02 物料衡算表550

44物料热量衡算表4.4.2日产550吨氨、400吨甲醇系统物料热量衡算表4.4.2.13000低压醇化系统物料热量衡算表名称流量Nm3/h温度压力MPa组成%H2N2CH4ArCOCO2CH3OHH2O新鲜气量103830405.571.13215.5270.9820.31211.3980.5000.0000.149入塔气2987222255.4572.41920.1911.2670.4065.2000.3690.0000.149出塔气总量2771392505.269.77521.6471.3690.4351.8120.2864.4060.271出塔前换热器277139805.1569.77521.6471.3690.4351.8120.2864.4060.271出水冷器气量266515385.172.55622.5091.4230.4521.8840.2970.7290.149出醇分离器266515385.072.55622.5091.4230.4521.8840.2970.7290.149循环气量194892385.073.09022.6751.4340.4561.8980.3000.0000.149醇洗去高压醇化气量71100385.073.09022.6751.4340.4561.8980.3000.0000.149近路去高压醇化气0385.571.13215.5270.9820.31211.3980.5000.0000.149出醇分粗醇量1062496.6683.332冷却水量t/h2300334.4.2.21600高压醇化系统物料热量衡算表名称流量Nm3/h温度压力MPa组成%H2N2CH4ArCOCO2CH3OHH2O入塔总气量710194019.673.17422.7011.4350.4561.9000.3000.0000.034一次入塔气213064019.673.17422.7011.4350.4561.9000.3000.0000.034二次入塔气16519.5573.17422.7011.4350.4561.9000.3000.0000.034f0冷激气量4019.673.17422.7011.4350.4561.9000.3000.0000.034f1冷激气量4019.673.17422.7011.4350.4561.9000.3000.0000.034f2冷激气量4019.673.17422.7011.4350.4561.9000.3000.0000.034f3冷激气量4019.673.17422.7011.4350.4561.9000.3000.0000.034出塔气总量6793419019.371.66123.7321.4890.4770.0210.0082.2710.341出塔前换热器679348019.2571.66123.7321.4890.4770.0210.0082.2710.341出水冷器气量663263819.273.39824.3071.5250.4880.0220.0080.2180.034醇洗去甲烷化塔661823819.173.55824.3601.5280.4890.0220.0080.0000.034出醇分离器粗醇量160786.97213.028冷却水量t/h3704.4.2.31400高压甲烷化系统物料热量衡算表名称流量Nm3/h温度压力MPa组成%H2N2CH4ArCOCO2CH3OHH2O进塔总气量661824019.173.55824.3601.5280.4890.0220.0080.0000.034一次入塔气198544019.173.55824.3601.5280.4890.0220.0080.0000.034塔前换热器冷气出口6618222519.0573.55824.3601.5280.4890.0220.0080.0000.034提温换热器冷气出口6618225019.073.55824.3601.5280.4890.0220.0080.0000.034出塔气6614325018.873.50424.3751.5590.4900.00070.00030.0000.072塔前换热器热气出口661438018.7573.50524.3731.5590.4900.00070.00030.0000.072出水冷器气量661213818.773.53324.3831.5600.4900.00070.00030.0000.034出氨冷器气量66121818.6573.53324.3831.5600.4900.00070.00030.0000.034水分离器出口气量66101818.673.55024.3901.5600.4900.00070.00030.0000.004水分离器分离水量258100.000冷却水量t/h2304.4.2.41800串塔氨合成系统物料热量衡算表节点流量Nm3/h压力MPa温度 组成 %H2N2CH4ArNH31#塔总入塔气26944219.9536.557.7519.2516.503.503.001#塔一入气19.9536.557.7519.2516.503.503.002#塔一入气19.9536.557.7519.2516.503.503.001#塔二入气19.919057.7519.2516.503.503.00f0冷激气19.919057.7519.2516.503.503.00f1冷激气19.919057.7519.2516.503.503.00f2冷激气19.919057.7519.2516.503.503.00f3冷激气19.927057.7519.2516.503.503.002#塔总入塔气24603319.4533048.9716.3218.073.8312.80f0冷激气19.4533048.9716.3218.073.8312.80废锅入口气23924619.236046.1115.3718.583.9416.00热交热气入口23924619.123246.1115.3718.583.9416.00水冷入口气23924619.08646.1115.3718.583.9416.00冷交进口热气22885618.93848.1616.0519.374.1212.29冷交出口热气21831918.82350.4516.8120.264.318.161#氨冷进口气21280518.82350.4516.8120.264.318.162#氨冷进口气20602818.7852.0917.3620.904.455.202#氨冷出口气20169218.6-6.5753.2017.7321.344.553.19冷交进口冷气26944218.5-8.1957.7519.2516.503.503.00冷交出口冷气26944218.43057.7519.2516.503.503.00循环机进口气26944218.43057.7519.2516.503.503.00循环机出口气26944220.036