Adrian Bejan(Editor), Allan D. Kraus (Editor). Heat transfer Handbok (776115), страница 8

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— John Wiley & Sons / Page 63 / 2nd Proofs / Heat Transfer Handbook / Bejans (liq.)s (vap.)cv (liq.)cv (vap.)cp (liq.)cp (vap.)w (liq.)w (vap.)η (liq.)η (vap.)λ (liq.)λ (vap.)σ−1.43994.41651.60120.90802.33181.18401938.3189.89877.993.3157248.153.45620.0300−1.01153.67951.53450.91682.34531.18751795.5207.39488.153.8961230.304.65350.0267−0.65163.21491.46470.89952.32841.16181647.8223.45320.914.4956210.905.95840.0233−0.33982.90671.42820.92172.34971.18881498.5236.89231.745.1100191.087.41100.0200−0.06032.69201.41841.00652.40821.30171347.7246.81176.395.7388171.519.06630.01680.19742.53571.42811.12802.50191.47911194.8252.96138.236.3908152.5610.9970.01360.44032.41651.45361.26332.63771.70901039.0254.94109.907.0891134.4713.3050.01050.67452.31901.49411.40472.83982.0151878.23252.0387.6507.8826117.3716.1790.00760.90662.22941.55131.55603.18052.4986708.85243.2769.2738.8799101.1820.0600.00481.14812.12791.63561.73653.97113.6068520.93227.1652.96210.38185.53426.4180.00231.44781.94511.87812.05079.983212.744276.76200.4734.91814.02371.37146.9290.0003225.000.0769588.401.871186.460518.590.54652.46701.44231.20402.21961.42441187.5216.87250.000.2179558.784.9424143.65548.270.78632.40481.50651.33132.35151.59081027.5221.28275.000.5020526.1710.941204.67576.711.01682.36971.58391.47362.52331.8048868.89220.90300.000.9980489.1421.658270.61602.561.24282.34931.67381.62812.75722.0984710.10214.52325.001.7832444.8940.480343.27623.161.46992.33111.77941.79753.13712.5937544.17200.36350.002.9510384.0277.052427.71630.911.71162.29211.92482.00044.20914.0530350.19175.23continuedPropane (R-290)Tpρ (liq.)ρ (vap.)h (liq.)h (vap.)s (liq.)s (vap.)cv (liq.)cv (vap.)cp (liq.)cp (vap.)w (liq.)w (vap.)100.002.5 × 10−8718.540.0000−168.39379.56−1.09204.38761.34360.74801.93100.93652026.4153.65125.007.5 × 10−6693.010.0003−119.73404.10−0.65773.53291.33390.83661.96131.02521857.6169.94150.000.00028667.730.0100−70.291430.71−0.29733.04271.33910.91841.99561.10751684.4184.59175.000.0034642.230.1026−19.808459.040.01382.75011.35821.00162.04611.19331515.0197.65200.000.0201615.980.540432.227488.580.29152.57331.39261.09462.11941.29501349.7208.6863[63], (21)Lines: 672 to 707———* 528.0pt PgVar———Normal Page* PgEnds: PageBreak[63], (21)12345678910111213141516171819202122232425262728293031323334353637383940414243444564BOOKCOMP, Inc.

