Adrian Bejan(Editor), Allan D. Kraus (Editor). Heat transfer Handbok, страница 10
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— John Wiley & Sons / Page 72 / 2nd Proofs / Heat Transfer Handbook / BejanTABLE 2.7Thermophysical Properties of Fluids along the Saturation Linea (Continued)Carbon Dioxide (R-744)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.)σ220.000.59911166.115.81786.728431.640.55172.11940.96980.63891.96180.9303951.21223.15242.0111.135176.1511.3010.0163230.000.89291128.723.271106.57434.600.63872.06490.95670.67001.99701.0053879.09223.57204.2311.689163.2812.2210.0139240.001.28251088.933.295126.84436.490.72352.01370.94540.70532.05101.1033806.38222.96172.9612.272150.7513.2970.0115250.001.78501046.046.644147.71437.040.80681.96410.93640.74592.13201.2366731.78221.22146.7412.902138.4714.6100.0093260.002.4188998.8964.417169.44435.920.88951.91440.93230.79432.25541.4295652.58218.19124.4013.614126.3516.3060.0071270.003.2033945.8388.374192.41432.560.97321.86260.93960.85172.45341.7307565.46213.75105.0214.469114.2518.6870.0051280.004.1607883.58121.74217.30425.941.05981.80500.96050.92322.81412.2769471.54207.7287.73115.601102.0322.4680.0033285.004.7123847.05143.92230.86420.801.10561.77200.97480.96863.13332.7668422.75203.9479.54816.36195.81025.4240.0024290.005.3177804.67171.96245.63413.751.15441.73410.99371.02603.67563.6142371.95199.4571.40917.35789.54629.8210.0017295.005.9822752.56209.72262.38403.641.20871.68761.02651.10604.79395.4316315.91193.8462.93618.79283.55837.2150.0010300.006.7131679.24268.58283.38387.081.27591.62151.11991.24768.697911.921245.67185.3353.10721.30680.59353.6890.0003110.001.0663646.6541.53364.903226.69115.001.4299612.6856.99078.078225.37120.001.8745573.4078.08092.410222.13125.002.4112525.22108.67108.66215.82130.003.0556455.45161.99129.41202.48Carbon MonoxideTpρ (liq.)ρ (vap.)h (liq.)h (vap.)70.0000.0210840.211.0232−25.074205.0880.0000.0836798.973.6494−3.5476213.8190.0000.2384754.429.637018.162220.8895.0000.3685730.3614.53029.279223.56100.000.5443704.7021.13740.692225.53105.000.7741677.0129.92052.515226.64[72], (30)Lines: 985 to 1020———* 528.0pt PgVar———Normal Page* PgEnds: PageBreak[72], (30)123456789101112131415161718192021222324252627282930313233343536373839404142434445BOOKCOMP, Inc.
— John Wiley & Sons / Page 73 / 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−0.33012.95781.27790.75402.16061.0669967.52169.27255.084.7766162.956.88410.0119−0.04361.67341.18030.77272.14481.1157872.05178.52178.905.6070145.127.98110.00980.20972.46211.10750.80562.18771.2115773.63184.85139.806.6165126.199.12670.00780.32802.37311.07800.82802.23551.2858722.64186.78125.977.2220116.489.72770.00670.44262.29091.05250.85462.30681.3860670.00187.83114.097.9187106.7610.3590.00570.55472.21301.03120.88572.41101.5243615.20187.97103.408.733397.19311.0390.00470.66582.13661.01470.92252.56511.7245557.54187.1693.3809.705687.89511.8030.00370.77782.05861.00490.96732.80452.0383495.94185.3483.64310.90378.96712.7300.00270.89331.97441.00631.02493.21682.5995428.49182.4573.84112.45370.41913.9860.00181.01801.87521.03051.10724.10753.8853351.29178.2763.50814.66161.99515.9990.00101.17301.73231.12321.25557.95669.7719253.47171.8051.25318.68552.28020.3310.0003425.000.5729641.7915.830166.10463.470.42491.12481.93161.88062.52242.0972697.60182.910.0104450.000.9133609.9425.495231.07502.440.57221.17522.01392.03812.67602.3452594.66175.580.0079475.001.3839573.7340.045300.04540.440.71961.22572.13442.20322.86292.6798487.67164.250.0056500.002.0124530.6262.573373.80576.110.86851.27312.24192.37523.12013.1989378.12148.100.0034525.002.8316475.08100.85454.16606.531.02211.31232.35982.54443.63934.2107263.49124.780.0016550.003.8928349.73198.59559.79617.681.21361.31882.56052.640311.57011.408108.3987.2290.0001continuedCyclohexane73Tpρ (liq.)ρ (vap.)h (liq.)h (vap.)s (liq.)s (vap.)cv (liq.)cv (vap.)cp (liq.)cp (vap.)w (liq.)w (vap.)σ300.000.0141772.060.4810−107.66283.43−0.32900.97471.31761.17131.82651.27321245.3177.990.0244325.000.0388748.081.2313−59.864315.78−0.17610.97971.48661.30751.98991.41481108.1182.880.0214350.000.0900723.432.6979−8.3171350.42−0.02361.00141.61651.44432.12821.5618996.64186.300.0185375.000.1833697.805.262146.568386.930.12751.03511.72791.58462.25701.7199895.44187.760.0157400.000.3373670.779.4161104.68424.830.27691.07721.83121.72972.38581.8951797.11186.800.0130[73], (31)Lines: 1020 to 1056———* 528.0pt PgVar———Normal Page* PgEnds: PageBreak[73], (31)12345678910111213141516171819202122232425262728293031323334353637383940414243444574BOOKCOMP, Inc.
