016_s0378-3812(01)00431-9

  404. Marrero-Morejon, J., Pardillo-Fontdevila, E.; Estimation of Liquid Viscosity at Ambient Temperature of Pure Organic Compounds by Using Group-Interaction Contributions. Chemical Engineering Journal 79 (2000) 69-72, http://dx.doi.org/10.1016/s1385-8947(99)00173-4

  405. Marrero-Morejón, J., Pardillo-Fontdevila, F.; Estimation of Pure Compound Properties Using Group-Interaction C9ontributions. AIChE J., 45(3) (1999) 615-621, http://dx.doi.org/10.1002/aic.690450318

  406. Marsh, K.N., Perkins, R.A., Ramires, M.L.V.; Measurement and Correlation of the Thermal Conductivity of Propane from 86 to 600 K at Pressures to 70 MPa. J. Chem. Eng. Data 47(4) (2002) 932-940, http://dx.doi.org/10.1021/je010001m

  407. Marx, V., Pruss, A., Wagner, W.; Neue Zustandsgleichungen fuer R 12, R 22, R 11 und R 113. Beschreibung des thermodynamishchen Zustandsverhaltens bei Temperaturen bis 525 K und Druecken bis 200 MPa. Düsseldorf: VDI Verlag, Series 19 (Waermetechnik/Kaeltetechnik), No. 57, 1992.

  408. Mason, E.A., Saxena, S.C.; Approximate Formula for the Thermal Conductivity of Gas Mixtures. Fhys. Fluids 1(5) (1958) 361-369, http://dx.doi.org/10.1063/1.1724352

  409. Mathias, P.M., Copeman, T.W.; Extension of the Peng-Robinson Equation of State to Complex Mixtures: Evaluation of the Various Forms of the Local Composition Concept. Fluid Phase Equilibria 13 (1983) 91-108, http://dx.doi.org/10.1016/0378-3812(83)80084-3

  410. Matsumoto, S., Hara, M., Saito, S., Maeda, S.; Minimum Transport Velocity for Horizontal Pneumatic Conveying. J. Chem. Eng. Japan 7(6) (1974) 425-430, http://dx.doi.org/10.1252/jcej.7.425

  411. Matsumoto, S., Harada, S., Saito, S., Maeda, S.; Saltation Velocity for Horizontal Pneumatic Conveying. J. Chem. Eng. Japan 8(4) (1975) 331-333, http://dx.doi.org/10.1252/jcej.8.331

  412. Matsumoto, S., Kikuta, M., Maeda, S.; Effect of Particle Size on the Minimum Transport Velocity for Horizontal Pneumatic Conveying of Solids. J. Chem. Eng. Japan 10(4) (1977) 273-279, http://dx.doi.org/10.1252/jcej.10.273

  413. McCarty, R.D.; Thermophysical Properties of Helium-4 from 2 to 1500 K with Pressures to 1000 MPa. NIST Technical Note 631 (1972)

  414. McCarty, R.D.; Correlations for the Thermophysical Properties of Deuterium. NIST, Boulder, CO, 1989

  415. McCarty, R.D.; Correlations for the Thermophysical Properties of Carbon Monoxide. NIST, Boulder, CO, 1989

  416. McCarty, R.D., Arp, V.D.; A New Wide Range Equation of State for Helium. Adv. Cryo. Eng., 35:1465-1475, 1990, http://dx.doi.org/10.1007/978-1-4613-0639-9_174

  417. McCarty, R.D., Hord, J., Roder, H.M.; Selected Properties of Hydrogen (Engineering Design Data). NBS Monograph 168, NBS 1981.

  418. McCarty, R.D., Jacobsen, R.T.; An Equation of State for Fluid Ethylene. Natl. Bur. Stand., Tech. Note 1045, 1981.

  419. McCarty, R.D., Weber, L.A.; Thermophysical Properties of Parahydrogen from the Freezing Liquid Line to 5000 R for Pressures to 10000 psia. NBS Technical Note 617

  420. McGarry, J.; Correlation and Perediction of the Vapor Pressures of PureLiquids over Large Pressure Ranges. Ind. Eng. Chem. Process. Des. Dev. 22 (1983) 313-322, http://dx.doi.org/10.1021/i200021a023

  421. Mchaweh, A., Alsaygh, A., Nasrifar, Kh., Moshfeghian, M.; A Simplified Method for Calculating Saturated Liquid Densities. Fluid Phase Equilibria 224 (2004) 157-167, http://dx.doi.org/10.1016/j.fluid.2004.06.054

  422. McLinden, M.O., Akasaka, R.; Thermodynamic Properties of cis-1,1,1,4,4,4-Hexafluorobutene [R-1336mzz(Z)]: Vapor Pressure, (p, ρ, T) Behavior, and Speed of Sound Measurements and Equation of State. J. Chem. Eng. Data 65(9) (2020) 4201-4214, http://dx.doi.org/10.1021/acs.jced.9b01198

  423. McLinden, M.O., Klein, S.A., Perkins, R.A.; An Extended corresponding states model for the thermal conductivity of refrigerants and refrigerant mixtures. Int. J. Refrigeration 23 (2000) 43-63, http://dx.doi.org/10.1016/s0140-7007(99)00024-9

  424. McLinden, M.O., Perkins, R.A., Lemmon, E.W., Fortin, T.J.; Thermodynamic Properties of 1,1,1,2,2,4,5,5,5-nonafluoro-4-(trifluoromethyl)-3-pentanone: Vapor Pressure, (p, ρ, T) Behavior, and Speed of Sound Measurements, and an Equation of State. J. Chem. Eng. Data 60(12) (2015) 3646-3659, http://dx.doi.org/10.1021/acs.jced.5b00623

  425. McLinden, M.O., Thol, M., Lemmon, E.W.; Thermodynamic Properties of trans-1,3,3,3-Tetrafluoropropene [R1234ze(E)]: Measurements of Density and Vapor Pressure and a Comprehensive Equation of State. International Refrigeration and Air Conditioning Conference at Purdue, July 12-15, 2010., http://dx.doi.org/10.0000_docs.lib.purdue.edu_generic-99DA7EA2C877

  426. McLinden, M.O., Younglove, B.A., Sandarusi, J.; Measurement of the PVT properties and formulation of an equation of state for refrigerant 124 (1-chloro-1,2,2,2-tetrafluoroethane). 1994. (unpublished manuscript)

  427. Mebelli, M., Velliadou, D., Assael, M.J., Antoniadis, K.D., Huber, M.L.; Reference Correlations for the Thermal Conductivity of Ethane-1,2-diol (Ethylene Glycol) from the Triple Point to 475 K and Pressures up to 100 MPa. Int. J. Thermophysics 42(11) (2021) 151, http://dx.doi.org/10.1007/s10765-021-02904-y

  428. Mebelli, M., Velliadou, D., Assael, M.J., Huber, M.L.; Reference Correlations for the Viscosity of Ethane-1,2-diol (Ethylene Glycol) from the Triple Point to 465 K and up to 100 MPa. Int. J. Thermophys. 42(8) (2021) 116, http://dx.doi.org/10.1007/s10765-021-02867-0

  429. Melhem, G.A., Saini, R., Goodwin, B.M.; A Modified Peng-Robinson Equation of State. Fluid Phase Equilibria 47 (1989) 189-237, http://dx.doi.org/10.1016/0378-3812(89)80176-1

  430. Meng, L., Duan, Y.Y. Li, L.; Correlations for Second and Third Virial Coefficients of Pure Fluids. Fluid Phase Equilibria 226 (2004) 109-120, http://dx.doi.org/10.1016/j.fluid.2004.09.023

  431. Meng, X., Zhang, J., Wu, J., Liu, Z.; Experimental Measurement and Modeling of the Viscosity of Dimethyl Ether. J. Chem. Eng. Data 57(3) (2012) 988-993, http://dx.doi.org/10.1021/je201297j

  432. Meng, X.Y., Cao, F.L., Wu, J.T., Vesovic, V.; Reference Correlation of the Viscosity of Ethylbenzene from the Triple Point to 673 K and up to 110 MPa. J. Phys. Chem. Ref. Data 46(1) (2017) 013101, http://dx.doi.org/10.1063/1.4973501

  433. Meng, X.Y., Sun, Y.K., Cao, F.L., Wu, J.T., Vesovic, V.; Reference Correlation of the Viscosity of n-Hexadecane from the Triple Point to 673 K and up to 425 MPa. J. Phys. Chem. Ref. Data 47(3) (2018) 033102, http://dx.doi.org/10.1063/1.5039595

  434. Michailidou, E.K., Assael, M.J., Huber, M.L., Abdulagatov, I.M., Perkins, R.A.; Reference Correlation of the Viscosity of n-Heptane from the Triple Point to 600 K and up to 248 MPa. J. Phys. Chem. Ref. Data 43(2) (2014) 023103, http://dx.doi.org/10.1063/1.4875930

  435. Michailidou, E.K., Assael, M.J., Huber, M.L., Perkins, R.A.; Reference Correlation of the Viscosity of n-Hexane from the Triple Point to 600 K and up to 100 MPa. J. Phys. Chem. Ref. Data 42(3) (2013) 033104, http://dx.doi.org/10.1063/1.4818980

  436. Michels, A., Prins, C.; The Melting Lines of Argon, Krypton and Xenon up to 1500 Atm; Representation of the Results by a Law of Corresponding States. Physica 28 (1962) 101-116, http://dx.doi.org/10.1016/0031-8914(62)90096-4

  437. Mikhailov, M.D., Silva Freire, A.P.; The Drag Coefficient of a Sphere: An Approximation Using Shanks Transform. Powder Technology 237 (2013) 432-435, http://dx.doi.org/10.1016/j.powtec.2012.12.033

  438. Miller, D.G., Thodos, G.; Reduced Frost-Kalkwarf Vapor Pressure Equation. I&EC Fundamentals 2(1) (1963) 78-80, http://dx.doi.org/10.1021/i160005a015

  439. Miqueu, C., Broseta, D., Satherley, J., Mendiboure, B., Lachaise, J., Graciaa, A.; An Extended Scaled Equation for the Temperature Dependence of the Surface Tension of Pure Compounds Inferred from an Analysis of Experimental Data. Fluid Phase Equilibria 172(2) (2000) 169-182, http://dx.doi.org/10.1016/s0378-3812(00)00384-8

  440. Mishra, P., Gupta, S.N.; Momentum Transfer in Curved Pipes. 1. Newtonian Fluids. Ind. Eng. Chem. Process Des. Dev. 18(1) (1979) 130-137, http://dx.doi.org/10.1021_i260069a017

  441. Misic, D., Thodos, G.; The Thermal Conductivity of Hydrocarbon Gases at Normal Pressures. AIChE Journal 7(2) (1961) 264-267, http://dx.doi.org/10.1002/aic.690070219

  442. Miyamoto, H., Watanabe, K.; A Thermodynamic Property Model for Fluid-Phase Propane. Int. J. Thermophys., 21(5) (2000) 1045-1072, http://dx.doi.org/10.1023/A:1026441903474

  443. Miyamoto, H., Watanabe, K.; A Thermodynamic Property Model for Fluid-Phase n-Butane. Int. J. Thermophys., 22(2) (2001) 459-475, http://dx.doi.org/10.1023/A:1010722814682

  444. Miyamoto, H., Watanabe, K.; A Thermodynamic Property Model for Fluid-Phase Isobutane. Int. J. Thermophys., 23(2) (2002) 477-499, http://dx.doi.org/10.1023/A:1015161519954

  445. Mondejar, M.E., McLinden, M.O., Lemmon, E.W.; Thermodynamic Properties of trans-1-Chloro-3,3,3-trifluoropropene (R1233zd(E)): Vapor Pressure, (p-ρ-T) Behavior, and Spped of Sound Measurements, and Equation of State. J. Chem. Eng. Data 60(8) (2015) 2477-2489, http://dx.doi.org/10.1021/acs.jced.5b00348

  446. Monogenidou, S.A., Assael, M.J., Huber, M.L.; Reference Correlation for the Viscosity of Ammonia from the Triple Point to 725K and up to 50 MPa. J. Phys. Chem. Ref. Data 47(2) (2018) 023102, http://dx.doi.org/10.1063/1.5036724

  447. Monogenidou, S.A., Assael, M.J., Huber, M.L.; Reference Correlations for the Thermal Conductivity of Ammonia from the Triple Point to 680 K and Pressures up to 80 MPa. J. Phys. Chem. Ref. Data 47(4) (2018) 043101, http://dx.doi.org/10.1063/1.5053087