— John Wiley & Sons / Page 64 / 2nd Proofs / Heat Transfer Handbook / BejanTABLE 2.7Thermophysical Properties of Fluids along the Saturation Linea (Continued)Propane (R-290) (Continued)η (liq.)η (vap.)λ (liq.)λ (vap.)σ3821.52.9792203.492.41710.03541269.73.5913192.173.78870.0315655.974.2258178.465.34180.0277415.284.8708163.557.07220.0239289.685.5148148.258.97110.0203212.586.1540133.1311.0400.0167160.606.8026118.6213.3230.0132123.317.5026105.0815.9570.009995.0858.340592.75519.2480.006872.3519.508381.72023.9150.003951.63211.63471.50232.6360.0014325.000.5206539.7612.847326.94685.131.42232.44141.81611.75082.60822.0227752.87199.83123.098.124594.18019.6040.0088350.000.9447504.7723.402394.69692.201.62062.47071.91471.89552.81942.2764620.83192.5497.3008.961385.38623.0610.0061375.001.5821463.2740.982468.29722.981.82002.49922.02152.04853.13512.6684483.83178.6175.69710.11077.58127.6640.0037400.002.4950408.1472.839551.10745.402.02822.51402.14822.21783.85923.6114328.58154.9755.86312.01670.52634.9930.0015425.003.7828256.91201.07680.26709.192.33072.39882.45432.4822211.56242.27119.17113.8427.11021.260118.63123.390.0000Butane (R-600)Tpρ (liq.)ρ (vap.)h (liq.)h (vap.)s (liq.)s (vap.)cv (liq.)cv (vap.)cp (liq.)cp (vap.)w (liq.)w (vap.)η (liq.)η (vap.)λ (liq.)λ (vap.)σ150.008.8 × 10−6720.910.0004−58.828422.68−0.25012.96001.42901.01491.98241.15801719.0156.471370.63.7090171.215.57930.0313200.000.0020673.730.068741.883484.260.32892.54071.47181.17482.05371.31981430.6178.85494.944.9792149.198.49730.0243225.000.0106649.750.333693.960517.460.57412.45631.51351.26502.11551.41471290.7188.13349.265.5998137.4210.2500.0210250.000.0393624.931.1234147.89551.890.80112.41711.57091.36812.20041.52821153.3195.52259.206.2086125.7712.1970.0177275.000.1109598.782.9507204.27587.151.10552.40781.64221.48492.30921.66441018.2200.40198.786.8131114.5314.3570.0146300.000.2580570.676.5301263.73622.771.22152.41831.72481.61332.44351.8266884.92202.11155.627.4364103.9416.7850.0116[64], (22)Lines: 707 to 742———* 528.0pt PgVar———Normal Page* PgEnds: PageBreak[64], (22)123456789101112131415161718192021222324252627282930313233343536373839404142434445BOOKCOMP, Inc.

— John Wiley & Sons / Page 65 / 2nd Proofs / Heat Transfer Handbook / BejanIsobutane (2-Methylpropane, R-600a)Tpρ (liq.)ρ (vap.)h (liq.)h (vap.)s (liq.)s (vap.)cv (liq.)cv (vap.)cp (liq.)cp (vap.)w (liq.)w (vap.)η (liq.)η (vap.)λ (liq.)λ (vap.)σ150.000.000023706.140.0011−49.648404.10−0.19982.82521.31030.89431.81041.03741612.0157.761751.43.7993148.494.46060.0285175.000.00045682.480.0179−3.4665431.220.08482.56881.35240.99471.88501.13831470.8169.14903.054.4453139.486.16660.0253200.000.0038658.250.131844.680460.560.34192.42121.40191.09591.96841.24191332.1179.38551.155.0797129.368.02760.0221225.000.0185633.090.580795.083491.720.57912.34191.46201.20402.06521.35641195.1188.05369.875.6991118.7510.0320.0189250.000.0631606.611.8175148.13524.220.80232.30661.53361.32302.17811.48941059.3194.51262.916.3047108.1112.1740.0158275.000.1672578.294.5187204.27557.511.01552.30001.61601.45412.30951.6466924.64198.00194.156.909597.86214.4770.0128300.000.3698547.489.6081264.00591.001.22202.31211.70771.59542.46231.8340791.59197.70147.227.545788.32317.0260.0099325.000.7162513.3118.417327.86623.831.42432.33501.80731.74462.64462.0676660.70192.61113.538.277379.77620.0300.0071350.001.2577474.2433.238396.67654.411.62502.36141.91441.90212.89112.4005528.31181.3287.8889.241372.40223.9540.0045375.002.0551425.5759.391472.64679.121.82962.38022.03562.07493.38223.0674378.18161.4266.26410.81566.12630.1100.0022400.003.1920340.74119.80566.69683.392.06432.35612.23882.30416.54007.3172183.42128.3442.43614.85762.04846.2640.0003325.000.1685593.354.803838.051382.47350.000.3396565.699.3842101.10422.37375.000.6177535.0216.939168.03462.26400.001.0384499.7329.117239.58500.99425.001.6429456.4749.281317.05536.24450.002.4836395.8587.430404.03561.62continuedPentaneTpρ (liq.)ρ (vap.)h (liq.)h (vap.)150.002.7 × 10−7756.280.0000−334.92139.41200.000.0002711.190.0086−235.81199.97250.000.0076666.320.2651−132.70268.35275.000.0266643.130.8533−78.400305.08300.000.0732618.952.1937−21.633343.2265[65], (23)Lines: 742 to 776———* 528.0pt PgVar———Normal Page* PgEnds: PageBreak[65], (23)12345678910111213141516171819202122232425262728293031323334353637383940414243444566BOOKCOMP, Inc.

