低温甲醇洗工艺流程图及物料平衡.xls

11C2201679824NH32C2202CWK2201235222NH314151619345396965686740454113424318CW56727383708293LSLC8163LSLC71NH33462CWCWNH3C2204C2203氮气放空气体脱盐水杂质水261C2205C2206D2205D2204D2203D2202D2201P2207D2206P2208P2209T2201P2205A/BP2204A/BP2201A/BP2202A/BP2203A/BP2206A/BE2201E2202E2204E2203E2205E2206E2207A/BE2208E2209E2210E2211E2212E2213E2214A-CE2215A-HE2216E2217E2218E2219E2220E2221E2222E2224E2225E2223E2225E2223去C2205去C2205去D22041217202128303132333635373851535457585966排放746127火炬火炬66中石化湖北化肥煤代油改造工程低温甲醇洗工序工艺流程图 PFD2004年5月变换气净化气CO2产品冷凝液60254429LALLAL6455LCLCLCLCPCLSFCLCFCLCFCLCFCFCLCFCTCFIFFCFFCLCLCPCLCPCFCLCFCFCLCFCFCCLAUS气体E2216D2204D2205E2215A-H55PCE2201、E2203变换气/净化气换热器、E2202变换气氨冷器E2204变换气/二氧化碳产品换热器E2205、E2206硫化氢、二氧化碳吸收塔甲醇氨冷器E2207循环甲醇冷却器E2208、E2209水冷器E2210循环气压缩机进出口换热器E2211闪蒸甲醇氨冷器E2212氮气冷却器E2213液氨过冷器E2214再吸收塔甲醇/贫甲醇换热器E2215富/贫甲醇换热器E2216热闪蒸气冷凝器E2217、E2219预洗甲醇加热器、E2218热再生气体急冷器E2220热再生塔冷凝器E2221克劳斯气体再热器E2222克劳斯气体/尾气换热器E2223、E2224E2225污水冷却器C2201硫化氢吸收塔C2202二氧化碳吸收塔C2203中压闪蒸塔C2204再吸收塔C2205热再生塔C2206甲醇精馏塔D2201变换气分离器D2202循环气压缩机分离罐D2203预洗甲醇闪蒸罐D2204回流罐D2205克劳斯气体分离器D2206地下甲醇槽P2201硫化氢吸收塔给料泵P2202再吸收塔循环泵P2203热再生塔给料泵P2204贫甲醇泵P2205甲醇精馏塔给料泵P2206热再生塔回流泵P2207地下甲醇泵P2208补液泵P2209新鲜甲醇泵T2201新鲜甲醇储槽K2201循环气压缩机序号1位号1232描述来自界区的变换气来自D2201变换气去E2203变换气3来自变换工序D2201D22014流向E2201E2203/E2204E22035相态气相6成分kmol/h%kmol/h%kmol/h%7CO23368.039.9173368.040.0242424.940.0688CO33.70.39933.70.40024.50.4059H24650.555.1174650.555.2653335.655.00610CH40.00.0000.00.0000.00.00011N2336.63.990336.64.000242.54.00712AR5.90.0705.90.0704.20.07013H2S20.20.23920.20.24014.70.24314COS0.10.0010.10.0010.10.00115MEOH0.00.0000.00.0005.50.09216H2O22.50.2670.00.0000.00.000171819总流量kmol/h8437.58415.06052.020总流量kg/h169308.2168902.3121774.721液相气相液相气相液相气相22体积流量m3/h|Nm3/h189117.2188612.1135649.124质量流量kg/h169308.2168902.3121774.625摩尔流量kmol/h8437.58415605226摩尔质量kg/kmol20.06620.07220.12127比重kg/m326.1828.6728.928比热 kj/kg k1.7221.6851.68229粘度 mPa s0.0140.0130.01330电导率 kW/m k6.87E-56.31E-56.27E-531摩尔百分比%100.000100.000100.00032质量百分比%100.000100.000100.00033温度 40.08.06.634压力 MPa（g）3.2493.2143.214备注：序号1位号4562描述去E2204变换气去C2201变换气脱硫气3来自D2201E2203C22014流向E2204C2201C22025相态气相气液混合气相6成分kmol/h%kmol/h%kmol/h%7CO2990.340.0683451.240.0682986.737.0308CO10.00.40534.50.40534.40.4279H21362.355.1164697.955.1164695.558.21610CH40.00.0000.00.0000.00.00011N299.04.007341.54.007341.54.23412AR1.70.0706.00.0706.00.07413H2S6.00.24320.70.2430.00.00014COS0.00.0010.10.0010.00.00015MEOH2.30.0927.80.0921.50.01916H2O0.00.0000.00.0000.00.000171819总流量kmol/h2471.620总流量kg/h19732.421液相气相液相气相液相气相22体积流量m3/h|Nm3/h55398.70.4190805.1180783.124质量流量kg/h49732.4392.6171114.4151728.325摩尔流量kmol/h2471.610.88512.88065.726摩尔质量kg/kmol20.12136.25720.10118.81227比重kg/m328.9913.8832.9629.4128比热 