  448. Monogenidou, S.A., Assael, M.J., Huber, M.L.; Reference Correlations for the Thermal Conductivity of n-Hexadecane from the Triple Point to 700K and up to 50MPa. J. Phys. Chem. Ref. Data 47(1) (2018) 013103, http://dx.doi.org/10.1063/1.5021459

  449. Moody, L. F.; An approximate formula for pipe friction factors. Trans. ASME, 69(12) (1947) 1005-1006.

  450. Mori, Y., Nakayama, W.; Study on Forced Convective Heat Transfer in Curved Pipes (1st Report, Laminar Region). Int. J. Heat Mass Transfer 8(1) (1965) 67-82, http://dx.doi.org/10.1016/0017-9310(65)90098-0

  451. Mori, Y., Nakayama, W.; Study on Forced Convective Heat Transfer in Curved Pipes (2nd Report, Turbulent Region). Int. J. Heat Mass Transfer 10(1) (1967) 37-59, http://dx.doi.org/10.1016/0017-9310(67)90182-2

  452. Mori, Y., Nakayama, W.; Study on Forced Convective Heat Transfer in Curved Pipes (3rd Report, Theoretical Analysis under the Condition of Uniform Wall Temperature and Practical Formulae). Int. J. Heat Mass Transfer 10(5) (1967) 681-695, http://dx.doi.org/10.1016_0017-9310(67)90113-5

  453. Morrison, F.A.; An Introduction to Fluid Mechanics.. Cambridge University Press, 2013.

  454. Morshed, M., Alam, M.J., Tuhin, A.R., Islam, M.A., Miyara, A.; Empirical models of thermal conductivity of cis-1,3,3,3-tetrafluoropropene (R1234ze(Z)) with measurements using transient hot-wire method. Int. J. Refrigeration 158 (2024) 1-8, http://dx.doi.org/10.1016/j.ijrefrig.2023.11.004

  455. Morshed, M., Tuhin, A.R., Akasaka, R., Miyara, A.; Application of Extended Corresponding States (ECS) and Residual Entropy Scaling (RES) Techniques for Modeling Viscosity of cis-1,3,3,3-Tetrafluoropropene (R1234ze(Z)) with Revised Experimental Data. Int. J. Thermophysics 44 (2023) 123, http://dx.doi.org/10.1007/s10765-023-03231-0

  456. Morsi, S.A., Alexander, A.J.; An Investigation of Particle Trajectories in Two-Phase Flow Systems. J. Fluid Mechanics 55(2) (1972) 193-208, http://dx.doi.org/10.1017/S0022112072001806

  457. Mulero, A., Cachadiña, I.; Recommended Correlations for the Surface Tension of Several Fluids Included in the REFPROP Program. J. Phys. Chem. Ref. Data 43(2) (2014) 023104, http://dx.doi.org/10.1063/1.4878755

  458. Mulero, A., Cachadiña, I., Bautista, D.; Recommended Correlations for the Surface Tension of n-Alkanes. J. Phys. Chem. Ref. Data 50(2) (2021) 023104, http://dx.doi.org/10.1063/5.0048675

  459. Mulero, A., Cachadiña, I., Parra, M.I.; Recommended Correlations for the Surface Tension of Common Fluids. J. Phys. Chem. Ref. Data 41(4) (2012) 043105, http://dx.doi.org/10.1063/1.4768782

  460. Mulero, A., Cachadiña, I., Rodríguez-Martín, A.; Recommended Correlations for the Surface Tension of 42 Alkenes. J. Phys. Chem. Ref. Data 54(3) (2025) 033102, http://dx.doi.org/10.1063/5.0277723

  461. Mulero, A., Cachadiña, I., Sanjuán, E.L.; Surface Tension of Alcohols. Data Selection and Recommended Correlations. J. Phys. Chem. Ref. Data 44(3) (2015) 033104, http://dx.doi.org/10.1063/1.4927858

  462. Murugesan, P., Mayilsamy, K., Suresh, S.; Heat Transfer and Friction Factor Studies in a Circular Tube Fitted with Twisted Tape Consisting of Wire-nails. Chin. J. Chem. Eng. 18(6) (2010) 1038-1042, http://dx.doi.org/10.1016/S1004-9541(09)60166-X

  463. Murugesan, P., Mayilsamy, K., Suresh, S.; Turbulent Heat Transfer and Pressure Drop in Tube Fitted with Square-cut Twisted Tape. Chin. J. Chem. Eng. 18(4) (2010) 609-617, http://dx.doi.org/10.1016/s1004-9541(10)60264-9

  464. Murugesan, P., Mayilsamy, K., Suresh, S.; Heat Transfer in Tubes Fitted with Trapezoidal-Cut and Plain Twisted Tape Inserts. Chem. Eng. Communications 198(7) (2011) 886-904, http://dx.doi.org/10.1080/00986445.2011.545294

  465. Murugesan, P., Mayilsamy, K., Suresh, S.; Heat Transfer in a Tube Fitted with Vertical and Horizontal Wing-cut Twisted Tapes. Exp. Heat Transfer 25(1) (2012) 30-47, http://dx.doi.org/10.1080/08916152.2011.559567

  466. Murugesan, P., Mayilsamy, K., Suresh, S., Srinivasan, P.S.S; Heat transfer and pressure drop characteristics in a circular tube fitted with and without V-cut twisted tapeinsert. Int. Comm. Heat Mass Transfer 38(3) (2011) 329-334, http://dx.doi.org/10.1016/j.icheatmasstransfer.2010.11.010

  467. Muzny, C.D., Huber, M.L., Kazakov, A.F.; Correlation for the Viscosity of Normal Hydrogen Obtained from Symbolic Regression. J. Chem. Eng. Data 58(4) (2013) 969-979, http://dx.doi.org/10.1021/je301273j

  468. Mylona, S.K., Antoniadis, K.D., Assael, M.J., Huber, M.L., Perkins, R.A.; Reference Correlations of the Thermal Conductivity of o-Xylene, m-Xylene, p-Xylene, and Moderate Pressures. J. Phys. Chem. Ref. Data 43(4) (2014) 043104, http://dx.doi.org/10.1063/1.4901166

  469. Nanan, K., Thianpong, C., Promvonge, P., Eiamsa-ard, S.; Investigation of heat transfer enhancement by perforated helical twisted-tapes. Int. Comm. Heat Mass Transfer 52 (2014) 106-112, http://dx.doi.org/10.1016/j.icheatmasstransfer.2014.01.018

  470. Nannoolal, Y., Rarey, J., Ramjugernath, D.; Estimation of Pure Component Properties 2. Estimation of Critical Property Data by Group Contribution. Fluid Phase Equilib., 252 (2007) 1-27, http://dx.doi.org/10.1016/j.fluid.2006.11.014

  471. Nannoolal, Y., Rarey, J., Ramjugernath, D.; Estimation of Pure Component Properties 3. Estimation of the Vapor Pressure of Non-Electrolyte Organic Compounds Via Group Contributions and Group Interactions. Fluid Phase Equilib., 269 (2008) 117-133, http://dx.doi.org/10.1016/j.fluid.2008.04.020

  472. Nannoolal, Y., Rarey, J., Ramjugernath, D.; Estimation of Pure Component Properties 4. Estimation of the Saturated Liquid Viscosity of Non-Electrolyte Organic Compounds Via Group Contributions and Group Interactions. Fluid Phase Equilib., 281 (2009) 97-119, http://dx.doi.org/10.1016/j.fluid.2009.02.016

  473. Nannoolal, Y., Rarey, J., Ramjugernath, D., Cordes, W.; Estimation of Pure Component Properties 1. Estimation of the Normal Boiling Point of Non-electrolyte Organic Compounds Via Group Contributions and Group Interactions. Fluid Phase Equilib., 226 (2004) 45-63, http://dx.doi.org/10.1016/j.fluid.2004.09.001

  474. Naphon, P.; Heat transfer and pressure drop in the horizontal double pipes with and without twisted tape insert. Int. Comm. Heat Mass Transfer 33 (2006) 166-175, http://dx.doi.org/10.1016/j.icheatmasstransfer.2005.09.007

  475. Naphon, P.; Effect of coil-wire insert on heat trasnfer enhancement pressure drop of the horizontal concentric tubes. Int. Comm. Heat Mass Transfer 33(6) (2006) 753-763, http://dx.doi.org/10.1016/j.icheatmasstransfer.2006.01.020

  476. Naphon, P., Nuchjapo, M., Kurujareon, J.; Tube side heat transfer coefficient and friction factor characteristics of horizontal tubes with helical rib. Energy Conv. Management 47(18-19) (2006) 3031-3044, http://dx.doi.org/10.1016/j.enconman.2006.03.023

  477. Nasrifar, K., Ayatollahi, S., Moshfeghian, M.; A Compressed Liquid Density Correlation. Fluid Phase Equilibria 168 (2000) 149-163, http://dx.doi.org/10.1016/s0378-3812(99)00336-2

  478. Nasrifar, Kh., Bolland, O.; Square-Well Potential and a New α Function for the Soave-Redlich-Kwong Equation of State. Ind. Eng. Chem. Res. 43(21) (2004) 6901-6909, http://dx.doi.org/10.1021/ie049545i

  479. Nasrifar, Kh., Moshfeghian, M.; A New Cubic Equation of State for Simple Fluids: Pure and Mixture. Fluid Phase Equilibria 190 (2001) 73-88, http://dx.doi.org/10.1016/s0378-3812(01)00592-1

  480. Nath, J.; Acentric Factor and the Critical Volumes for Normal Fluids. Ind. Eng. Chem. Fundam. 21(3) (1985) 325-326, http://dx.doi.org/10.1021/i100007a023

  481. Nelson, H.F., Sauer, H.J.; Formulation of High-Temperature Properties for Moist Air. HVAC&R Research 8(2) (2002) 311-334, http://dx.doi.org/10.1080/10789669.2002.10391444

  482. Neufeld, P.D., Janzen, A.R., Aziz, R.A.; Empirical Equations to Calculate 16 of the Transport Collision Integrals Ω for the Lennard-Jones Potential. J. Chem. Phys. 57(3) (1972) 1100-1102, http://dx.doi.org/10.1063/1.1678363

  483. Nishiumi, H., Saito, S.; An Improved Generalized BWR Equation of State Applicable to Low Reduced Temperatures. J. Chem. Eng. Japan 8(5) (1975) 356-360, http://dx.doi.org/10.1252/jcej.8.356

  484. Ochi, M.; Saltation Velocity of the Gas-Solid Two-Phase Flow in a Horizontal Pipe. Trans. JSME B. 59(564) (1993) 2416-2421, http://dx.doi.org/10.1299/kikaib.59.2416

  485. Okada, M., Shibata, T., Sato. Y., Higashi, Y.; Surface Tension of HFC Refrigerant Mixtures. Int. J. Thermophysics 20(1) (1999) 119-127, http://dx.doi.org/10.1023/a:1021482231102

  486. Okada, M., Shibata, T., Sato. Y., Higashi, Y.; Surface Tension of HFC Refrigerant Mixtures. Int. J. Thermophysics 20(1) (1999) 119-127, http://dx.doi.org/10.1023/A:1021482231102

  487. Olchowy, G.A., Sengers, J.V.; A Simplified Representation for the Thermal Conductivity of Fluids in the Critical Region. Int. J. Thermophys. 10(2) (1989) 417-426, http://dx.doi.org/10.1007/bf01133538

  488. Orbey, H.; A Four Parameter Pitzer-Curl Type Correlation of Second Virial Coefficients. Chemical Engineering Comm. 65(1) (1988) 1-19, http://dx.doi.org/10.1080/00986448808940239

  489. Orbey, H., Vera, J.H.; Correlation for the Third Virial Coefficient Using Tc, Pc and ω as Parameters. AIChE Journal 29(1) (1983) 107-113, http://dx.doi.org/10.1002/aic.690290115

  490. Ortiz-Vega, D.O.; A New Wide Range Equation of State for Helium-4. Doctoral Dissertation, Texas A&M University (2013), http://dx.doi.org/1969.1/151301

  491. Outcalt, S.L. McLinden, M.O.; An Equation of State for the Thermodynamic Properties of R236fa. NIST report to sponsor under contract N61533-94-F-0152, 1995.