— John Wiley & Sons / Page 74 / 2nd Proofs / Heat Transfer Handbook / BejanTABLE 2.7Thermophysical Properties of Fluids along the Saturation Linea (Continued)CyclopropaneTpρ (liq.)ρ (vap.)h (liq.)h (vap.)s (liq.)s (vap.)cv (liq.)cv (vap.)cp (liq.)cp (vap.)w (liq.)w (vap.)290.000.5777631.5211.361240.80655.851.14372.57491.48621.18382.32571.5298875.75239.65300.000.7615616.1814.851263.98663.681.22132.55371.41881.25132.30541.6387836.04238.29310.000.9849600.1119.140287.23671.201.29642.53501.40101.32212.34241.7615789.18236.10320.001.2529583.1724.390311.06678.301.37052.51821.41731.39612.42421.9024736.55232.99330.001.5709565.1430.814335.82684.841.44502.50271.45711.47352.54492.0682679.48228.84340.001.9441545.7538.698361.86690.641.52082.48781.51301.55462.70512.2705618.85223.51350.002.3784524.5748.459389.49695.421.59852.47261.58001.64002.91442.5304554.99216.83360.002.8796500.9360.747419.11698.721.67912.45581.65561.73053.19942.8917487.71208.55370.003.4546473.6376.696451.33699.731.76422.43551.73881.82763.63063.4598416.20198.34380.004.1114440.1698.678487.35696.751.85642.40741.83221.93414.43824.5706338.70185.70390.004.8609393.04133.76530.72684.851.96432.35951.94712.05666.98028.1541251.34169.7330.0000.4767144.338.905060.234342.682.167311.5824.90282.381432.0000.6814136.7713.07082.614339.652.842010.8744.73422.806734.0000.9432126.8319.017109.06330.703.582910.1024.59713.503436.0001.2621113.4226.539140.62319.194.40819.36864.74934.313237.0001.4389103.7530.756160.36313.414.90419.04085.13004.679038.0001.690383.19383.193195.52195.525.76965.76966.45946.4594DeuteriumTpρ (liq.)ρ (vap.)h (liq.)h (vap.)s (liq.)s (vap.)cv (liq.)cv (vap.)20.0000.0333171.960.7929−22.077303.50−0.999115.2803.51942.478222.0000.0678167.251.4776−9.5250315.14−0.411414.3464.14112.298824.0000.1232161.962.50315.3945325.690.222413.5684.67672.168226.0000.2055156.413.966822.156334.400.872112.8824.94862.116428.0000.3209150.646.016340.366340.441.518712.2364.99852.1737[74], (32)Lines: 1056 to 1090———* 528.0pt PgVar———Normal Page* PgEnds: PageBreak[74], (32)123456789101112131415161718192021222324252627282930313233343536373839404142434445BOOKCOMP, Inc.
— John Wiley & Sons / Page 75 / 2nd Proofs / Heat Transfer Handbook / Bejancp (liq.)cp (vap.)w (liq.)w (vap.)σ5.67854.15211023.8266.640.00386.79693.9417919.13280.240.00347.85373.8780858.60292.490.00308.59074.0466830.29302.870.00269.29464.5882801.77310.720.002110.3205.7989755.58315.320.001712.1828.3068683.32316.510.001315.58412.743578.05315.630.000921.48318.581437.40313.140.000540.46723.229337.51309.680.000375.41975.419243.33243.330.0000220.000.9566486.6717.452128.03519.070.65162.42901.31961.13202.70021.7382903.49261.5495.6818.0066134.4513.9430.0075240.001.7730446.1133.066184.88522.740.89112.29891.34351.25403.04302.2112724.39254.8874.9619.1616116.0717.1420.0046250.002.3295422.0244.970216.09520.391.01322.23041.36791.33443.36292.6608628.10248.8065.3989.9344106.8419.5630.0033260.003.0035393.4761.542250.40513.451.14132.15301.40681.43873.94573.5116524.13240.4755.95010.95797.24123.2190.0021270.003.8125356.3986.795290.30498.321.28362.05411.48391.59185.40865.7658404.99229.1746.02812.50686.86030.4510.0010280.004.7835290.70140.70347.75457.491.48141.87331.77841.980919.56229.260246.68208.8833.08516.17683.42271.7230.0001110.000.8891120.001.6342125.002.1389130.002.7475135.003.4739140.004.3357continuedEthylene (Ethene, R-1150)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.)σ120.000.0014634.170.0385−119.17428.29−0.83073.73141.55300.89372.42711.19201660.4217.51427.513.3390248.796.77950.0250140.000.0118608.020.2876−70.809451.32−0.45813.27141.46550.90642.40811.21251520.9233.95277.584.8414222.347.89230.0212160.000.0562580.871.2123−22.661473.00−0.13722.96071.39480.93352.40671.25981376.7247.39200.135.6998197.469.11460.0175180.000.1818552.203.588925.871492.310.14732.73861.34640.97832.44131.34671227.0256.98153.026.4011174.6010.3600.0140200.000.4555521.228.493675.686508.130.40702.56921.32141.04312.52861.49201069.9261.94120.527.1332153.7311.8620.0106Fluorine75Tp60.0000.001570.0000.012080.0000.054790.0000.1730100.000.4275[75], (33)Lines: 1090 to 1125———* 528.0pt PgVar———Normal Page* PgEnds: PageBreak[75], (33)12345678910111213141516171819202122232425262728293031323334353637383940414243444576BOOKCOMP, Inc.