kj/kg k1.6821.9531.691.77229粘度 mPa s0.0130.6550.0120.01230电导率 kW/m k6.27E-51.65E-45.68E-56.14E-631摩尔百分比%100.0000.12799.873100.00032质量百分比%100.0000.22999.771100.00033温度 6.6-26.7-22.734压力 MPa（g）3.2143.1943.114备注：序号1位号7892描述来自C2202的净化气来自E2203净化气出界区净化气3来自C2202E2203E22014流向E2203E2201界区5相态气相气相6成分kmol/h%kmol/h%kmol/h%7CO20.00.0010.00.0010.00.0018CO33.40.66533.40.66533.40.6659H24646.492.4844646.492.4844646.492.48410CH40.00.0000.00.0000.00.00011N2337.96.726337.96.726337.96.72612AR5.90.1175.90.1175.90.11713H2S0.00.0000.00.0000.00.00014COS0.00.0000.00.0000.00.00015MEOH0.40.0070.40.0070.40.00716H2O0.00.0000.00.0000.00.000171819总流量kmol/h5024.05024.05024.020总流量kg/h20017.220017.220017.221液相气相液相气相液相气相22体积流量m3/h|Nm3/h112608.9112608.9112608.824质量流量kg/h20017.220017.220017.225摩尔流量kmol/h50245024502426摩尔质量kg/kmol3.9843.9843.98427比重kg/m36.575.384.8328比热 kj/kg k7.2777.2847.29329粘度 mPa s0.0090.010.01130电导率 kW/m k1.25E-41.43E-41.54E-431摩尔百分比%100.000100.000100.00032质量百分比%100.000100.000100.00033温度-46.22.032.034压力 MPa（g）3.0513.0313.011备注：序号1位号1112132描述变换气冷凝液来自C2202上段富甲醇来自C2202中段富甲醇3来自D2201C2202C22024流向界区E2206E22075相态液相液相液相6成分kmol/h%kmol/h%kmol/h%7CO20.21.199758.76.7071583.913.0508CO0.00.0001.00.0091.00.0089H20.00.01448.30.42747.90.39510CH40.00.0000.00.0000.00.00011N20.00.0015.30.0474.50.03712AR0.00.0000.20.0010.10.00113H2S0.00.0200.00.0000.00.00014COS0.00.0000.00.0000.00.00015MEOH0.00.00010499.892.81010499.786.50916H2O19.198.7650.00.0000.00.000171819总流量kmol/h19.311313.212137.120总流量kg/h353.9370093.6406380.621液相气相液相气相液相气相22体积流量m3/h|Nm3/h0.4439.1477.324质量流量kg/h353.9370093.6406380.725摩尔流量kmol/h19.311313.212137.126摩尔质量kg/kmol18.32832.71333.48327比重kg/m3995.93842.81851.428比热 kj/kg k4.6562.1812.12429粘度 mPa s1.3421.140.91730电导率 kW/m k4.14E-42.00E-41.86E-431摩尔百分比%100.000100.000100.00032质量百分比%100.000100.000100.00033温度 8.0-26.0-20.534压力 MPa（g）3.1643.1423.152备注：序号1位号1415162描述C2202底部去P2201富甲醇C2201主洗段甲醇C2201预洗段甲醇3来自C2202E2205E22054流向P2201C2201主洗段C2201预洗段5相态液相液相液相6成分kmol/h%kmol/h%kmol/h%7CO21040.922.0551007.422.05531.322.0558CO0.40.0070.30.0070.00.0079H217.10.36316.60.3630.50.36310CH40.00.0000.00.0000.00.00011N21.30.0271.20.0270.00.02712AR0.00.0010.00.0010.00.00113H2S0.00.0000.00.0000.00.00014COS0.00.0000.00.0000.00.00015MEOH3660.077.5472542.277.547110.077.54716H2O0.00.0000.00.0000.00.000171819总流量kmol/h4719.74567.8141.820总流量kg/h163165.2157915.64903.921液相气相液相气相液相气相22体积流量m3/h|Nm3/h187.8176.45.524质量流量kg/h163165.2157915.64903.925摩尔流量kmol/h4719.74567.8141.826摩尔质量kg/kmol34.57134.57134.57127比重kg/m3868.75895.24895.2428比热 