  492. Outcalt, S.L., McLinden, M.O.; Equations of State for the Thermodynamic Properties of R32 (Difluoromethane) and R125 (Pentafluoroethane). Int. J. Thermophysics 16(1) (1995) 79-89., http://dx.doi.org/10.1007/BF01438959

  493. Outcalt, S.L., McLinden, M.O.; An Equation of State for the Thermodynamic Properties of R143a (1,1,1-Trifluoroethane). Int. J. Thermophys., 18(6) (1997) 1445-1463, http://dx.doi.org/10.1007/BF02575344

  494. Outcalt, S.L., McLinden, M.O.; A modified Benedict-Webb-Rubin Equation of State for the Thermodynamic Properties of R152a (1,1-difluoroethane). J. Phys. Chem. Ref. Data 25(2) (1996) 605-636, http://dx.doi.org/10.1063/1.555979

  495. Overhoff, U.; Development of a New Equation of State for the Fluid Region of Propene for Temperatures from the Melting Line to 575 K with Pressures to 1000 MPa as well as Software for the computation of thermodynamic properties of fluids. PhD. Dissertation, Ruhr University, Bochum Germany, 2006

  496. Pachaiyappan, V., Ibrahim, S.H., Kuloor, N.R.; Thermal Conductivities of Organic Liquids: A New Correlation. J. Chem. Eng. Data, 11 (1966) 73-76, http://dx.doi.org/10.1021/je60028a021

  497. Pal, A., Pope, G., Arai, Y., Carnahan, N., Kobayashi, R.; Experimental Pressure-Volume-Temperature Relations for Saturated and Compressed Fluid Ethane. J. Chem. Eng. Data 21(4) (1976) 394-397, http://dx.doi.org/10.1021@je60071a008

  498. Pan, J., Rui, X., Zhao, X., Qiu, L.; An equation of state for the thermodynamic properties of 1,1,1,3,3,3-hexafluoropropane (HFC-236fa). Fluid Phase Equilib., 321 (2012) 10-16, http://dx.doi.org/10.1016/j.fluid.2012.02.012

  499. Panasiti, M.D., Lemmon, E.W., Penoncello, S.G., Jacobsen, R.T, Friend, D.G.; Thermodynamic Properties of Air from 60 to 2000 K at Pressures up to 2000 MPa. Int. J. Themophys. 20(1) (1999) 217-228, http://dx.doi.org/10.1023/a:1021450818807

  500. Papaevangelou, G., Evangelides, C., Tzimopoulos, C.,; A new explicit relation for friction coefficient in the Darcy-Weisbach equation. Proceedings of the Tenth Conference on Protection and Restoration of the Environment 166,1-7pp, PRE10 July 6-09 2010 Corfu, Greece.

  501. Papay, J.A.,; Termelestechnologiai Parameterek Valtozasa a GazlelepkMuvelese. Soran. OGIL MUSZ, Tud, Kuzl. [Budapest], 1985. pp. 267–273.

  502. Patel, N.C.; Improvements of the Patel-Teja Equation of State. Int. J. Thermophysics 17(3) (1996) 673-682, http://dx.doi.org/10.1007/bf01441513

  503. Patel, N.C., Teja, A.S.; A New Cubic Equation of State for Fluids and Fluid Mixtures. Chem. Eng. Sci. 37(3) (1982) 463-473, http://dx.doi.org/10.1016/0009-2509(82)80099-7

  504. Pawar, S.S., Sunnapwar, V.K.; Studies on convective heat transfer through helical coils. Heat Mass Transfer 49(12) (2013) 1741-1754, http://dx.doi.org/10.1007/s00231-013-1210-3

  505. Pawar, S.S., Sunnapwar, V.K.; Experimental studies on heat transfer to Newtonian and non-Newtonian fluids in helical coils with laminar and turbulent flow. Exp. Thermal Fluid Sci. 44 (2013) 792-804, http://dx.doi.org/10.1016/j.expthermflusci.2012.09.024

  506. Peng, D.-Y.; Accelerated Successive Substitution Schemes for Bubble-Point and Dew-Point Calculations. Can. J. Chem. Eng. 69(4) (1991) 978-985, http://dx.doi.org/10.1002/cjce.5450690421

  507. Peng, D.-Y., Robinson, D.B.; A New Two-Constant Equation of State. Ind. Eng. Chem. Fund. 15(1) (1976) 59-64, http://dx.doi.org/10.1021/i160057a011

  508. Peng, D.-Y., Robinson, D.B.; Two- and Three-Phase Equilibrium Calculations for Coal Gasification and Related Processes. in Newman, Barner, Klein, Sandler (Eds.). Thermodynamic of Aqueous Systems with Industrial Applications. ACS (1980), pag. 393-414, http://dx.doi.org/10.1021/bk-1980-0133.ch020

  509. Penoncello, S.G., Jacobsen, R.T., Goodwin, A.R.H.; A Thermodynamic Property Formulation for Cyclohexane. Int. J. Thermophys., 16(2) (1995) 519-531, http://dx.doi.org/10.1007/BF01441918

  510. Penoncello, S.G., Lemmon, E.W., Jacobsen, R.T, Shan, Z.; A Fundamental Equation for Trifluoromethane (R-23). J. Phys. Chem. Ref. Data 32(4) (2003) 1473-1499, http://dx.doi.org/10.1063/1.1559671

  511. Penoncello, S.G., Shan, Z., Jacobsen, R.T.; A Fundamental Equation for the Calculation of the Thermodynamic Properties of Trifluoromethane (R23). ASHRAE Trans. 106(Part 1) (2000) 739-756

  512. Perkins, H.C., Woroe-Schmidt, P.; Turbulent Heat and Momentum Transfer for Gases in a Circular Tube at Wall to Bulk Temperature Ratios to Seven. Int. J. Heat Mass Transfer 8(7) (1965) 1011-1031, http://dx.doi.org/10.1016/0017-9310(65)90085-2

  513. Perkins, R.A, Ramires, M.L.V., Nieto de Castro, C.A., Cusco, L.; Measurement and Correlation of the Thermal Conductivity of Butane from 135 K to 600 K at Pressures to 70 MPa. J. Chem. Eng. Data 47(5) (2002) 1263-1271, http://dx.doi.org/10.1021/je0101202

  514. Perkins, R.A.; Measurement and Correlation of the Thermal Conductivity of Isobutane from 114 K to 600 K at Pressures to 70 MPa. J. Chem. Eng. Data 47(5) (2002) 1272-1279, http://dx.doi.org/10.1021/je010121u

  515. Perkins, R.A. Hammerschmidt, U., Huber, M.L.; Measurement and Correlation of the Thermal Conductivity of Methylcyclohexane and Propylcyclohexane from 300 to 600 K at Pressures to 60 MPa. J. Chem. Eng. Data 53(9) (2008) 2120-2127, http://dx.doi.org/10.1021/je800255r

  516. Perkins, R.A., Friend, D.G., Roder, H.M., Nieto de Castro, C.A.; Thermal Conductivity Surface of Argon: A Fresh Analysis. Int. J. Thermophys., 12(6) (1991) 965-984, http://dx.doi.org/10.1007/BF00503513

  517. Perkins, R.A., Huber, M.L.; Measurement and Correlation of the Thermal Conductivities of Biodiesel Constituent Fluids: Methyl Oleate and Methyl Linoleate. Energy Fuels 25(5) (2011) 2383-2388, http://dx.doi.org/10.1021/ef200417x

  518. Perkins, R.A., Huber, M.L.; Measurement and Correlation of the Thermal Conductivity of Pentafluoroethane (R125) from 190 K to 512 K at Pressures to 70 MPa. J. Chem. Eng. Data 51(3) (2006) 898-904, http://dx.doi.org/10.1021/je050372t

  519. Perkins, R.A., Huber, M.L.; Measurement and Correlation of the Thermal Conductivity of 2,3,3,3-Tetrafluoroprop-1-ene (R1234yf) and trans-1,3,3,3-Tetrafluoropropene (R1234ze(E)). J. Chem. Eng. Data 56(12) (2011) 4868-4874, http://dx.doi.org/10.1021/je200811n

  520. Perkins, R.A., Huber, M.L.; Measurement and Correlation of the Thermal Conductivity of trans-1-Chloro-3,3,3-trifluoropropene (R1233zd(E)). J. Chem. Eng. Data 62(9) (2017) 2659-2665, http://dx.doi.org/10.1021/acs.jced.7b00106

  521. Perkins, R.A., Huber, M.L.; Measurement and Correlation of the Thermal Conductivity of cis-1,1,1,4,4,4-hexafluoro-2-butene. Int. J. Thermophysics 41 (2020) 103, http://dx.doi.org/10.1007/s10765-020-02681-0

  522. Perkins, R.A., Huber, M.L.; Measurement and Correlation of the Thermal Conducitivity of 1,1,1,2,2,4,5,5,5-Nanofluoro-4-(trifluromethyl)-3-pentanone. J. Chem. Eng. Data 63(8) (2018) 2783-2789, http://dx.doi.org/10.1021/acs.jced.8b00132

  523. Perkins, R.A., Huber, M.L., Assael, M.J.; Measurements of the Thermal Conductivity of 1,1,1,3,3-Pentafluoropropane (R245fa) and Correlations for the Viscosity and Thermal Condutivity Surfaces. J. Chem. Eng. Data 61(9) (2016) 3286-3294, http://dx.doi.org/10.1021/acs.jced.6b00350

  524. Perkins, R.A., Huber, M.L., Assael, M.J.; Measurement and Correlation of the Thermal Conductivity of 1,1,1,2,2,3,3-Heptafluoro-3-methoxypropane (RE-347mcc). Int. J. Thermophys. 43(1) (2022) 12, http://dx.doi.org/10.1007/s10765-021-02941-7

  525. Perkins, R.A., Laesecke, A., Howley, J., Ramires, M.L.V., Gurova, A.N., Cusco, L.; Experimental Thermal conductivity Values for the IUPAC Round-Robin Sample of 1,1,1,2-tetrafluoroethane (R134a). NIST Interagency/Internal Report (NISTIR) - 6605, http://dx.doi.org/nistir6605

  526. Perry’s Chemical Engineers’ Handbook 7th Edition. McGraw Hill (1997)

  527. Perry’s Chemical Engineers’ Handbook 8th Edition. McGraw Hill (2008)

  528. Perry’s Chemical Engineers’ Handbook 9th Edition. McGraw-Hill (2019)

  529. Piao, C.-C., Noguchi, M.; An International Standard Equation of State for the Thermodynamic Properties of HFC-125 (Pentafluoroethane). J. Phys. Chem. Ref. Data, 27(4) (1998) 775-806, http://dx.doi.org/10.1063/1.556021

  530. Piazza, L., Span, R.; An equation of state for methanol including the association term of SAFT. Fluid Phase Equilib. 349 (2013) 12-24, http://dx.doi.org/10.1016/j.fluid.2013.03.024

  531. Piazza, L., Span, R.; An equation of state for acetic acid including the association term of SAFT. Fluid Phase Equilib. 303 (2011) 134-149, http://dx.doi.org/10.1016/j.fluid.2011.01.008

  532. Pimenta, T.A., Campos, J.B.L.M.; Friction losses of Newtonian and non-Newtonian fluids flowing in laminar regime in a helical coil. Exp. Thermal Fluid Sci. 36 (2012) 194-204, http://dx.doi.org/10.1016/j.expthermflusci.2011.09.013

  533. Pimenta, T.A., Campos, J.B.L.M.; Heat transfer coefficients from Newtonian and non-Newtonian fluids flowing in laminar regime in a helical coil. Int. J. Heat Mass Transfer 58 (2013) 676-690, http://dx.doi.org/10.1016/j.ijheatmasstransfer.2012.10.078

  534. Piriyarungrod, N., Eiamsa-ard, S., Thianpong, C., Pimsarn, M., Nanan, K.; Heat transfer enhancement by tapered twisted tape inserts. Chem. Eng. Process. 96 (2015) 62-71, http://dx.doi.org/10.1016/j.cep.2015.08.002

  535. Platzer, B., Polt, A., Maurer, G.; Thermophysical Properties of refrigerants. Berlin: Springer-Verlag, 1990.

  536. Platzer, B., Polt, A., Maurer, G.; Thermophysical Properties of Refrigerants. Berlin: Springer-Verlag, 1990.

  537. Plöcker, U., Knapp, H., Prausnitz, J.; Calculation of High-Pressure Vapor-Liquid Equilibria from a Corresponding-States Correlation with Emphasis on Asymmetric Mixtures. Ind. Eng. Chem. Process Des. Dev. 17(3) (1978) 324-332, http://dx.doi.org/10.1021/i260067a020

  538. Poling, B.E, Prausnitz, J.M, O’Connell, J.P; The Properties of Gases and Liquids 5th Edition. McGraw-Hill, New York, 2001

  539. Polt, A., Platzer, B., Maurer, G.; Parameter der thermischen Zustandsgleichung von Bender fuer 14 mehratomige reine Stoffe. Chem. Technik 22(1992)6 - 216/224

  540. Polt, A., Platzer, B., Maurer, G.; Parameter der thermischen Zustandsgleichung von Bender fuer 14 mehratomige reine Stoffe. Chem. Technik 22(1992)6 , 216/224

