Adrian Bejan(Editor), Allan D. Kraus (Editor). Heat transfer Handbok (776115), страница 6
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(1986)Span et al. (2000)Younglove (1982)Schmidt and Wagner (1985)Younglove (1982)ECS (fitted)ECS (fitted)Lemmon and Span (2001)Angus et al. (1980)Polt et al. (1992)Polt (1987)de Reuck et al. (1991)Lemmon and Span (2001)Wagner and Pruss (2002)Lemmon and Span (2001)Jacobsen et al. (1992)Marx et al. (1992)Platzer et al. (1990)ECS (fitted)Kozlov (1996)Marx et al.
(1992)NIST14, Version 9.08ECS (fitted)Not currently availableECS (fitted)Lemmon and Jacobsen (2001)Not currently availableLemmon and Jacobsen (2001)McCarty and Weber (1972)Not currently availableNot currently availableNot currently availableNot currently availableNot currently availableNot currently availableNot currently availableNot currently availableIAPWS (1998)McCarty (1989)ECS (fitted)ECS (fitted)ECS (fitted)ECS (fitted)ECS (predictive)ECS (fitted)Viscosity EquationNIST14, Version 9.08ECS (fitted)Not currently availableECS (fitted)Lemmon and Jacobsen (2001)Not currently availableLemmon and Jacobsen (2001)McCarty and Weber (1972)Not currently availableNot currently availableNot currently availableNot currently availableNot currently availableNot currently availableNot currently availableNot currently availableIAPWS (1997)McCarty (1989)ECS (fitted)ECS (fitted)ECS (fitted)ECS (fitted)ECS (predictive)ECS (fitted)Temp.Range (K)(EOS)Max.Pressure(MPa)187.7–760115.77–800175.61–62024.562–70063.151–200085–50054.361–100013.8–400189–500200–500113–500100–600273–474273–523222.38–525179–750273.16–1275161.36–800162.68–625236.93–525273.15–507173.76–500176–423116.099–52517030080070022005082121303030200323255100100030030200216050200[50], (8)Lines: 231 to 268———* 528.0pt PgVar———Normal Page* PgEnds: PageBreak[50], (8)123456789101112131415161718192021222324252627282930313233343536373839404142434445BOOKCOMP, Inc.
— John Wiley & Sons / Page 51 / 2nd Proofs / Heat Transfer Handbook / BejanR-123R-124R-125R-13R-134aR-14R-141bR-142bR-143aR-152aR-22R-227eaR-23R-236eaR-236faR-245caR-245faR-32R-41RC318Younglove and McLinden (1994)de Vries et al. (1995)Sunaga et al. (1998)Magee et al. (2000)Tillner-Roth and Baehr (1994)Platzer et al. (1990)Lemmon and Span (2001)Lemmon and Span (2001)Lemmon and Jacobsen (2000)Outcalt and McLinden (1996)Kamei et al.
(1995)ECS (fitted)Penoncello et al. (2003)ECS (fitted)Outcalt and McLinden (1995)ECS (fitted)ECS (fitted)Tillner-Roth and Yokozeki (1997)Outcalt (1996)Platzer et al. (1990)Laesecke et al. (1996)ECS (predictive)ECS (fitted)ECS (fitted)Perkins et al. (2000)ECS (predictive)ECS (predictive)ECS (fitted)ECS (fitted)Krauss et al. (1996)ECS (fitted)ECS (fitted)Shan et al.
(2000)ECS (predictive)ECS (predictive)ECS (fitted)ECS (fitted)ECS (fitted)ECS (predictive)ECS (predictive)Tanaka and Sotani (1995)ECS (predictive)ECS (fitted)ECS (fitted)Laesecke (2000)ECS (predictive)ECS (predictive)ECS (fitted)ECS (fitted)Krauss et al. (1996)ECS (fitted)ECS (fitted)Shan et al. (2000)ECS (predictive)ECS (predictive)ECS (fitted)ECS (fitted)ECS (fitted)ESC (predictive)ECS (predictive)a166–600120–470172.52–50092–403169.85–45598.94–623169.85–500142.72–500161.34–650154.56–500115.73–550200–500118.20–475242–500179.52–500200–500200–500136.340–435175–500233.35–6234040603570511006010060606012060406060706060The equations of state for the fluids in bold type can be considered primary standards, and those for the italicized fluids are high-accuracy equations.