kj/kg k2.0561.9861.98629粘度 mPa s0.7551.0641.06430电导率 kW/m k1.73E-41.85E-41.85E-431摩尔百分比%100.000100.000100.00032质量百分比%100.000100.000100.00033温度-18.8-36.0-36.034压力 MPa（g）3.1143.5443.174备注：序号1位号1718192描述去C2203富S甲醇C2201底部去E2217富甲醇进变换气喷淋甲醇3来自C2201主洗段C2201P22014流向C2203E2217E22035相态液相液相液相6成分kmol/h%kmol/h%kmol/h%7CO21400.828.11466.535.8892.222.0558CO0.40.0080.00.0090.00.0079H218.70.3750.70.3990.00.36310CH40.00.0000.00.0000.00.00011N21.20.0240.00.0210.00.02712AR0.00.0010.00.0010.00.00113H2S19.50.3911.20.6530.00.00014COS0.10.0020.00.0020.00.00015MEOH3541.971.087116.763.0267.877.57416H2O0.00.0000.00.0000.00.000171819总流量kmol/h4982.5185.211.020总流量kg/h175889.86709.1346.721液相气相液相气相液相气相22体积流量m3/h|Nm3/h198.47.30.424质量流量kg/h175889.76709345.725摩尔流量kmol/h4982.5185.21026摩尔质量kg/kmol35.30236.23234.57127比重kg/m3886.5913.33868.4428比热 kj/kg k1.9931.9562.05929粘度 mPa s0.7030.6580.75230电导率 kW/m k1.68E-41.65E-41.73E-431摩尔百分比%100.000100.000100.00032质量百分比%100.000100.000100.00033温度-21.6-26.6-18.634压力 MPa（g）3.1743.1843.564备注：序号1位号2021222描述C2202底部去C2203富甲醇C2203上段闪蒸气出C2203循环气3来自C2202C2203上段C22034流向C2203C2203下段E22105相态液相气相气相6成分kmol/h%kmol/h%kmol/h%7CO21945.722.055163.083.5437.212.1128CO0.70.0070.50.2630.81.3719H232.00.36329.314.99846.677.97210CH40.00.0000.00.0000.00.00011N22.40.0272.11.0974.88.08812AR0.10.0010.10.0320.10.15413H2S0.00.0000.00.0000.20.28814COS0.00.0000.00.0000.00.00215MEOH6841.377.5470.10.0670.00.01416H2O0.00.0000.00.0000.00.000171819总流量kmol/h8822.1195.159.720总流量kg/h304991.87312.8579.221液相气相液相气相液相气相22体积流量m3/h|Nm3/h351.14372.81338.224质量流量kg/h304991.87312.8579.225摩尔流量kmol/h8822.1195.159.726摩尔质量kg/kmol34.57137.4849.70127比重kg/m3868.7520.774.228比热 kj/kg k2.0560.9813.04729粘度 mPa s0.7550.0130.0130电导率 kW/m k1.73E-42.16E-59.01E-531摩尔百分比%100.000100.000100.00032质量百分比%100.000100.000100.00033温度-18.8-21.5-45.634压力 MPa（g）3.1140.9890.719备注：序号1位号2324252描述C2203与D2203总循环气 进E2203循环气出C2204顶部二氧化碳产品气3来自C2203/D2203E2210C22044流向E2210E2203E22045相态气相气液混合相气相6成分kmol/h%kmol/h%kmol/h%7CO245.045.64345.045.6391447.999.6538CO0.80.8460.80.8460.20.0169H247.347.94447.347.9484.10.28210CH40.00.0000.00.0000.00.00011N24.94.9364.94.9360.30.02212AR0.10.0950.10.0950.00.00113H2S0.50.4880.50.4870.00.00014COS0.00.0030.00.0030.00.00015MEOH0.00.0460.00.0460.40.02616H2O0.00.0000.00.0000.00.000171819总流量kmol/h59.798.71453.020总流量kg/h579.22259.663759.421液相气相液相气相液相气相22体积流量m3/h|Nm3/h2212.202211.432566.524质量流量kg/h2259.60.32258.863759.425摩尔流量kmol/h98.7098.7145326摩尔质量kg/kmol22.89534.84622.89543.88227比重kg/m39.61862.5935.94.3328比热 