  541. Polychroniadou, S., Antoniadis, K.D., Assael, M.J., Bell, I.H.; A Reference Correlation for the Viscosity of Krypton From Entropy Scaling. Int. J. Thermophys. 43 (2022) 6, http://dx.doi.org/10.1007/s10765-021-02927-5

  542. Ponnada, S., Subrahmanyam, T., Naidu, S.V.; A comparative study on the thermal performance of water in a circular tube with twisted tapes, perforated twisted tapes and perforated twisted tapes with alternate axis. Int. J. Thermal Sci. 136 (2019) 530-538, http://dx.doi.org/10.1016/j.ijthermalsci.2018.11.008

  543. Prasad, B.V.S.S.S., Das, D.H., Prabhaker, A.K.; Pressure Drop, Heat Transfer and Performance of a Helically Coiled Tubular Exchanger. Heat Recovery Systems & CHP 9(3) (1989) 249-256, http://dx.doi.org/10.1016/0890-4332(89)90008-2

  544. Proust, P., Vera, J.H.; PRSV: The Stryjek-Vera Modification of the Peng-RobinsonEquation of Stte. Parameters for Other Pure Compounds of Industrial Interest. Can. J. Chem. Eng. 67 (1989) 170-173, http://dx.doi.org/10.1002/cjce.5450670125

  545. Przedziecki, J.W., Sridhar, T.; Prediction of Liquid Viscosities. AIChE Journal 31(2) (1985) 333-335, http://dx.doi.org/10.1002/aic.690310225

  546. Péneloux, A., Rauzy, E., Fréze, R.; A Consistent Correction for Redlich-Kwong-Soave Volumes. Fluid Phase Equilibria 8 (1982) 7-23, http://dx.doi.org/10.1016/0378-3812(82)80002-2

  547. Qi, H., Fang, D., Gao, K., Meng, X., Wu, J.; Compressed Liquid Densities and Helmholtz Energy Equation of State for Fluoroethane (R161). Int. J. Thermophys. 37(3) (2016) 55, http://dx.doi.org/10.1007/s10765-016-2061-1

  548. Quinones-Cisneros, S.E., Schmidt, K.A.G., Giri, B.R, Blais, P., Marriott, R.A.,; Reference Correlation for the Viscosity Surface of Hydrogen Sulfide. J. Chem. Eng. Data 57(11) (2012) 3014-3018, http://dx.doi.org/10.1021/je300601h

  549. Quiñones-Cisneros, S.E., Deiters, U.K.; Generalization of the Friction Theory for Viscosity Modeling. J. Phys. Chem. B, 110(25) (2006) 12820-12834, http://dx.doi.org/10.1021/jp0618577

  550. Quiñones-Cisneros, S.E., Huber, M.L., Deiters, U.K.; Correlation for the Viscosity of Sulfur Hexafluoride (SF6) from the Triple Point to 1000 K and Pressures to 50 MPa. J. Phys. Chem. Ref. Data 41(2) (2012) 023102, http://dx.doi.org/10.1063/1.3702441

  551. Rabinovich, V.A., Vasserman, A.A., Nedostup, V.I., Veksler, L.S.; Thermophysical Properties of Neon, Argon, Krypton, and Xenon. Hemisphere Publishing Corp., 1988.

  552. Rachford, H.H., Rice, J.D.; Procedure for Use of Electronic Digital Computers in Calculating Flash Vaporization Hydrocarbon Equilibrium. Petroleum Transactions, AIME 195 (1952) 327-328, http://dx.doi.org/10.2118/952327-G

  553. Rackett, H.G.; Equation of State for Saturated Liquids. J. Chem. Eng. Data 15(4) (1970) 514-517, http://dx.doi.org/10.1021/je60047a012

  554. Ratanapisit, J., Ely, J.F.; Application of New, Modified BWR Equations of State to the Corresponding-States Prediction of Natural Gas Properties. Int. J. Thermophys., 20(6) (1999) 1721-1735, http://dx.doi.org/10.1023/A:1022610013596

  555. Ravigururajan, T.S., Bergles, A.E.; Development and Verification of General Correlations forPressure Drop and Heat Transfer in Single-Phase Turbulent Flow in Enhanced Tubes. Exp. Thermal Fluid Sci. 13(1) (1996) 55-70, http://dx.doi.org/10.1016/0894-1777(96)00014-3

  556. Rea, H.E., Spencer, C.F., Danner, R.P.; Effect of Pressure and Temperature on the Liquid Densities of Pure Hydrocarbons. J. Chem. Eng. Data 18(2) (1973) 227-230, http://dx.doi.org/10.1021/je60057a003

  557. Reddy, K.V.S., Pei, D.C.T.; Particle Dynamics in Solids-Gas Flow in a Vertical Pipe. Ind. Eng. Chem. Fundamen. 8(3) (1969) 490-497, http://dx.doi.org/10.1021/i160031a020

  558. Redlich, O., Kwong, J.N.S.; On the Thermodynamnics of Solutions V. An Equation of State. Fugacities of Gaseous Solutions. Chem. Rev. 44 (1949) 233-244, http://dx.doi.org/10.1021/cr60137a013

  559. Reeves, L.E., Scott, G.J., Babb, S.E. Jr.; Melting Curves of Pressure-Transmitting fluids. Fluid Phase Equilib., 222-223 (2004) 107-118, http://dx.doi.org/10.1063/1.1725068

  560. Reid, R., Prausnitz, J.M., Sherwood, T.; The Properties of Gases and Liquids, 3rd ed. New York:McGraw-Hill, 1977, p. 21..

  561. Rhodes, M.; Introduction to Particle Technology 2Ed. (John Wiley & Sons) 2008, http://dx.doi.org/10.1002/9780470727102

  562. Riazi, M. R.; Characterization and Properties of Petroleum Fractions.. ASTM manual series MNL50, 2005

  563. Riazi, M.R.; Distribution Model for Properties of Hydrocarbon-Plus Fractions. Ind. Eng. Chem. Res. 28(11) (1989) 1731-1735., http://dx.doi.org/10.1021/ie00095a026

  564. Riazi, M.R., A1-Sahhaf, T.; Physical Properties of n-Alkanes and n-Alkyl Hydrocarbons: Application to Petroleum Mixtures. Ind. Eng. Chem. Res. 34(11) (1995) 4145-4148, http://dx.doi.org/10.1021/ie00038a062

  565. Riazi, M.R., A1-Sahhaf, T.A.; Physical Properties of Heavy Petroleum Fractions and CrudeOils. Fluid Phase Equilibria 117 (1996) 217-224., http://dx.doi.org/10.1016/s0378-3812(98)00251-9

  566. Riazi, M.R., Al-Sahhaf, T.A., Sl-Shammari M.A.; A Generalized Method for Estimation of Critical Constants. Fluid Phase Equilibria 147 (1998) 1-6, http://dx.doi.org/10.1016/s0378-3812(98)00251-9

  567. Riazi, M.R., Daubert, T.E.; Characterization Parameters for Petroleum Fractions. Ind. Eng. Chem. Res. 26(4) (1987) 755-759, http://dx.doi.org/10.1021/ie00064a023

  568. Riazi, M.R., Daubert, T.E.; Simplify Property Predictions. Hydrocarbon Processing (March 1980): 115–116

  569. Riazi, M.R., Daubert, T.E.; Analytical Correlations Interconvert Distillation Curve Types. Oil & Gas Journal 84 (1986) 50-57

  570. Riazi, M.R., Faghri, A.; Thermal Conductivity of Liquid and Vapor Hydrocarbon Systems: Pentanes and Heavier at Low Pressures. Ind. Eng. Chem. Process Des. Dev. 24 (1985) 398-401, http://dx.doi.org/10.1021/i200029a030

  571. Riazi, M.R., Nasimi, N., Roomi, Y.; Estimating Sulfur Content of Petroleum Products and Crude Oils. Ind. Eng. Chem. Res. 38(11) (1999) 4507-4512, http://dx.doi.org/10.1021/ie990262d

  572. Richardson, I.A., Leachman, J.W., Lemmon, E.W.; Fundamental Equation of State for Deuterium. J. Phys. Chem. Ref. Data 43(1) (2014) 013103, http://dx.doi.org/10.1063/1.4864752

  573. Richter, M., McLinden, M.O., Lemmon, E.W.; Thermodynamic Properties of 2,3,3,3-Tetrafluoroprop-1-ene (R1234yf): Vapor Pressure and p-ρ-T Measurements and an Equation of State. J. Chem. Eng. Data, 56(7) (2011) 3254-3264, http://dx.doi.org/10.1021/je200369m

  574. Riedel, L.; Kritischer Koeffizient, Dichte des gesättigten Dampfes und Verdampfungswärme: Untersuchungen über eine Erweiterung des Theorems der übereinstimmenden Zustände. Teil III. Chem. Ingr. Tech., 26(12) (1954) 679-683, http://dx.doi.org/10.1002/cite.330261208

  575. Riedel, L.; Die Zustandsfunktion des realen Gases: Untersuchungen über eine Erweiterung des Theorems der übereinstimmenden Zustände. Chem. Ings-Tech. 28 (1956) 557-562, http://dx.doi.org/10.1002/cite.330280809

  576. Riedel, L.; Die Flüssigkeitsdichte im Sättigungszustand. Untersuchungen über eine Erweiterung des Theorems der übereinstimmenden Zustände. Teil II.. Chem. Eng. Tech. 26(5) (1954) 259-264, http://dx.doi.org/10.1002/cite.330260504

  577. Rizk, F.; Pneumatic conveying at optimal operation conditions and a solution of Bath’s equation. Proceedings of Pneumotransport 3, paper D4. BHRA Fluid Engineering, Cranfield, England (1973)

  578. Robinson, D.B., Peng, D.Y.; The characterization of the heptanes and heavier fractions. Research Report 28. GPA, 1978. Tulsa, OK.

  579. Rogers, G.F.C., Mayhew, Y.R.; Heat Transfer and Pressure Loss in Helically Coiled Tubes with Turbulent Flow. Int. J. Heat Mass Transfer 7(11) (1964) 1207-1216, http://dx.doi.org/10.1016/0017-9310(64)90062-6

  580. Romeo, E., Royo, C., Monzon, A.; Improved explicit equation for estimation of the frictionfactor in rough and smooth pipes.. Chem. Eng. J. 86(3) (2002) 369-374, http://dx.doi.org/10.1016/S1385-8947(01)00254-6

  581. Romeo, R., Lemmon, E.W.; Equations of State for n-Hexadecane and n-Docosane. Int. J. Thermophys. 43 (2022) 146, http://dx.doi.org/10.1007/s10765-022-03059-0

  582. Round, G.F.; An Explicit Approximation for the Friction Factor-ReynoldsNumber Relation for Rough and Smooth Pipes. Can. J. Chem. Eng. 58 (1980) 122-123, http://dx.doi.org/10.1002/cjce.5450580119

  583. Rowe, A.M.; Internally Consistent Correlations for Predicting PhaseCompositions for Use in Reservoir Compositional Simulators. Paper SPE 7475, In: Presented at the 53rd Annual Society ofPetroleum Engineers Fall Technical Conference and Exhibition,1978., http://dx.doi.org/10.2118/7475-MS

  584. Rui, X., Pan, J., Wang, Y.; An Equation of State for Thermodynamic Properties of 1,1,1,2,3,3-Hexafluoropropane (R236ea). Fluid Phase Equilibria 341 (2013) 78-85, http://dx.doi.org/10.1016/j.fluid.2012.12.026

  585. Saha, S.K., Gaitonde, U.N., Date, A.W.; Heat Transfer and Pressure Drop Characteristics of Laminar Flow in a Circular Tube Fitted with Regularly Spaced Twisted-Tape Elements. Exp. Thermal Fluid Sci. 2(3) (1989) 310-322, http://dx.doi.org/10.1016/0894-1777(89)90020-4

  586. Sakoda, N., Uematsu, M.; A Thermodynamic Property Model for Fluid Phase Hydrogen Sulfide. Int. J. Thermophys., 25(3) (2004) 709-737, http://dx.doi.org/10.1023/B:IJOT.0000034234.06341.8a

  587. Salerno, S, Cascella, M., May, D., Watson, P., Tassios, D.; Prediction of Vapor Pressures and Saturated Volumes with aSimple Cubic Equation of State: Part I. A Reliable DataBase. Fluid Phase Equilibria 27 (1986) 15-34, http://dx.doi.org/10.1016/0378-3812(86)87038-8

  588. Salim, P.H., Trebble, M.A.; A Modified Trebble-Bishnoi Equation of State: Thermodynamic Consistency Revisited. Fluid Phase Equilibria 65 (1991) 59-71, http://dx.doi.org/10.1016/0378-3812(91)87017-4

