液氨饱和蒸气压力值

1、液氨饱和蒸气压力值温度 ()-78-76-74-72-70-68-66-64-62-60压力 (大气压)0.05820.06830.07970.09290.10780.12460.14370.16510.18910.2161温度 ()-58-56-54-52-50-48-46-44-42-40压力 (大气压)0.24610.27960.31670.35780.40340.45360.50870.56930.63570.7083温度()-38-36-34-32-30-28-26-24-22-20压力 (大气压)0.78750.87380.96761.06951.17991.29921.42811

2、.56711.71661.8774温度()-18-16-14-12-10-8-6-4-20压力 (大气压)2.04992.23492.43282.64432.87033.11123.36773.64053.93034.2380温度 ()2468101214161820压力 (大气压)4.56404.90905.27505.66106.06856.49856.95207.42907.93108.4585温度 ()22242628303234363840压力 (大气压)11.51212.21212.94313.70814.50715.33916.20917.11318.0569.0125温度 ()

3、42444648505254565860压力 (大气压)9.594010.20410.84319.03820.05921.12122.22423.37224.56225.797温度 ()62646668707274767880压力 (大气压)27.07928.40729.78431.21132.68734.22735.81337.45339.14940.902温度 ()828486889092949698100压力 (大气压)42.71244.58246.51148.50350.55852.67754.86057.11159.42961.816温度 ()10210410610811011211

4、4116118120压力 (大气压)64.27466.80469.40672.08474.83777.66880.57883.57086.64489.802温度 ()122124126128130132132.3压力 (大气压)93.04596.37699.796103.309106.913110.613111.3注意：表中所给压力为绝压。投入FPCl大约163kg，甲苯大约70kg（约80L）；通入液氨总量大约35kg，其中理论反应大约27kg，液氨剩余大约8kg，常压体积大约10541L。 现使用1000L反应釜，反应体积大约240L，气相体积大约760L，折算剩余的液氨在釜内的压力是：1

5、0541/760*1.013E5=14E5帕=1.4MPa。氯代完毕，产品平均分子量：172.1，投入液氨35kg，理论需求：32kg，液氨剩余3kg。温度蒸汽压MPa(a)温度蒸汽压MPa(a)温度蒸汽压MPa(a)温度蒸汽压MPa(a)温度蒸汽压MPa(a)-400.072-200.19000.429200.857401.554-380.079-180.20820.462220.913421.642-360.089-160.22640.497240.972441.734-340.098-140.24760.534261.034461.830-320.109-120.26880.574281.099481.929-300.120-100.291100.615301.167502.033-280.132-80.315120.658321.237522.140-260.145-60.341140.704341.311542.252