kj/kg k1.4062.1211.5260.77829粘度 mPa s0.0110.0130.01130电导率 kW/m k4.73E-55.10E-51.09E-531摩尔百分比%100.0000.00999.991100.00032质量百分比%100.0000.01399.987100.00033温度-35.7-12.4-53.734压力 MPa（g）0.7193.2140.074备注：序号1位号2627282描述出界区二氧化碳产品气来自界区气提氮气C2204放空尾气3来自E2204界区C2204放空尾气4流向界区E2212E2212/E22225相态气相气相气相6成分kmol/h%kmol/h%kmol/h%7CO21447.999.6530.00.0001865.274.1938CO0.20.0160.00.0000.00.0009H24.10.2820.00.0000.00.00110CH40.00.0000.00.0000.00.00011N20.30.022650.0100.000648.425.79012AR0.00.0010.00.0000.00.00013H2S0.00.0000.00.0000.00.00014COS0.00.0000.00.0000.00.00115MEOH0.40.4000.00.0000.40.01616H2O0.00.0000.00.0000.00.000171819总流量kmol/h1453.0650.02514.020总流量kg/h63759.418208.5100266.121液相气相液相气相液相气相22体积流量m3/h|Nm3/h32566.51456956349.124质量流量kg/h63759.418208.5100266.125摩尔流量kmol/h1453650251426摩尔质量kg/kmol43.88228.01339.88327比重kg/m33.16.033.3128比热 kj/kg k0.8311.0490.81729粘度 mPa s0.0140.0180.01130电导率 kW/m k1.48E-52.67E-51.24E-531摩尔百分比%100.000100.000100.00032质量百分比%100.000100.000100.00033温度 2.040.0-60.234压力 MPa（g）0.0590.4590.044备注：序号1位号2930312描述进E2212放空尾气进E2222放空尾气出C2203富C甲醇3来自C2204C2204C22034流向E2212E2222E22115相态气相气相液相6成分kmol/h%kmol/h%kmol/h%7CO21308.874.193556.474.1931782.720.6648CO0.00.0000.00.0000.10.0029H20.00.0010.00.0012.80.03210CH40.00.0000.00.0000.00.00011N2454.925.790193.425.7900.20.00312AR0.00.0000.00.0000.00.00013H2S0.00.0000.00.0000.00.00014COS0.00.0010.00.0010.00.00015MEOH0.30.0160.10.0166841.279.29916H2O0.00.0000.00.0000.00.000171819总流量kmol/h1764.0750.08627.020总流量kg/h70354.229911.9297678.921液相气相液相气相液相气相22体积流量m3/h|Nm3/h39538.716810.3340.524质量流量kg/h70354.229911.9297678.925摩尔流量kmol/h1764750862726摩尔质量kg/kmol39.88339.88334.50527比重kg/m33.093.09874.1828比热 kj/kg k0.8160.8162.05829粘度 mPa s0.0110.0110.82430电导率 kW/m k1.24E-51.24E-51.77E-431摩尔百分比%100.000100.000100.00032质量百分比%100.000100.000100.00033温度-60.3-60.3-21.534压力 MPa（g）0.0340.0340.989备注：序号1位号3233342描述去C2204顶部富C甲醇去C2204第2段富C甲醇C2203底部去C2204富S甲醇3来自E2211E2211C22034流向C2204C2204C22045相态液相液相液相6成分kmol/h%kmol/h%kmol/h%7CO2870.720.664912.120.6641636.419.9098CO0.10.0020.10.0020.10.0019H21.30.0321.40.0321.40.01610CH40.00.0000.00.0000.00.00011N20.10.0030.10.0030.10.00112AR0.00.0000.00.0000.00.00013H2S0.00.0000.00.00038.80.47214COS0.00.0000.00.0000.20.00215MEOH3341.279.2993500.079.2996542.179.59816H2O0.00.0000.00.0000.00.000171819总流量kmol/h4213.44413.68219.020总流量kg/h145384.9152293.9282980.621液相气相液相气相液相气相22体积流量m3/h|Nm3/h162.5170.3321.324质量流量kg/h145384.9152294282980.625摩尔流量kmol/h4213.44413.6821926摩尔质量kg/kmol34.50534.50534.4327比重kg/m3894.47894.47880.7528比热 