  589. Salimpour, M.R.; Heat transfer coefficients of shell and coiled tube heat exchangers. Exp. Thermal Fluid Sci. 33(2) (2009) 203-207, http://dx.doi.org/10.1016/j.expthermflusci.2008.07.015

  590. Samadianfard, S.; Gene expression programming analysis of implicit Colebrook-White equation in turbulent flow friction factor calculation. J. Pet. Sci. Eng. 92-93 (2012) 48-55, http://dx.doi.org/10.1016/j.petrol.2012.06.005

  591. Sancet, J.,; Heavy Faction C7+ Characterization for PR-EOS.. SPE 113025, 2007 SPE Annual Conference, November 11–14,Anaheim, CA 2007., http://dx.doi.org/10.2118/113026-stu

  592. Sandarusi, J.A., Kidnay, A.J., Yesavage, V.F.; Compilation of Parameters for a Polar Fluid Soave-Redlich-Kwong Equation of State. Ind. Eng. Chem. Process Des. Dev. 25(4) (1986) 957-963, http://dx.doi.org/10.1021/i200035a020

  593. Sanjari E, Lay E.N.; An accurate empirical correlation for predicting natural gas compressibility factors.. Journal of Natural Gas Chemistry 21(2012):184-188., http://dx.doi.org/10.1016/s1003-9953(11)60352-6

  594. Sanjari, E., Honarmand, M., Badihi, H., Ghaheri, A.; An Accurate Generalized Model for Predict Vapor Pressure of Refrigerants. International Journal of Refrigeration 36 (2013) 1327-1332, http://dx.doi.org/10.1016/j.ijrefrig.2013.01.007

  595. Santamaría-Pérez, D., Mukherjee, G.D., Schwager, B., Boehler, R.; High-pressure melting curve of helium and neon: Deviations from corresponding states theory. Physical Review B 81 (2010) 214101, http://dx.doi.org/10.1103/PhysRevB.81.214101

  596. Sarem, A.M.; Z-Factor Equation Developed for Use in Digital Computers.. Oil and Gas J. (Sept. 18, 1961) 118

  597. Sarma, P.K., Kishore, P.S., Rao, V.D., Subrahnamyam, T.; A Conbined approach to predict friction coefficients and convective heat transfer characteristics in A tube with twisted tape inserts for a wide range of Re and Pr. Int. J. Therm. Sciences 44(4) (2005) 393-398, http://dx.doi.org/10.1016/j.ijthermalsci.2004.12.001

  598. Sastri, S.R.S., Rao, K.K.; A Simple Method to Predict Surface Tension of Organic Liquids. Chem. Eng. Journal 59(2) (1995) 181-186, http://dx.doi.org/10.1016/0923-0467(94)02946-6

  599. Saul, A., Wagner, W.; A Fundamental Equation for Water Covering theRange from the Melting Line to 1273 K atPressures up to 25000 MPa. J. Phys. Chem. Ref. Data 18(4) (1989) 1537-1564, http://dx.doi.org/10.1063/1.555836

  600. Scalabrin, G., Marchi, P., Finezzo, F.; A Reference Multiparameter Thermal Conductivity Equation for Carbon Dioxide with an Optimized Functional Form. J. Phys. Chem. Ref. Data 35(4) (2006) 1549-1575, http://dx.doi.org/10.1063/1.2213631

  601. Schmidt, E.F.; Wärmeübergand und Druckverlust in Rohrschlangen. Chemie Ingenieur Technik 39(13) (1967) 781-789, http://dx.doi.org/10.1002/cite.330391302

  602. Schmidt, K.A.G., Carroll, J.J., Quinones-Cisneros, S.E., Kvamme, B.; Hydrogen Sulfide Viscosity Modeling. Energy & Fuels 22(5) (2008) 3424-3434, http://dx.doi.org/10.1021/ef700701h

  603. Schmidt, R., Wagner, W.; A New Form of the Equation of State for Pure Substances and its Application to Oxygen. Fluid Phase Equuilibria. 19 (1985) 175-200, http://dx.doi.org/10.1016/0378-3812(85)87016-3

  604. Schroeder, J.A.; Penoncello, S.G.; Schroeder, J.S.; A Fundamental Equation of State for Ethanol. J. Phys. Chem. Ref. Data 43(4) (2014) 043102, http://dx.doi.org/10.1063/1.4895394

  605. Seban R.A., McLaughlin, E.F.; Heat Transfer in Tube Coils with Laminar and Turbulent Flow. Int. J. Heat Mass Transfer 6() (1963) 387-395, http://dx.doi.org/10.1016/0017-9310(63)90100-5

  606. Serghides, T.K.; Estimate friction factor accurately. Chem. Eng., 91(5) (1984) 63-64.

  607. Seth, K.K., Stahel, E.P.; Heat Transfer from Helical Coils Immersed in Agitated Vessels. Ind. Eng. Chem. 61(6) (1969) 39-49, http://dx.doi.org/10.1021/ie50714a007

  608. Sethumadhavan, R., Raja Rao, M.; Turbulent Flow Friction and Heat Transfer Characteristics of Single and Multistart Spirally Enghanced Tubes. J. Heat Transfer 108(1) (1986) 55-61, http://dx.doi.org/10.1115/1.3246905

  609. Sethumadhavan, R., Raja Rao, M.; Turbulent Flow Heat Transfer and Fluid Friction in Helical-Wire-Coil-Inserted Tubes. Int. J. Heat Mass Transfer 26(12) (1983) 1833-1845, http://dx.doi.org/10.1016/s0017-9310(83)80154-9

  610. Setzmann, U., Wagner, W.; A New Equation of State and Tables of Thermodynamic Properties for Methane Covering the Range from the Melting Line to 625 K at Pressures up to 1000 MPa. J. Phys. Chem. Ref. Data, 20(6) (1991) 1061-1155, http://dx.doi.org/10.1063/1.555898

  611. Shacham. M.; An explicit equation for friction factor in pipe. Ind. Eng. Chem. Fund. 19 (1981) 228-229.

  612. Shah, R.K., London, A.L.; Laminar Flow Forced Convection in Ducts: A Source Book for Compact Heat Exchanger Analytical Data. Academic Press 1978

  613. Shah, R.K., Sekulić, D.P.; Fundamentals of Heat Exchanger Design. John Wiley & Sons

  614. Shan, Z., Penoncello, S.G., Jacobsen, R.T.; A Generalized Model for Viscosity and Thermal Conductivity of Trifluoromethane (R-23). ASHRAE Trans. 106(Part 1) (2000) 757-767

  615. Shchukin, V.K.; Correlation of Experimental Data on Heat Transfer in Curved Pipes. Teploenergetika 16(2) (1969) 72-76

  616. Shokir, Eissa M.El-M., El-Awad, Musaed N., Al-Quraishi, Adulhrahman A., Al-Mahdy, Osama A.; Compressibility factor model of sweet, sour, and condensate gases using genetic programming. Chem. Eng. Res. Des. 90 (2012), 785-792., http://dx.doi.org/10.1016/j.cherd.2011.10.006

  617. Sieder, E.N., Tate, G.E.; Heat Transfer and Pressure Drop of Liquids in Tubes. Ind. & Eng. Chemistry 28(12) (1936) 1929-1935, http://dx.doi.org/10.1021/ie50324a027

  618. Silva, M.B., Rodriguez, F.; Automatic fitting of equations of state for phase behaviormatching.. Paper SPE 23703, Society of Petroleum Engineers, Richardson,TX, 1992., http://dx.doi.org/10.2118/23703-MS

  619. Sim, W.J., Daubert, T.E.; Prediction of Vapor-Liquid Equilibria of UndefinedMixtures. Ind. Eng. Chem. Process Des. Dev. 19(3) (1980) 386-393, http://dx.doi.org/10.1021/i260075a010

  620. Singh, B., Mutyala, S.R., Puttagunta, V.; Viscosity range from one test. Hydrocarbon Processing 69 (1990) 39-41

  621. Sivashanmugam, P., Nagarajan, P.K.; Studies on heat transfer and friction factor characteristics of laminar flow through a circular tube fitted with right and left helical screw-tape inserts. Exp. Thermal Fluid Sci. 32(1) (2007) 192-197, http://dx.doi.org/10.1016/j.expthermflusci.2007.03.005

  622. Sivashanmugam, P., Nagarajan, P.K., Suresh, S.; Experimental Studies on Heat Transfer and Friction Factor Characteristics of Turbulent Flow Through a Circular Tube Fitted with Right and Left Helical Screw-Tape Inserts. Chem. Eng. Comm. 195(8) (2008) 977-987, http://dx.doi.org/10.1080/00986440801906658

  623. Sivashanmugam, P., Suresh, S.; Experimental studies on heat transfer and friction factor characteristics of laminar flow through a circular tube fitted with helical screw-tape inserts. App. Thermal Eng. 26(16) (2006) 1990-1997, http://dx.doi.org/10.1016/j.applthermaleng.2006.01.008

  624. Sivashanmugam, P., Suresh, S.; Experimental studies on heat transfer and friction factor characteristics of turbulent flow through a circular tube fitted with helical screw-tape inserts. Chem. Eng. Processing 46(12) (2007) 1292-1298, http://dx.doi.org/10.1016/j.cep.2006.10.009

  625. Sivashanmugam, P., Suresh, S.; Experimental studies on heat transfer and friction factor characteristics of turbulent flow through a circular tube fitted with regularly spaced helical screw-tape inserts. App. Thermal Eng. 27(8-9) (2007) 1311-1319, http://dx.doi.org/10.1016/j.applthermaleng.2006.10.035

  626. Smithberg, E., Landis, F.; Friction and Forced Convection Heat-Transfer Characteristics in Tubes With Twisted Tape Swirl Generators. J. Heat Transfer. 86(1) (1964) 39-48, http://dx.doi.org/10.1115/1.3687060

  627. Smukala, J., Span, R., Wagner, W.; New equation of state for ethylene covering the fluid region from the melting line to 450 K at pressures up to 300 MPa. J. Phys. Chem. Ref. Data 29(5) (2000) 1053-1121, http://dx.doi.org/10.1063/1.1329318

  628. Soave, G.; Equilibrium Constants from a modified Redlich-Kwong Equation of State. Chem. Eng. Sci. 27 (1972) 1197-1203, http://dx.doi.org/10.1016/0009-2509(72)80096-4

  629. Soave, G.; Application of a Cubic Equation of State to Vapor-Liquid Equilibria of Systems Containing Polar Compounds. Inst. Chem. Eng. Symp. Ser. 56 (1979) 1.2/1-1.2/16

  630. Soave, G.; Improvement of the van der Waals Equation of State. Chem. Eng. Sci. 39(2) (1984) 357-369, http://dx.doi.org/10.1016/0009-2509(84)80034-2

  631. Soave, G.S.; An Effective Modification of the Benedict-Webb-Rubin Equation of State. Fluid Phase Equilibria 164(2) (1999) 157-172, http://dx.doi.org/10.1016/s0378-3812(99)00252-6

  632. Soave, G.S.; A Noncubic Equation of State for the Tretament of Hydrocarbon Fluids at Rerservoir Conditions. Ind. Eng. Chem. Res. 34(11) (1995) 3981-3994, http://dx.doi.org/10.1021/ie00038a039

  633. Sonnad, J.R., Goudar, C.T.; Explicit Reformulation of the Colebrook-White Equation for Turbulent Flow Frcition Factor Calculation. Ind. Eng. Chem. Res. 46(8) (2007) 2593-2600, http://dx.doi.org/10.1021/ie0340241

  634. Soreide, I.; Improved Phase Behavior Predictions of Petroleum ReservoirFluids From a Cubic Equation of State.. Doctor of engineering dissertation. Norwegian Institute ofTechnology, Trondheim, 1989.

