Page 15 - Demo

Acetylene n-HexaneHydrogenMethaneNitrogenOxygenHydrogen chlorideDichloro difluoro methaneAirArgonAmmoniaCarbon disulfideHydrogen sulfideCarbon dioxideCarbon monoxideEthyl alcoholn-HeptaneCyclohexaneEthyleneiso-Butanen-Butanen-DecaneEthaneBenzeneChlorineButadieneC2H2 26.04 1.26 n-C6H14 86.18 1.06CO 28.01 1.40 n-CH3(CH2)7CH3 or C9H20 128.26 1.04C6H6 78.12 1.12 CH4 16.04 1.31Sulfur dioxidePropyleneC2H5OH or C2H6O 46.07 - SO2 or O2S 64.06 1.29- 28.97 1.40 HCl 36.46 1.41Cl2 70.91 1.36 O2 32.00 1.40iso-C4H10 or CH(CH3)3 58.12 1.10 CH3OH or CH4O 32.04 1.20C2H4 28.05 1.24 C6H5CH3 or C7H8 92.15 1.09Ar 39.95 1.67 H2S 34.08 1.32n-PropaneWatern-C10H22 142.29 1.03 n-CH3CH2CH3 or C3H8 44.10 1.13CS2 76.14 1.21 N2 28.01 1.40n-CH3(CH2)5CH3 or C7H16 100.21 1.05 CH3(CH2)6CH3 or C8H18 114.00 1.05NH3 17.03 1.31 H2 2.02 1.41C6H12 84.16 1.09 n-CH3(CH2)3CH3 or C5H12 72.15 1.07Methyl chlorideNitrogen dioxiden-C4H10 58.12 1.09 CH3Cl 50.49 1.20Helium He 4.00 1.66 CH3CHCH2 or C3H6 42.08 1.15C4H6 54.09 1.113 CCl2F2 120.91 1.139C2H6 30.07 1.19 H2O 18.02 1.133CO2 44.01 1.29 NO2 44.01 1.30P0PbIsentropic exponent(k)Volume modification factor for back pressure0.450.500.550.600.650.700.750.800.820.840.860.880.900.920.940.960.981.001.0000.9850.9700.9480.9190.8810.8310.7690.6870.5790.4220.0000.9990.9950.9650.9440.9170.8840.8420.7910.7270.6470.5420.3930.0000.9990.9830.9420.9180.8880.8520.8090.7570.6930.6140.5130.3710.0000.9930.9680.9210.8940.8620.8000.7800.7280.6640.5870.4890.3530.0000.9990.9850.9530.9000.8720.8390.7790.7550.7030.6400.5650.4690.3370.0001.0000.9950.9750.9380.8810.8520.8180.7590.7330.6810.6190.5450.4520.3250.0000.9990.9890.9640.9230.8640.8330.7990.7420.7140.6620.6010.5280.4380.3140.0000.9990.9970.9820.9530.9090.8470.8170.7820.7270.6970.6450.5850.5140.4250.3050.0001.0000.9930.9740.9430.8960.8330.8010.7660.7120.6820.6310.5710.5010.4140.2960.0000.9990.9890.9710.9450.9090.8540.8080.7390.7070.6720.6340.5920.5440.4900.4280.3520.2510.0000.9990.9920.9750.9500.9150.8710.8150.7470.7150.6800.6410.5990.5510.4970.4340.3570.2540.0001.0000.9940.9790.9550.9220.8790.8240.7550.7230.6880.6490.6060.5580.5040.4400.3620.2580.0000.9960.9830.9610.9290.8860.8320.7640.7320.6970.6580.6150.5660.5110.4460.3670.2620.0000.9990.9870.9670.9360.8950.8410.7730.7410.7060.6670.6240.5750.5190.4530.3730.2660.0000.9990.9910.9720.9440.9030.8510.7830.7520.7160.6670.6330.5840.5270.4610.3800.2710.0001.0000.9940.9780.9510.9130.8610.7940.7530.7270.6770.6440.5940.5370.4700.3870.2770.0001.0000.9970.9830.9590.9220.8720.8060.7740.7390.6880.6550.6050.5470.4790.3950.2820.0000.9990.9890.9670.9320.8840.8190.7870.7520.7000.6880.6170.5590.4890.4040.2890.0000.9990.9920.9790.9570.9240.8800.8200.7390.6280.4260.0000.4 0.5 0.6 0.7 0.8 0.9 1.001 1.1 1.2 1.3 1.4 1.5 1.6 1.7 1.8 1.9 2.0 2.1 2.2Reynold%u2019s numberViscosity modification factor 1.00.90.80.70.60.50.40.310 20 40 60 80 100 200 400 600 800 1,000 2,000 4,000 10,000 20,000 100,000Methyl alcoholn-Nonanen-PentaneTolueneOctaneFDC BROCHURE | 14 | 15 |Table 1. Physical properties of gasMol weight(M) Physial property Name Formula Adiabatic constant(K) Mol weight(M) Physial property Name Formula Adiabatic constant(k)Table 2. Capacity correction factor for back pressureTable 3. Capacity correction factor for viscosity