kj/kg k1.9981.9982.03329粘度 mPa s1.0811.0810.91730电导率 kW/m k1.86E-41.86E-41.82E-431摩尔百分比%100.000100.000100.00032质量百分比%100.000100.000100.00033温度-35.0-35.0-26.734压力 MPa（g）0.9690.9690.739备注：序号1位号3537382描述C2203底部去C2204第2段富S甲醇C2204上段流向C2204第3段甲醇液C2204第二段流向C2204第3段甲醇液3来自C2203C2204第一段C2205第二段4流向C2204C2204第三酸C2205第三酸5相态液相液相液相6成分kmol/h%kmol/h%kmol/h%7CO21636.419.909525.813.5971445.212.5398CO0.10.0010.00.0000.00.0009H21.40.0160.00.0000.00.00010CH40.00.0000.00.0000.00.00011N20.10.0010.00.0000.00.00012AR0.00.0000.00.0000.00.00013H2S38.80.4720.00.00038.80.33614COS0.20.0020.00.0000.20.00115MEOH6542.179.5983341.186.40310041.987.12316H2O0.00.0000.00.0000.00.000171819总流量kmol/h3866.911527.020总流量kg/h130196.4386703.721液相气相液相气相液相气相22体积流量m3/h|Nm3/h321.3144.8434.224质量流量kg/h282980.6130196.43867.3.725摩尔流量kmol/h82193866.91152726摩尔质量kg/kmol34.4333.66933.54827比重kg/m3880.75898.93890.5628比热 kj/kg k2.0332.0092.03929粘度 mPa s0.9171.9481.75530电导率 kW/m k1.82E-42.05E-42.04E-431摩尔百分比%100.000100.000100.00032质量百分比%100.000100.000100.00033温度-26.7-53.6-49.134压力 MPa（g）0.7390.0840.109备注：序号1位号3940412描述出C2204第三段甲醇循环甲醇去C2204第四段出C2204底部甲醇3来自C2204P2202C22044流向P2202C2204P22035相态液相液相液相6成分kmol/h%kmol/h%kmol/h%7CO21563.010.3751561.410.375362.62.5728CO0.00.0000.00.0000.00.0009H20.00.0000.00.0000.00.00010CH40.00.0000.00.0000.00.00011N22.50.0172.50.0177.30.05212AR0.00.0000.00.0000.00.00013H2S111.50.740111.40.74088.60.62814COS0.60.0040.60.0040.40.00315MEOH13388.288.86513374.988.86513641.196.75416H2O0.00.0000.00.0000.00.000171819总流量kmol/h15.65.815050.814100.020总流量kg/h501700.1501199.6456304.821液相气相液相气相液相气相22体积流量m3/h|Nm3/h564.3578.852924质量流量kg/h501699.9501199.6456304.925摩尔流量kmol/h15065.815050.814100.126摩尔质量kg/kmol33.30133.30132.36227比重kg/m3889.03865.97862.6628比热 kj/kg k2.0532.1072.16629粘度 mPa s2.041.2452.25430电导率 kW/m k2.09E-41.98E-42.19E-431摩尔百分比%100.000100.000100.00032质量百分比%100.000100.000100.00033温度-53.5-33.3-51.934压力 MPa（g）0.1090.3990.119备注：序号1位号4243442描述出P2203甲醇出E2207富S甲醇P2203去C2203的甲醇3来自P2203E2207P22034流向E2207E2215C22035相态液相液相液相6成分kmol/h%kmol/h%kmol/h%7CO2282.92.572282.92.57279.82.5728CO0.00.0000.00.0000.00.0009H20.00.0000.00.0000.00.00010CH40.00.0000.00.0000.00.00011N25.70.0525.70.0521.60.05212AR0.00.0000.00.0000.00.00013H2S69.10.62869.10.62819.50.62814COS0.30.0030.30.0030.10.00315MEOH10641.096.74510641.096.7453000.196.74516H2O0.00.0000.00.0000.00.000171819总流量kmol/h10999.010999.03101.020总流量kg/h355949.2355949.2100355.821液相气相液相气相液相气相22体积流量m3/h|Nm3/h412.7423.9116.424质量流量kg/h355949.1355949.1100355.825摩尔流量kmol/h1099910999310126摩尔质量kg/kmol32.36232.36232.36227比重kg/m3862.39839.63862.3928比热 