  635. Sotiriadou, S., Ntonti, E., Assael, M.J., Huber, M.L.,; Reference Correlations of the Viscosity and Thermal Conductivity of 1-Hexene from the Triple Point to High Temmperatures and Pressures. Int. J. Thermophysics 44 (2023) 108, http://dx.doi.org/10.1007/s10765-023-03217-y

  636. Sotiriadou, S., Ntonti, E., Assael, M.J., Perkins, R.A., Huber, M.L.,; Reference Correlations of the Viscosity of Ethene from the Triple Point to 450 K and up to 195 MPa. Int. J. Thermophysics 45 (2024) 87, http://dx.doi.org/10.1007/s10765-024-03378-4

  637. Sotiriadou, S., Ntonti, E., Velliadou, D., Antoniadis, K.D., Assael, M.J., Huber, M.L.,; Reference Correlation for the Viscosity of Ethanol from the Triple Point to 620 K and Pressures up to 102 MPa. Int. J. Thermophysics 44 (2023) 40, http://dx.doi.org/10.1007/s10765-022-03149-z

  638. Sotiriadou, S.G., Ntonti, E., Assael, M.J., Huber, M.L.; Reference Correlation for the Viscosity and Thermal Conductivity of Acetone from the Triple Point to High Temperatures and Pressures. Int. J. Thermophys. 46(1) (2025) 3, http://dx.doi.org/10.1007/s10765-024-03465-6

  639. Span, R.; Multiparameter Equations of State: An Accurate Source of Thermodynamic Property Data. Springer, 2000

  640. Span, R., Lemmon, E.W., Jacobsen, R.T, Wagner, W., Yokozeki, A.; A Reference Equation of State for the Thermodynamic Properties of Nitrogen for Temperatures from 63.151 to 1000 K and Pressures to 2200 MPa. J. Phys. Chem. Ref. Data 29(6) (2000) 1361-1433, http://dx.doi.org/10.1063/1.1349047

  641. Span, R., Wagner, W.; Equations of state for technical applications. II. Results for nonpolar fluids.. Int. J. Thermophys. 24 (1) (2003) 41-109, http://dx.doi.org/10.1023/A:1022310214958

  642. Span, R., Wagner, W.; A New Equation of State for Carbon Dioxide Covering the Fluid Region from the Triple‐Point Temperature to 1100K at Pressures up to 800MPa. J. Phys. Chem. Ref. Data, 25(6) (1996) 1509-1596, http://dx.doi.org/10.1063/1.555991

  643. Span, R., Wagner, W.; Equations of State for Technical Applications. III. Results for Polar Fluids. Int. J. Thermophys., 24(1) (2003) 111-162, http://dx.doi.org/10.1023/A:1022362231796

  644. Spencer, C.F., Danner, R.P.; Improved Equation for Prediction of Saturated Liquid Density. J. Chem. Eng. Data 17(2) (1972) 236-241, http://dx.doi.org/10.1021/je60053a012

  645. Spencer, C.F., Danner, R.P.; Prediction of Bubble-Point Density of Mixtures. J. Chem. Eng. Data 18(2) (1973) 230-234, http://dx.doi.org/10.1021/je60057a007

  646. Srinivasan, P.S., Nandapurkar, S.S., Holland, F.A.; Pressure Drop and Heat Transfer in Coils. Chem. Eng. 218 (1968) 113-119

  647. Srinivasan, V., Christensen, R.N.; Experimental Investigation of Heat Transfer and Pressure Drop Characteristics of Flow Through Spirally Fluted Tubes. Exp. Thermal Fluid Sci. 5(6) (1992) 820-827, http://dx.doi.org/10.1016/0894-1777(92)90126-P

  648. Standing, M.B.; Volumetric and Phase Behavior of Oil Field HydrocarbonSystems.. Society of Petroleum Engineers, Dallas, TX. 1977

  649. Starling, K.E.; Fluid Thermodynamics Properties of Light Petroleum Systems. Gulf Publishing Company, 1973

  650. Starling, K.E.; Fluid Thermodynamic Properties for Light Petroleum Systems. Gulf Publishing Company, 1973.

  651. Stein, R.P., Begell, W.; Heat Transfer to Water in Turbulent Flow in Internally Heated Annuli. AIChE Journal 4(2) (1958) 127-131, http://dx.doi.org/10.1002/aic.690040203

  652. Stemerding, S.; The pneumatic transport of cracking catalyst in vertical risers. Chem. Eng. Sci. 17(8) (1962) 599-608, http://dx.doi.org/10.1016/0009-2509(62)80053-0

  653. Stephan, K.; Wärmeübergang bei turbulenter und bei laminarer Strömung in Ringspalten. Chem. Ing. Techn. 34(3) (1962) 207-212, http://dx.doi.org/10.1002/cite.330340313

  654. Stephan, K., Krauss, R., Laesecke, A.; Viscosity and Thermal Conductivity of Nitrogen for a Wide Range of Fluid States. J. Phys. Chem. Ref. Data 16(4) (1987) 993-1023, http://dx.doi.org/10.1063/1.555798

  655. Stewart, R.B., Jacobsen, R.T.; Thermodynamic Properties of Argon from the Triple Point to 1200 K at Pressures to 1000 MPa. J. Phys. Chem. Ref. Data, 18(2):639-798, 1989, http://dx.doi.org/10.1063/1.555829

  656. Stiel, L.I., Thodos, G.; The Viscosity of Nonpolar Gases at Normal Pressures. AIChE Journal 7(4) (1961) 611-615, http://dx.doi.org/10.1002/aic.690070416

  657. Stiel, L.I., Thodos, G.; The Viscosity of Polar Substances in the Dense Gaseous and Liquid Regions. AIChE Journal 10(2) (1964) 275-277, http://dx.doi.org/10.1002/aic.690100229

  658. Stiel, L.I., Thodos, G.; The Thermal Conductivity of Nonpolar Substances in the Dense Gaseous and Liquid Regions. AIChE Journal 10(1) (1964) 26-30, http://dx.doi.org/10.1002/aic.690100114

  659. Stryjek, R., Vera, J.H.; PRSV: An Improved Peng—Robinson Equation of State for Pure Compounds and Mixtures. Can. J. Chem. Eng. 64 (1986) 323-333, http://dx.doi.org/10.1002/cjce.5450640224

  660. Stryjek, R., Vera, J.H.; PRSV2: A Cubic Equation of State for Accurate Vapor—Liquid Equilibria calculations. Can. J. Chem. Eng. 64 (1986) 820–826, http://dx.doi.org/10.1002/cjce.5450640516

  661. Sun, L., Ely, J.F.; Universal equation of state for engineering application: Algorithm and application to non-polar and polar fluids. Fluid Phase Equilib., 222-223 (2004) 107-118, http://dx.doi.org/10.1016/j.fluid.2004.06.028

  662. Sun, L., Ely, J.F.; Universal equation of state for engineering application: Algorithm and application tonon-polar and polar fluids. Fluid Phase Equilib., 222-223 (2004) 107-118, http://dx.doi.org/10.1016/j.fluid.2004.06.028

  663. Sun, T.F., Schouten, J.A., Trappeniers, N.J., Biswas, S.N.; Accurate Measurement of the Melting Line of Methanol and Ethanol at Pressures up to 270 MPa. Ber. Bunsenges. Phys. Chem. 92 (1988) 652-655, http://dx.doi.org/10.1002/bbpc.198800153

  664. Sunaga, H., Tillner-Roth, R., Sato, H., Watanabe, K.; A Thermodynamic Equation of State for Pentafluoroethane (R-125). Int. J. Thermophys., 19(6) (1998) 1623-1635, http://dx.doi.org/10.1007/BF03344914

  665. Swamee, P.K., Ojha, C.S.P.; Drag Coefficient and Fall Velocity of Nonspherical Particles. J. Hydraul. Eng. 117(5) (1991) 660-667, http://dx.doi.org/10.1061/(ASCE)0733-9429(1991)117:5(660)

  666. Swamee, P.K.; Jain, A.K.; Explicit equations for pipe-flow problems. J. Hydraulics Division (ASCE) 102(5) (1976) 657-664.

  667. Sykioti, E.A., Assael, M.J., Huber, M.L.,Perkins, R.A.; Reference Correlations of the Thermal Conductivity of Methanol from the Triple Point to 660 K and up to 245 MPa. J. Phys. Chem. Ref. Data 42(4) (2013) 043101, http://dx.doi.org/10.1063/1.4829449

  668. Takacs., G.; Comparing Methods for Calculating Z-factor. Oil & Gas Journal, May 15, 1989, pp. 43-46.

  669. Tanaka, K., Higashi, Y.; Surface Tensions of trans-1,3,3,3-Tetrafluoropropene and trans-1,3,3,3-Tetrafluoropropene + Difluoromethane Mixture. J. Chem. Eng. Japan 46(6) (2013) 371-375, http://dx.doi.org/10.1252/jcej.13we021

  670. Tanaka, Y., Sotani, T.; Thermal Conductivity and Viscosity of 2,2-Dichioro-1,1,1-Trifluoroethane (HCFC-123). Int. J. Thermophys. 17(2) (1996) 293-328, http://dx.doi.org/10.1007/BF01443394

  671. Tarakad, R.R., Danner, R.P.; An Improved Corresponding States Method for Polar Fluids: Correlation of Second Virial Coefficients. AIChE J. 23(5) (1977) 685-695, http://dx.doi.org/10.1002/aic.690230510

  672. Tarbell, J.M., Samuels, M.R.; Momentum and Heat Transfer in Helical Coils. Chem. Eng. J. 5(2) (1973) 117-127, http://dx.doi.org/10.1016/0300-9467(73)80002-4

  673. Tariq, U., Jusoh, A.R.B., Riesco, N., Vesovic, V.; Reference Correlation of the Viscosity of Cyclohexane from the Triple Point to 700K and up to 110 MPa. J. Phys. Chem. Ref. Data 43(3) (2014) 033101, http://dx.doi.org/10.1063/1.4891103

  674. Tasidou, K.A., Huber, M.L., Assael, M.J.; Reference Correlation for the Viscosity of Cyclopentane from the Triple Point to 460 K and up to 380 MPa. J. Phys. Chem. Ref. Data 48(4) (2019) 043101, http://dx.doi.org/10.1063/1.5128321

  675. Tegeler, Ch., Span, R., Wagner, W.; A New Equation of State for Argon Covering the Fluid Region for Temperatures From the Melting Line to 700 K at Pressures up to 1000 MPa. J. Phys. Chem. Ref. Data 28, 779 (1999), http://dx.doi.org/10.1063/1.556037

  676. Terfous, A., Hazzab, A., Ghenaim, A.; Predicting the Drag Coefficient and Settling Velocity of Spherical Particles. Powder Technology 239 (2013) 12-20, http://dx.doi.org/10.1016/j.powtec.2013.01.052

  677. Thelen, B.; Python refprop wrapper, https://github.com/BenThelen/python-refprop.

  678. Thianpong, C., Eiamsa-ard, S., Somkleang, P.; Heat transfer and thermal performance characteristics of heat exchanger tube fitted with perforated twisted-tapes. Heat Mass Transfer 48(6) (2012) 881-892, http://dx.doi.org/10.1007/s00231-011-0943-0

  679. Thol, M., Dubberke, F.H., Baumhögger, E., Span, R., Vrabec, J.; Speed of Sound Measurements and a Fundamental Equation of State for Hydrogen Chloride. J. Chem. Eng. Data 63(7) (2018) 2533-2547, http://dx.doi.org/10.1021/acs.jced.7b01031

  680. Thol, M., Dubberke, F.H., Baumhögger, E., Vrabec, J., Span, R.; Speed of Sound Measuements and Fundamental Equations State for Octamethyltrisiloxane and Decamethyltetrasiloxane. J. Chem. Eng. Data 62(9) (2017) 2633-2648, http://dx.doi.org/10.1021/acs.jced.7b00092

  681. Thol, M., Dubberke, F.H., Rutkai, G., Windmann, T., Köster, A., Span, R., Vrabec, J.; Fundamental equation of state correlation for hexamethyldisiloxane based on experimental and molecular simulation data. Fluid Phase Equilibria 418 (2016) 133-151, http://dx.doi.org/10.1016/j.fluid.2015.09.047

  682. Thol, M., Fenkl, F., Lemmon, E.W.; A Fundamental Equation of State for Chloroethene for Temperatures from the Triple Point to 430 K and Pressures to 100 MPa. Int. J. Themophysics 42 (2022) 41, http://dx.doi.org/10.1007/s10765-021-02961-3

  683. Thol, M., Herrig, S., Span, R., Lemmon, E.W.; A fundamental equation of state for the calculation of thermodynamic proeprties of chlorine. AIChE J. 67(9) (2021) 2633-2648, http://dx.doi.org/10.1002/aic.17326

  684. Thol, M., Javed, M.A., Baumhögger, E., Span, R., Vrabec, J.; Thermodynamic Properties of Dodecamethylpentasiloxane, Tetradecamethylhexasiloxane, and Decamethylcyclopentasiloxane. Ind. Eng. Chem. Res. 58(22) (2019) 9617-9635, http://dx.doi.org/10.1021/acs.iecr.9b00608

  685. Thol, M., Lemmon, E.W.; Equation of State for the ThermodynamicProperties of trans-1,3,3,3-Tetrafluoropropene[R-1234ze(E)]. Int. J. Thermophys. 37(3) (2016) 28, http://dx.doi.org/10.1007/s10765-016-2040-6