See the text foradditional details.51[51], (9)Lines: 268 to 297———* 528.0pt PgVar———Normal Page* PgEnds: PageBreak[51], (9)12345678910111213141516171819202122232425262728293031323334353637383940414243444552BOOKCOMP, Inc. — John Wiley & Sons / Page 52 / 2nd Proofs / Heat Transfer Handbook / BejanTABLE 2.3Physical Constants and Fixed PointsMethaneEthanePropaneButaneIsobutanePentaneIsopentaneNeopentaneHexaneHeptaneOctaneAmmoniaArgonBenzeneCarbon dioxideCarbon monoxideCyclohexaneCyclopropaneDeuteriumEthyleneFluorineHeavy waterHeliumHydrogenHydrogen sulfideMolecularWeight(g/mol)CriticalTemperature(K)CriticalPressure(MPa)CriticalDensity(kg/m3)TriplePoint (K)NormalBoilingPoint (K)AcentricFactor16.04330.07044.09658.12258.12272.14972.14972.15186.175100.20114.2317.03039.94878.10844.01028.01184.16142.0814.028228.05437.99720.0274.00262.015934.082190.56305.33369.82425.13407.82469.70460.35433.75507.82540.13569.32405.40150.69562.05304.13132.80553.64398.3038.340282.35144.41643.895.195333.190373.604.59924.87184.24713.79603.64003.37003.39573.19633.03402.73602.497011.3334.86304.89407.37733.49354.07505.57971.66535.04185.172421.6710.22751.31509.1100162.66206.58218.50227.84224.36232.00236.00232.00233.18232.00234.90225.00535.60309.00467.60303.92273.00258.5069.797214.24592.86358.0069.64130.118337.4190.69490.35285.480134.87113.56143.47112.65256.60177.83182.55216.37195.5083.806278.70216.5967.127279.47145.7018.710103.9953.481276.972.176813.957187.70111.67184.55231.06272.59261.48309.21300.97282.63341.86371.53398.77239.8287.302353.23—81.648353.89241.6723.309169.3885.037374.564.230420.277212.860.01140.09930.15240.20000.18500.25100.22960.19600.29700.34800.39300.2560−0.00220.20920.22390.05100.20930.1305−0.17500.08660.04490.3640−0.3820−0.21400.0960DipoleMoment(D)000.0830.020.1320.370.1000.051.47000.100.300001.90000.90[52], (10)Lines: 297 to 335———* 528.0pt PgVar———Normal Page* PgEnds: PageBreak[52], (10)123456789101112131415161718192021222324252627282930313233343536373839404142434445BOOKCOMP, Inc.
— John Wiley & Sons / Page 53 / 2nd Proofs / Heat Transfer Handbook / Bejan53KryptonMethanolNeonNitrogenNitrogen trifluorideOxygenParahydrogenPerfluorobutanePerfluoropentanePerfluoropropanePropylenePropyneSulfur dioxideSulfur hexafluorideTolueneWaterXenonR-11R-113R-114R-115R-116R-12R-123R-124R-125R-13R-134aR-14R-141b83.80432.04220.17928.01371.01931.9992.0159238.03288.03188.0242.08040.06064.066146.0692.13818.015131.30137.37187.38170.93154.47138.01120.91152.93136.47120.02104.46102.0388.010116.95209.48513.3844.492126.19234.00154.5832.938386.33420.56345.10365.57402.38430.65318.73593.88647.10289.73471.11487.21418.83353.10293.03385.12456.83395.43339.17302.00374.21227.51479.965.51008.21582.67863.39584.46075.04301.28382.32342.04502.67104.66465.62607.88003.75464.238022.0645.84004.40763.39223.25703.12003.04204.13613.66183.62433.62903.87904.05933.75004.4600908.44281.50481.91313.30562.47436.1431.360599.84609.47628.00223.39244.90525.00743.81290.24322.001099.0554.00560.00580.00613.10622.00565.00550.00560.00568.00582.88511.90625.70460.00115.77175.6124.56263.15166.36054.36113.800145.00200.00113.0087.950170.50197.70222.38179.00273.16161.36162.68236.93179.00173.76176.00116.10166.0074.000172.5292.000169.8598.940169.85119.78337.6327.10477.355144.1490.18820.277271.06302.90236.32225.46191.00256.61—383.70373.12165.03296.86320.74276.74234.21194.98243.40300.97261.19225.02191.67247.08145.10305.21−0.00170.5625−0.03870.03720.12600.0222−0.21800.37400.42300.32100.14080.20400.23000.21000.26100.34400.00360.18880.25250.25230.25200.25400.17950.28190.28810.30610.17230.32680.17850.223501.70000.20000.140.140.400.701.6000.401.85500.450.8030.6580.5200.511.3561.4691.5630.512.05802.014continued[53], (11)Lines: 335 to 372———* 528.0pt PgVar———Normal Page* PgEnds: PageBreak[53], (11)12345678910111213141516171819202122232425262728293031323334353637383940414243444554BOOKCOMP, Inc.