— John Wiley & Sons / Page 66 / 2nd Proofs / Heat Transfer Handbook / BejanTABLE 2.7Thermophysical Properties of Fluids along the Saturation Linea (Continued)Pentane (Continued)s (liq.)s (vap.)cv (liq.)cv (vap.)cp (liq.)cp (vap.)w (liq.)w (vap.)η (liq.)η (vap.)λ (liq.)λ (vap.)σ−1.50461.65761.44261.00611.96821.12141788.3138.802750.83.4236172.924.33380.0323−0.93461.24431.48691.18172.00911.29721500.5159.00689.404.5515152.506.96150.0265−0.47491.12921.58621.35972.12831.47931244.1175.83344.145.7318130.6810.2070.0208−0.26811.12641.65721.46292.21711.58891122.1182.32267.516.3409120.3712.1640.0180−0.07091.14531.73971.57632.32391.71411002.5186.93214.426.9672110.6414.3930.01530.11971.17941.83101.69832.44801.8562884.21189.09174.847.6198101.5416.9280.01260.30561.22351.92841.82722.59162.0189765.87188.17143.568.315893.03319.8110.01000.48891.27352.03031.96192.76202.2132645.89183.35117.619.088385.07323.0990.00750.67141.32492.13632.10292.98082.4707522.16173.4895.07010.00477.56026.8970.00510.85611.37192.24882.25433.31772.9032391.45156.7774.43611.22270.31131.4310.00301.05031.40052.38212.43284.17824.2191246.17130.1453.84213.31262.80937.3670.0011380.000.8347518.6323.563199.99466.500.58401.28532.05302.00172.80942.3018400.001.2377487.6736.004257.89496.360.73041.32652.14122.11883.01492.5477420.001.7700450.3554.920320.05523.380.87921.36332.23482.24393.32652.9552440.002.4600400.6386.923388.70543.591.03501.38702.34402.38834.02524.0178460.003.3570287.45190.32482.73525.561.23781.33092.56652.625242.07069.567Isopentane (2-Methylbutane)Tpρ (liq.)ρ (vap.)h (liq.)h (vap.)s (liq.)s (vap.)cv (liq.)cv (vap.)cp (liq.)cp (vap.)260.000.0189652.360.6394−89.675283.21−0.31951.11471.56511.35722.09021.4807280.000.0461633.241.4647−46.927312.03−0.16131.12071.64091.45952.18341.5904300.000.0980613.332.9606−2.2196341.94−0.00741.13981.71961.56392.28431.7064320.000.1872592.355.441744.614372.680.14321.16851.80061.67022.39391.8305340.000.3284569.959.307293.760403.970.29141.20381.88321.77852.51421.9659360.000.5382545.6315.089145.45435.420.43801.24351.96731.88872.64952.1186[66], (24)Lines: 776 to 812———* 528.0pt PgVar———Normal Page* PgEnds: PageBreak[66], (24)123456789101112131415161718192021222324252627282930313233343536373839404142434445BOOKCOMP, Inc.

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