  686. Thol, M., Lemmon, E.W., Span, R.; Equation of State for Benzene for Temperatures from the Melting Line up to 750 K with Pressures up to 500 MPa. High Temperatures-High Pressures 41 (2012) 81-97

  687. Thol, M., Piazza, L., Span, R.; A New Functional Form for Equations of State for Some Weakly Associating Fluids. Int. J. Thermophys., 35(5):783-811, 2014., http://dx.doi.org/10.1007/s10765-014-1633-1

  688. Thol, M., Rutkai, G., Köster, A., Dubberke, F.H., Windmann, T., Span, R., Vrabec, J.; Thermodynamic Properties of Octamiethylciyclotetrasilosane. J. Chem. Eng. Data 61(7) (2016) 2580-2595, http://dx.doi.org/10.1021/acs.jced.6b00261

  689. Thol, M., Rutkai, G., Köster, A., Kortmann, M., Span, R., Vrabec, J.; Corrigendum to ‘Fundamental equation of state for ethylene oxide based on a hybrid dataset. Chem. Eng. Sci. 134 (2015) 887-890, http://dx.doi.org/10.1016/j.ces.2015.06.020

  690. Thol, M., Rutkai, G., Köster, A., Kortmann, M., Span, R., Vrabec, J.; Fundamental equation of state for ethylene oxide based on a hybrid dataset. Chem. Eng. Sci. 121 (2015) 87-99, http://dx.doi.org/10.1016/j.ces.2014.07.051

  691. Thol, M., Rutkai, G., Köster, A., Lustig, R., Span, R., Vrabec, J.; Equation of State for the Lennard-Jones Fluid. J. Phys. Chem. Ref. Data 45(2) (2016) 023101, http://dx.doi.org/10.1063/1.4945000

  692. Thol, M., Rutkai, G., Köster, A., Miroshnichenko, S., Wagner, W., Vrabec, J., Span, R.; Equation of state for 1,2-dichloroethane based on a hybrid data set. Molecular Physics 115(9-12) (2017) 1166-1185, http://dx.doi.org/10.1080/00268976.2016.1262557

  693. Thomson, G.H., Brobst, K.R., Hankinson, R.W.; An Improved Correlation for Densities of Compressed Liquids and Liquid Mixtures. AIChE Journal 28(4) (1982): 671-76, http://dx.doi.org/10.1002/aic.690280420

  694. Thorade, M., Saadat, A.; Partial derivatives of thermodynamic state properties for dynamic simulation. Environ Eartth Sci 70(8) (2013) 3497-3503, http://dx.doi.org/10.1007/s12665-013-2394-z

  695. Tillner-Roth, R.; A Fundamental Equation of State for 1,1-Difluoroethane (HFC-152a). Int. J. Thermophys., 16(1) (1995) 91-100, http://dx.doi.org/10.1007/BF01438960

  696. Tillner-Roth, R., Baehr, H.D.; An International Standard Formulation for the Thermodynamic Properties of 1,1,1,2-Tetrafluoroethane (HFC-134a) for Temperatures from 170 K to 455 K at Pressures up to 70 MPa. J. Phys. Chem. Ref. Data 23(5) (1994) 657-729, http://dx.doi.org/10.1063/1.555958

  697. Tillner-Roth, R., Yokozeki, A.; An International Standard Equation of State for Difluoromethane (R-32) for Temperatures from the Triple Point at 136.34 K to 435 K at Pressures up to 70 MPa. J. Phys. Chem. Ref. Data 26(6) (1997) 1273-1328, http://dx.doi.org/10.1063/1.556002

  698. Trebble, M.A.; Calculation of Constants in the Trebble-Bishnoi Equation of State with an Extended Corresponding States Approach. Fluid Phase Equilibria 45 (1989) 165-172, http://dx.doi.org/10.1016/0378-3812(89)80255-9

  699. Trebble, M.A., Bishnoi, P.R.; Development of a New Four-Parameter Cubic Equation of State. Fluid Phase Equilibria 35 (1987) 1-8, http://dx.doi.org/10.1016/0378-3812(87)80001-8

  700. Triboix, A.; Exact and approximate formulas for cross flow heat exchangers with unmixed fluids. Int. Comm. Heat Mass Transfer 36(2) (2009), http://dx.doi.org/10.1016/j.icheatmasstransfer.2008.10.012

  701. Tsal, R.J.; Altshul-Tsal friction factor equation. Heating Piping Air Conditioning 8 (1989), 30-45.

  702. Tsolakidou, C.M., Assael, M.J., Huber, M.L.,Perkins, R.A.; Correlations for the Viscosity and Thermal Conductivity of Ethyl Fluoride (R161). J. Phys. Chem. Ref. Data 46(2) (2017) 023103, http://dx.doi.org/10.1063/1.4983027

  703. Tsonopoulos, C.; An Empirical Correlation of Second Virial Coefficients. AIChE Journal 20(2) (1974) 263-272, http://dx.doi.org/10.1002/aic.690200209

  704. Tsonopoulos, C., Heidman, J.L., Hwang, S.C.; Thermodynamic and Transport Properties of Coal Liquids. An Exxon Monograph, Wiley, New York, 1986

  705. Tufeu, R., Ivanov, D.Y., Garrabos, Y., Le Neindre, B.; Thermal Conductivity of Ammonia in a Large Temperature and Pressure Range Including the Critical Region. Ber. Bunsenges. Phys. Chem. 88 (1984) 422-427, http://dx.doi.org/10.1002/bbpc.19840880421

  706. Turton, R., Levenspiel, O.; A Short Note on the Drag Correlation for Spheres. Powder Technology 47(1) (1986) 83-86, http://dx.doi.org/10.1016/0032-5910(86)80012-2

  707. Twu, C.H.; An Internally Consistent Correlation for Predicting theCritical Properties and Molecular Weights of Petroleum andCoal-tar Liquids. Fluid Phase Equilbria 16 (1984) 137-150, http://dx.doi.org/10.1016/0378-3812(84)85027-x

  708. Twu, C.H., Coon, J.E., Cunningham, J.R.; A New Generalized Alpha Function for a Cubic Equation of State Part 2. Redlich-Kwong equation. Fluid Phase Equilibria 105 (1995) 61-69, http://dx.doi.org/10.1016/0378-3812(94)02602-w

  709. Twu, C.H., Coon, J.E., Cunningham, J.R.; A New Generalized Alpha Function for a Cubic Equation of State Part 1. Peng-Robinson equation. Fluid Phase Equilibria 105 (1995) 49-59, http://dx.doi.org/10.1016/0378-3812(94)02601-v

  710. Uttarwar, S.B., Raja Rao, M.; Augmentation of Laminar Flow Heat Transfer in Tubes by Means of Wire Coil Inserts. J. Heat Transfer 107(4) (1985) 930-935, http://dx.doi.org/10.1115/1.3247523

  711. Valderrama, J.O.; A Generalized Patel-Teja Equation of Stte for Polar and Nonpolar Fluids and their Mixtures. J. Chem. Eng. Jap. 23(1) (1990) 87-91, http://dx.doi.org/10.1252/jcej.23.87

  712. Valderrama, J.O., Cisternas, L.A.; A Cubic Equation of State for Polar and Other Complex Mixtures. Fluid Phase Equilibria 29 (1986) 431-438, http://dx.doi.org/10.1016/0378-3812(86)85041-5

  713. Valderrama, J.O., De la Puente, H., Ibrahim, A.A.; Generalization of a Polar-Fluid Soave-Redlich-Kwong Equation of State. Fluid Phase Equilibria 93 (1994) 377-383, http://dx.doi.org/10.1016/0378-3812(94)87021-7

  714. Valderrama, J.O., Álvarez, V.H.; A New Group Contribution Method Based on Equation of State Parameters to Evaluate the Critical Properties of Simple and Complex Molecules. Can. J. Chem. Eng. 84(4) (2006) 431-446, http://dx.doi.org/10.1002/cjce.5450840404

  715. van der Waals, J.D.; Over de Continuiteit van den Gas- En Vloestoftoestand. Dissertation, Leiden University, Leiden, Niederlande, 1873

  716. Van Dyke, M.; Extended Stokes series: laminar flow through a loosely coiled pipe. J. Fluid Mech. 86(1) 129-145, http://dx.doi.org/10.1017/S0022112078001032

  717. Van Nes, K., Van Western, H.A.; Aspects of the Constitution of Mineral Oils. Elsevier, New York, 1951

  718. van Swaaij, W.P.M., Buurman, C., van Breugel, J.W.; Shear Stresses on the Wall of a Dense Gas-Solids Riser. Chem. Eng. Sci. 25(11) (1970) 1818-1820, http://dx.doi.org/10.1016/0009-2509(70)80072-0

  719. Vargaftik, N.B., Vinogradov, Y.K., Yargin, V.S.; Handbook of Physical Properties of Liquids and Gases. Begell House, New York, 1996

  720. Vasserman A.A., Fominsky D.V.; Equations of State for the Ozone-Safe Refrigerants R32 and R125. Int. J. Thermophysics 22(4) (2001) 1089-1098, http://dx.doi.org/10.1023/a_1010699806169

  721. Vassiliou, C.-M., Assael, M.J., Huber, M.L., Perkins, R.A.; Reference Correlation of the Thermal Conductivity of Cyclopentane, iso-pentane, and n-Pentane. J. Phys. Chem. Ref. Data 44(3) (2015) 033102, http://dx.doi.org/10.1063/1.4927095

  722. Vatankhah, A.R., Kouchakzadeh, S; Full-range pipe-flow equations. Journal of Hydraulic Research 46(4) (2008) 559

  723. VDI-Gesellschaft; VDI Heat Atlas 2nd Edition. Berlin, New York. Springer 2010.

  724. Velliadou, D., Antoniadis, K.D., Assael, M.J., Huber, M.L.; Reference Correlation for the Viscosity of Propane-1,2-diol (Propylene Glycol) from the Triple Point to 452 K and up to 245 MPa. Int. J. Thermophys. 43(3) (2022) 42, http://dx.doi.org/10.1007/s10765-021-02970-2

  725. Velliadou, D., Antoniadis, K.D., Assael, M.J., Huber, M.L.; Reference Correlation for the Viscosity of Difluoromethane (R-32) from the Triple Point to 425 K and up to 70 MPa. Int. J. Thermophys. 43(8) (2022) 129, http://dx.doi.org/10.1007/s10765-022-03050-9

  726. Velliadou, D., Assael, M.J., Antoniadis, K.D., Huber, M.L.; Reference Correlations for the Thermal Conductivity of Xenon from the Triple Point to 606 K and Pressures up to 400 MPa. Int. J. Thermophysics 42(4) (2021) 51, http://dx.doi.org/10.1007/s10765-021-02803-2

  727. Velliadou, D., Assael, M.J., Huber, M.L.; Reference Correlation for the Viscosity of 1,1,1,2-Tetrafluoroethane (R-134a) from the Triple Point to 438 K and up to 70 MPa. Int. J. Thermophys. 43(7) (2022) 105, http://dx.doi.org/10.1007/s10765-022-03029-6

  728. Velliadou, D., Tasidou, K.A., Antoniadis, K.D., Assael, M.J., Perkins, R.A., Huber, M.L.,; Reference Correlation for the Viscosity of Xenon from the Triple Point to 750 K and up to 86 MPa. Int. J. Thermophysics 42(5) (2021) 74, http://dx.doi.org/10.1007/s10765-021-02818-9

  729. Vesovic, V., Wakeham, W.A., Olchowy, G.A., Sengers, J.V., Watson, J.T.R., Millat, J.; The Transport Properties of Carbon Dioxide. J. Phys. Chem. Ref. Data 19(3) (1990) 763-808, http://dx.doi.org/10.1063/1.555875

  730. Vicente, P.G., García, A., Viedma, A.; Experimental investigation on heat transfer and frictional characteristics of spirally corrugated tubes in turbulent flow at different Prandtl numbers. Int. J. Heat Mass Transfer 47(4) (2004) 671-681, http://dx.doi.org/10.1016/j.ijheatmasstransfer.2003.08.005

  731. Vicente, P.G., García, A., Viedma, A.; Mixed convection heat transfer and isothermal pressure drop in corruageted tubes for laminar and transition flow. Int. Comm. Heat Mass Transfer 31(5) (2004) 651-662, http://dx.doi.org/10.1016/S0735-1933(04)00052-1

  732. Vitu, S., Jaubert, J.-N., Mutelet, F.; Extension of the PPR78 model (predictive 1978, Peng-Robinson EOS with temperature dependent kij calculated through a group contribution method) to systems containing naphtenic compounds. Fluid Phase Equilibria 243 (2006) 9-28, http://dx.doi.org/10.1016/j.fluid.2006.02.004

