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参数名称符号数据单位气体流量qv1200m3/h操作温度T20Co气体临界温度196Co操作压力P0.101MPa液体密度ρL1000kg/m3气体密度ρG3kg/m3气体粘度μG0.000007259Pa.s气体临界压力3.37MPa液体流量QL(m3/min)QL0.055555556m3/min液体滞留时间t(min)t0.016666667min阻力系数查表附录Bf4.6气体压缩因子查表Z0.9滴液直径dL0.00008m修正系数k10.8重力加速度g(m/s2)g9.81m/s2KSBKSB0.107m/s容器内横截面积F9.354303556m2气体临界温度469K对比温度0.624733475四、计算结果二、查表系数三、固定值常数气液分离器计算公式本套公式根据GB50350-20056.2中立式重力分离器和石油化工设备设计手册第八篇第五部分直立式气液分离器编辑一、操作/介质参数对比压力0.029970326液滴沉降速度wo0.274952012m/s气体通过丝网最大允许速度1.950611272m/s液体区高度HL9.8984E-05m封头高度0.887781447m气体通过丝网最大设计速度1.462958454m/sf.(Re2)结果查附录B阻力系数380.1373345立式重力分离器直径3.451125787mA总高(m)B(m)C气体区(m)D直径(m)6.3995691125.5117876654.3139072343.451125787密度动力粘度kg/m3μPa·s空气air1.16918.448氨气ammonia0.69410.093氩argon1.61322.624丁烷butane2.4167.406丁烯1-butene2.3278.163二氧化碳carbondioxide1.78414.932一氧化碳carbonmonoxide1.1317.649二甲醚dimethylether1.8959.1乙烷ethane1.2229.354乙烯ethylene(ethane)1.13810.318氢hydrogen0.0818.915氢化硫hydrogensulfide1.38512.387异丁烷isobutane2.4077.498异丁烯isobutene2.3278.085氪krypton3.38725.132甲烷methane0.64811.067氖neon0.81431.113新戊烷neopentane3.0217.259氮nitrogen1.1317.805一氧化二氮nitrousoxide1.78514.841氧oxygen1.29220.55仲氢parahydrogen0.0818.915丙烷propane1.8088.146物质英文名常见气体的粘度、密度值25℃,常压丙烯propylene1.7228.56R115.74410.162R1147.10910.807R1156.34712.515R1165.62614.148R124.97111.807R1245.65111.593R1254.91512.962R134.25214.362R134a4.20111.819R143.56317.244R142b4.1610.421R143a3.44811.087R152a2.72210.081R2187.74812.49R223.53912.631R227ea7.0511.591R232.84614.913R236ea6.35410.897R236fa6.33210.96R245ca5.66110.117R245fa5.63910.303R322.12512.613R411.38410.955RC3188.31511.505反丁烯二酸trans-2-butene2.3348.028二氯碘甲烷trifluoroiodomethane8.08214.277氙xenon5.32422.984(qvTZ)/(PWoK1)[4gdL(ρL-ρG)]/3ρGf(ρL-ρG)/ρG972266.87340.075598609332.3333333计算过程请勿改动E液体区(m)9.8984E-05f.(Re2)=运动粘度换算粘度mm2/sPa·s15.7870.00001844814.5390.00001009314.030.0000226243.0650.0000074063.5070.0000081638.3690.00001493215.6140.0000176494.8010.00000917.6540.0000093549.0660.000010318109.690.0000089158.9420.0000123873.1150.0000074983.4740.0000080857.4190.00002513217.0710.00001106738.2390.0000311132.4030.00000725915.7530.0000178058.3140.000014841对比压力=15.910.00002055对比温度=109.690.0000089154.5070.000008146常见气体的粘度、密度值25℃,常压气体压缩因子表4.9710.000008561.7690.0000101621.520.0000108071.9720.0000125152.5150.0000141482.3750.0000118072.0510.0000115932.6370.0000129623.3780.0000143622.8130.0000118194.8390.0000172442.5050.0000104213.2150.0000110873.7040.0000100811.6120.000012493.5690.0000126311.6440.0000115915.240.0000149131.7150.0000108971.7310.000010961.7870.0000101171.8270.0000103035.9370.0000126137.9130.0000109551.3840.0000115053.440.0000080281.7670.0000142774.3170.000022984380.1373345392350000000000000000000.0299703260.624733475气体压缩因子表
本文标题:气液重力分离器计算软件
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