— John Wiley & Sons / Page 54 / 2nd Proofs / Heat Transfer Handbook / BejanTABLE 2.3R-142bR-143aR-152aR-22R-227eaR-23R-236eaR-236faR-245caR-245faR-32R-41RC318Physical Constants and Fixed Points (Continued)MolecularWeight(g/mol)CriticalTemperature(K)CriticalPressure(MPa)CriticalDensity(kg/m3)TriplePoint (K)NormalBoilingPoint (K)100.5084.04166.05186.468170.0370.014152.04152.04134.05134.0552.02434.033200.04410.26345.86386.41369.30374.88299.29412.44398.07447.57427.20351.25317.28388.384.07003.76104.51684.99002.92904.82803.50203.20003.92503.64005.78205.89702.7775446.00431.00368.00523.84584.00526.50563.00551.29523.59517.00424.00316.51620.00142.72161.34154.56115.73146.35118.02—179.52——136.34129.82233.35264.04225.91249.13232.34256.71191.13279.35271.71298.28288.05221.50195.02267.18AcentricFactor0.23370.26150.27520.22080.36320.26460.37940.37720.35360.37240.27690.20120.3553DipoleMoment(D)2.142.342.2621.4581.4561.6491.1291.9821.741.5491.9781.851[54], (12)Lines: 372 to 397———* 528.0pt PgVar———Normal Page* PgEnds: PageBreak[54], (12)123456789101112131415161718192021222324252627282930313233343536373839404142434445BOOKCOMP, Inc.
— John Wiley & Sons / Page 55 / 2nd Proofs / Heat Transfer Handbook / BejanTABLE 2.4Ideal Gas Isobaric Heat Capacity (kJ/kg · K)MethaneEthanePropaneButaneIsobutanePentaneIsopentaneNeopentaneHexaneHeptaneOctaneAmmoniaArgonBenzeneCarbon dioxideCarbon monoxideCyclohexaneCyclopropaneDeuteriumEthyleneFluorineHeavy waterHeliumHydrogenHydrogen sulfideKrypton100 K150 K200 K250 K300 K350 K400 K450 K500 K550 K2.07421.18710.9365—————————0.5203——1.0388——7.4682—0.7662—5.193111.195——2.07591.28461.10641.15791.03731.12140.9488—————0.5203——1.0390——7.30391.19990.7693—5.193112.591—0.24802.08901.40481.27141.31571.23591.29661.1782—1.28321.2739—2.00840.5203——1.0390——7.24771.26020.7812—5.193113.5300.98090.24802.13601.56171.46161.49441.44421.47031.4163—1.46071.45181.44532.03640.5203—0.79161.0388——7.24591.37680.8013—5.193114.0450.99130.24802.23011.75231.67711.70241.67131.67161.65631.68491.66251.65651.65192.09530.52031.05470.84581.03851.27301.33717.24991.53380.82471.71225.193114.3091.00590.24802.36631.96261.90501.92511.90781.89151.89271.93441.88291.87871.87532.17430.52031.25180.89511.03841.53421.58147.25261.70980.84751.74395.193114.4291.02410.24802.53122.17852.13212.14722.14112.11432.12102.16642.10622.10232.09882.26660.52031.43370.93921.03841.78521.82257.25701.88890.86811.77885.193114.4731.04510.24802.71181.39042.34962.35952.36242.32922.33802.38402.32122.31642.31212.36810.52031.60100.97861.03862.02802.04807.26672.01690.88591.81645.193114.4921.06830.24802.89892.59352.55372.55812.56812.53132.54162.58942.52222.51592.51072.47590.52031.75431.01411.03902.25912.25197.28422.22480.90121.85605.193114.5111.09310.24803.08682.78582.74342.74222.75742.71942.73082.78462.70782.69972.69342.58790.52031.89411.04631.03962.47562.43397.31082.37620.91421.89715.193114.5291.11890.2480600 