  733. Vogel, E., Herrmann, S.; New Formulation for the Viscosity of Propane. J. Phys. Chem. Ref. Data 45(4) (2016) 043103, http://dx.doi.org/10.1063/1.4966928

  734. Vogel, E., Küchenmeister, C., Bich, E.; Viscosity correlation for n-Butane in the Fluid Region. High Temp. - High Pressures 31(2) (1999) 173-186, http://dx.doi.org/10.1068/htrt154

  735. Vogel, E., Küchenmeister, C., Bich, E.; Viscosity Correlation for Isobutane over Wide Ranges of the Fluid Region. Int. J. Thermophys 21(2) (2000) 343-356, http://dx.doi.org/10.1023/A:1006623310780

  736. Vogel, E., Küchenmeister, C., Bich, E., Laesecke, A.; Reference Correlation of the Viscosity of Propane. J. Phys. Chem. Ref. Data 27(5) (1998) 947-970, http://dx.doi.org/10.1063/1.556025

  737. Vogel, E., Span, R., Herrmann, S.; Reference Correlation for the Viscosity of Ethane. J. Phys. Chem. Ref. Data 44(4) (2015) 043101, http://dx.doi.org/10.1063/1.4930838

  738. Vogel, E., Wilhelm, J., Küchenmeister, C., Jaesche, M.; High-precision viscosity measurements on methane. High Temperatures-High Pressures 32(1) (2000) 73-81, http://dx.doi.org/10.1068/htwu359

  739. Wagner, W.; New Vapour Pressure Measurements for Argon and Nitrogen and a New Method for Establishing Rational Vapour Pressure Equations. Cryogenics 13, 8 (1973) 470-82, http://dx.doi.org/10.1016/0011-2275(73)90003-9

  740. Wagner, W., Cooper, J.R., Dittmann, A., Kijima, J., Kretzschmar, H.-J., Kruse, A., Mareš, R., Oguchi, K., Sato, H., Stöcker, I., Šifner, O., Takaishi, Y., Tanishita, I., Trübenbach, J., Willkommen, T.; The IAPWS Industrial Formulation 1997 for the Thermodynamic Properties of Water and Steam. J. Eng. Gas Turbines & Power 122 (2000) 150-182, http://dx.doi.org/10.1115/1.483186

  741. Wagner, W., Marx, V., Pruß, A.; A New Equation of State for Chlorodifluoromethane (R22) Covering the Entire Fluid Region from 116 K to 550 K at Pressures up to 200 MPa. Int. J. Refrig., 16(6):373-389, 1993., http://dx.doi.org/10.1016/0140-7007(93)90055-D

  742. Wagner, W., Pruß, A.; The IAPWS Formulation 1995 for the ThermodynamicProperties of Ordinary Water Substance forGeneral and Scientific Use. J. Phys. Chem. Ref. Data 31, 387 (2002), http://dx.doi.org/10.1063/1.1461829

  743. Walas, S.M.; Phase Equilibria in Chemical Engineering. Butterworth, 1985

  744. Walas, S.M.; Phase Equiibria in Chemical Engineering. Butterworth-Heinemann, 1985, http://dx.doi.org/10.1016/C2013-0-04304-6

  745. Watansiri, S., Owens, V.H., Starling, K.E.; Correlations for estimating critical constants, acentricfactor, and dipole moment for undefined coal-fluidfractions. Ind. Eng. Chem. Process. Des. Dev. 24(2) (1985) 294-296, http://dx.doi.org/10.1021/i200029a013

  746. Wen, C., Meng, X., Huber, M.L., Wu, J.; Measurement and Correlation of the Viscosity of 1,1,1,2,2,4,5,5,5-Nanofluoro-4-(trifluromethyl)-3-pentanone. J. Chem. Eng. Data 62(10) (2017) 3603-3609, http://dx.doi.org/10.1021/acs.jced.7b00572

  747. Wen, X., Quiang, Y.; A New Group Contribution Method for Estimating Critical Properties of Orgnic Compounds. Ind. Eng. Chem. Res. 40(26) (2001) 6245-6250., http://dx.doi.org/10.1021/ie010374g

  748. White, C.M.; Streamline Flow through Curved Pipes. Proc. R .Soc. London A 123 (1929) 645-663, http://dx.doi.org/10.1098/rspa.1929.0089

  749. Wilke, C.R.; A Viscosity Equation for Gas Mixtures. J. Chem. Phys. 18(4) (1950) 517-519, http://dx.doi.org/10.1063/1.1747673

  750. Willman, B., Teja, A.; Prediction of dew points of semicontinuous natural gas andpetroleum mixtures. 1. Characterization by use of aneffective carbon number and ideal solution predictions. Ind. Eng. Chem. Res. 26(5) (1987) 948-952, http://dx.doi.org/10.1021/ie00065a017

  751. Wilson, G.M. Jasperson, L.V.; Critical constants Tc and Pc, estimation based on zero, first and second order methods. Paper given at AIChE Spring National Meeting, New Orleans, LA, USA, February 25-29, 1996.

  752. Wisotzki, K.D., Wǘrflinger, A.; PVT Data for Liquid and Solid Cyclohexane, Cyclohexanone and Cyclopentanol up to 3000 bar. J. Phis. Chem. Solids 43(1) (1982) 13-20, http://dx.doi.org/10.1016/0022-3697(82)90167-6

  753. Wood D.J.; An explicit friction factor relationship. Civil Eng. ASCE 60, 1966

  754. Wu, J., Zhou, Y.; An Equation of State for Fluoroethane (R161). Int. J. Thermophys. 33(2) (2012) 220-234, http://dx.doi.org/10.1007/s10765-011-1151-3

  755. Wu, J., Zhou, Y., Lemmon, E.W.; An Equation of State for the Thermodynamic Properties of Dimethyl Ether. J. Phys. Chem. Ref. Data 40(2) (2011) 023104, http://dx.doi.org/10.1063/1.3582533

  756. Wu, Z., Li, K., Zhang, K., Tian, W.; Single-phase flow heat transfer characteristics in helical coils with large coil diameters. Appl. Thermal Eng. 266 (2025) 125776, http://dx.doi.org/10.1016/j.applthermaleng.2025.125776

  757. Xiang, H.W., Laesecke, A., Huber, M.L.; A New Reference Correlation for the Viscosity of Methanol. J. Phys. Chem. Ref. Data 35(4) (2006) 1597, http://dx.doi.org/10.1063/1.2360605

  758. Xin, R.C., Ebadian, M.A. ; The Effects of Prandtl Numbers on Local and Average Convective Heat Transfer Characteristics in Helical Pipes. J. Heat Transfer 119(3) (1997) 467-73, http://dx.doi.org/10.1115/1.2824120

  759. Yakut, K., Sahin, B.; The effects of vortex characteristics on performance of coiled wire turbulators used for heat transfer augmentation. Applied Thermal Eng. 24(16) (2004) 2427-2438, http://dx.doi.org/10.1016/j.applthermaleng.2004.03.008

  760. Yamada, T., Gunn. R.; Saturated Liquid Molar Volumes: The Rackett Equation. Journal of Chemical Engineering Data 18(2) (1973): 234–236, http://dx.doi.org/10.1021/je60057a006

  761. Yanase, S., Goto, N., Yamamoto, K.; Dual solutions of the flow through a curved tube. Fluid Dyn. Research 5 (1989) 191-201, http://dx.doi.org/10.1016/0169-5983(89)90021-x

  762. Yang, W.-C.; A Correlation for Solid Friction Factor in Vertical Pneumatic Conveying Lines. AIChE J. 24(3) (1978) 548-552, http://dx.doi.org/10.1002/aic.690240326

  763. Yang, W.-C.; Correlations for Solid Friction Factors in Vertical and Horizontal Pneumatic Conveying. AIChE J. 20(3) (1974) 605-607, http://dx.doi.org/10.1002/aic.690200327

  764. Yen, L.C., Woods, S.S.; A Generalized Equation for Computer Calculation of Liquid Densities. AIChE Journal 12(1) (1966) 95-99, http://dx.doi.org/10.1002/aic.690120119

  765. Yildiz, C., Biçer, Y., Pehlivan, D.; Heat Transfer and Pressure Drop in a Heat Exchanger with a Helical Pipe Containing Inside Springs. Energy Convers. Management 38(6) (1997) 619-624, http://dx.doi.org/10.1016/S0196-8904(96)00040-4

  766. Yoon, P., Thodos, G.; Viscosity of Nonpolar Gaseous Mixtures at Normal Pressures. AIChE Journal 16(2) (1970) 300-304, http://dx.doi.org/10.1002/aic.690160225

  767. Yorizane, M., Yoshiumra, S., Masuoka, H., Yoshida, H.; Thermal Conductivities of Binary Gas Mixtures at High Pressures: N2-O2, N2-Ar, CO2-Ar, CO2-CH4. Ind. Eng. Chem. Fundam. 22(4) (1983) 458-462, http://dx.doi.org/10.1021/i100012a018

  768. Younglove, B.A.; Thermophysical Properties of Fluids. I. Argon, Ethylene, Parahydrogen, Nitrogen, Nitrogen Trifluoride, and Oxygen. J. Phys. Chem. Ref. Data, 11(Suppl. 1) (1982)

  769. Younglove, B.A., Ely, J.F.; Thermophysical Properties of Fluids. II. Methane, Ethane, Propane, Isobutane, and Normal Butane. J. Phys. Chem. Ref. Data 16(4) (1987) 577-798, http://dx.doi.org/10.1063/1.555785

  770. Younglove, B.A., Hanley, H.J.M.; The Viscosity and Thermal Conductivity Coefficients of Gaseous and Liquid Argon. J. Phys. Chem. Ref. Data 15(4) (1986) 1323-1337, http://dx.doi.org/10.1063/1.555765

  771. Younglove, B.A., McLinden, M.O.; An International Standard Equation of State for the Thermodynamic Properties of Refrigerant 123 (2,2-Dichloro-1,1,1-trifluoroethane). J. Phys. Chem. Ref. Data, 23(5) (1994) 731-779, http://dx.doi.org/10.1063/1.555950

  772. Yu, J.-M., Lu, B.C.-Y.; A Three-Parameter Cubic Equation of State for Asymmetric Mixture Density Calculations. Fluid Phase Equilibria 34 (1987) 1-19, http://dx.doi.org/10.1016/0378-3812(87)85047-1

  773. Yung, S.-C., Barbarika, H.F., Calvert, S.; Pressure Loss in Venturi Scrubbers. J. Air Pollution Control Assoc., 27(4) (1977) 348-351, http://dx.doi.org/10.1080/00022470.1977.10470432

  774. Zaboloy, M.S., Vera, J.H.; Cubic Equation of State for Pure Compound Vapor Pressure from the Triple Point to the Critical Point. Ind. Eng. Chem. Res. 35(3) (1996) 829-836, http://dx.doi.org/10.1021/ie950306s

  775. Zhou, Y., Lemmon, E.W.; Equation of State for the Thermodynamic Properties of 1,1,2,2,3-Pentafluoropropane (R-245ca). Int. J. Thermophys., 37(3) (2016) 27, http://dx.doi.org/10.1007/s10765-016-2039-z

  776. Zhou, Y., Lemmon, E.W.; Preliminary equation, 2010..

  777. Zhou, Y., Lemmon, E.W., Mahmoud, A.M.; Equations of state for RE245cb2, RE347mcc, RE245fa2 and R1216. Preliminary equation

  778. Zhou, Y., Lemmon, E.W., Wu, J.; Thermodynamic Properties of o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene. J. Phys. Chem. Ref. Data 41, 023103 (2012)., http://dx.doi.org/10.1063/1.3703506

  779. Zhou, Y., Liu, J., Penoncello, S.G., Lemmon, E.W.; An Equation of State for the Thermodynamic Properties of Cyclohexane. J. Phys. Chem. Ref. Data 43 (2014) 043105, http://dx.doi.org/10.1063/1.4900538

  780. Zhou, Y., Wu, J., Lemmon, E.W.; Thermodynamic Properties of Dimethyl Carbonate. J. Phys. Chem. Ref. Data, Vol. 40, No. 4 2011, http://dx.doi.org/10.1063/1.3664084

  781. Zigrang, D.J., Sylvester, N.D.; Explicit approximations to the solution of Colebrook’sfriction factor equation. AIChE J. 28(03) (1982) 514-515., http://dx.doi.org/10.1002/aic.690280323

  782. Zuo, Y., Stenby, E.H.; Corresponding-States and Parachor Models for the Calculation of Interfacial Tensions. Can. J. Chem. Eng. 75(6) (1997) 1130-1137, http://dx.doi.org/10.1002/cjce.5450750617