kj/kg k2.1672.232.16729粘度 mPa s2.2361.2642.23630电导率 kW/m k2.19E-42.19E-62.19E-431摩尔百分比%100.000100.000100.00032质量百分比%100.000100.000100.00033温度-51.6-27.5-51.634压力 MPa（g）1.3191.1691.319备注：序号1位号4551522描述P2202去D2205富甲醇放空尾气出D2203循环气3来自P2202E2213/E2218D22034流向D2205放空E22105相态液相气相气相6成分kmol/h%kmol/h%kmol/h%7CO21.610.3751865.274.19337.897.0808CO0.00.0000.00.0000.00.0429H20.00.0000.00.0010.71.88210CH40.00.0000.00.0000.00.00011N20.00.017648.425.7900.00.09312AR0.00.0000.00.0000.00.00313H2S0.10.7400.00.0000.30.79414COS0.00.0040.00.0010.00.00315MEOH13.388.8660.40.0160.00.09616H2O0.00.0000.00.0000.00.000171819总流量kmol/h15.02514.039.020总流量kg/h199.5100266.11680.421液相气相液相气相液相气相22体积流量m3/h|Nm3/h0.656349.1873.724质量流量kg/h499.5100266.11680.425摩尔流量kmol/h1525143926摩尔质量kg/kmol33.30139.88343.10827比重kg/m3889.02218.2228比热 kj/kg k2.0530.8670.87329粘度 mPa s2.040.0150.01330电导率 kW/m k2.09E-41.69E-51.41E-531摩尔百分比%100.000100.000100.00032质量百分比%100.000100.000100.00033温度-53.53.8-20.134压力 MPa（g）0.4990.0140.719备注：序号1位号5354552描述C2205热闪蒸气出E2216酸性气体出E2218酸性气体3来自C2205E2216E22184流向E2216E2217C22045相态混合相态气相气相6成分kmol/h%kmol/h%kmol/h%7CO2236.042.393234.673.814232.382.2078CO0.00.0000.00.0000.00.0009H20.00.0000.00.0000.00.00010CH40.00.0000.00.0000.00.00011N25.61.0125.71.7795.61.98612AR0.00.0000.00.0000.00.00013H2S43.27.76241.613.08240.714.40414COS0.20.0380.20.0640.20.07115MEOH271.748.79535.811.2623.81.33216H2O0.00.0000.00.0000.00.000171819总流量kmol/h556.7317.9282.620总流量kg/h20738.013054.511912.221液相气相液相气相液相气相22体积流量m3/h|Nm3/h0.512242.17125.16334.224质量流量kg/h338.220399.813054.511912.225摩尔流量kmol/h10.5546.2317.9282.626摩尔质量kg/kmol32.08837.3541.06642.15227比重kg/m3735.554.14.74.0528比热 kj/kg k2.9851.1720.9420.85429粘度 mPa s0.2840.0140.0150.01330电导率 kW/m k1.84E-42.00E-51.77E-51.45E-531摩尔百分比%1.89398.107100.000100.00032质量百分比%1.63198.369100.000100.00033温度 74.640.0-5.634压力 MPa（g）0.2090.1920.109备注：序号1位号5657582描述出C2205去E2219的酸性气体D2204去E2221酸性气体 出C2205顶部酸性气体3来自C2205D2204去E2221酸性气体 D22054流向E2219E2221C22045相态气相气相气相6成分kmol/h%kmol/h%kmol/h%7CO277.124.09577.364.37422.576.7798CO0.00.0000.00.0000.00.0009H20.00.0020.00.0040.00.00510CH40.00.0000.00.0000.00.00011N20.10.0260.10.0690.00.08912AR0.00.0000.00.0000.00.00013H2S29.79.27929.724.7556.722.94614COS0.10.0320.10.0840.0