K553.27202.96712.91942.91262.93132.89392.90582.97042.87862.86842.86082.70240.52032.02111.07551.04052.67592.59997.34682.51660.92531.93935.193114.5351.14540.2480continued[55], (13)Lines: 397 to 436———* 528.0pt PgVar———Normal Page* PgEnds: PageBreak[55], (13)12345678910111213141516171819202122232425262728293031323334353637383940414243444556BOOKCOMP, Inc.
— John Wiley & Sons / Page 56 / 2nd Proofs / Heat Transfer Handbook / BejanTABLE 2.4Ideal Gas Isobaric Heat Capacity (kJ/kg · K) (Continued)MethanolNeonNitrogenNitrogen trifluorideOxygenParahydrogenPerfluorobutanePerfluoropentanePerfluoropropanePropylenePropyneSulfur dioxideSulfur hexafluorideTolueneWaterXenonR-11R-113R-114R-115R-116R-12R-123R-124R-125R-13R-134a100 K150 K200 K250 K300 K350 K400 K450 K500 K550 K600 K—1.03011.03890.47930.909813.408———————————————————0.3445——1.03011.03900.52870.909816.188——0.50231.0550———————————0.4113—0.4935—0.4304—1.23841.03011.03910.60240.910216.0710.6181—0.61001.1898———0.7409—0.15830.4719——0.54580.59850.48730.53120.57770.61870.50810.64571.29231.03011.03920.68090.912615.3290.71880.72830.70541.3545——0.57790.9347—0.15830.52830.5896—0.63800.68900.55110.60690.65570.70790.57760.74481.37751.03011.03970.75410.918314.8360.80690.81760.78941.53751.51990.62290.66741.13471.86480.15830.57380.65010.69250.71560.77220.60450.67310.72840.79010.63890.83671.48731.03011.04120.81780.928014.6240.88350.89520.86271.72591.67030.65180.73971.33161.88060.15830.61060.69980.74540.78010.84450.64900.73100.79680.86580.69210.92301.61011.03011.04410.87110.940914.5730.94950.96210.92631.91161.81000.67850.79711.52061.90180.15830.64020.74130.79120.83300.90600.68600.78190.86190.93450.73711.00471.73681.03011.04900.91500.955814.5871.00591.01920.98092.09011.93980.70290.84271.69781.92720.15830.66410.77610.83080.87570.95800.71660.82670.92470.99570.77381.08281.86161.03011.05590.95140.971714.6151.05371.06761.02742.25922.06020.72520.87901.86081.95540.15830.68360.80550.86480.90981.00200.74210.86670.98621.04920.80241.15771.98141.03011.06460.98300.987614.6331.09381.10831.06672.41782.17220.74540.90822.00931.98520.15830.69960.83030.89330.93681.03910.76330.90311.04741.09570.82281.22992.09521.03011.07481.01271.003014.6381.12731.14221.09962.56582.27630.76350.93182.14392.01630.15830.71280.85130.91560.95821.07070.78100.93691.10921.13580.83501.2998[56], (14)Lines: 436 to 474———* 528.0pt PgVar———Normal Page* PgEnds: PageBreak[56], (14)123456789101112131415161718192021222324252627282930313233343536373839404142434445BOOKCOMP, Inc.
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