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[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
["表　各成分の塔頂および塔底ガス組成"]
["成分","メタン","エタン","プロパン","ブタン"]
["K",71.7,18.2,4.7,1.3]
["回収率",5.2999999999999999E-2,0.20799999999999999,0.73799999999999999,0.998]
["YB'(塔底ガス組成)",0.78,0.1,0.08,0.04]
["YT'(塔頂ガス組成)",0.74,8.2000000000000003E-2,2.8000000000000001E-2,2.0000000000000001E-4]

{"sheet":"COCO_ガス水Henry定数","index":3,"n_rows":83,"n_cols":10,"rows_kept":83,"cut":false,"hidden":false,"merged":[]}
["Fig. 4.27の再作成",null,null,"Henry, Seader, Roper: Separation Process Principles, Third edition, p. 177"]
[]
[null,"温度","1/H"]
["NH3",0,0.5]
[null,35,0.3]
[]
["SO2",0,6.4416926551517734E-2]
[null,43.2,1.4999999999999999E-2]
[]
["Br2",0,4.4999999999999998E-2]
[null,40,7.4473197390598871E-3]
[null,80,2.4717241450161313E-3]
[]
["Cl2",0,4.6451527522274926E-3]
[null,15.5,2.0137242498623887E-3]
[null,46.3,1.1066237839776653E-3]
[null,100,9.311078754678302E-4]
["H2S",0,3.6057864302164204E-3]
[null,40,1.2764388088113425E-3]
[null,100,5.9999999999999995E-4]
[]
["CO2",0,1.4E-3]
[null,23.1,5.9999999999999995E-4]
[null,60,2.9999999999999997E-4]
[]
["C2H4",0,1.8000000000000001E-4]
[null,20,9.7948998540869705E-5]
[null,40,6.7142885292595147E-5]
[]
["理想気体",0,7.27E-4]
[null,100,5.3200000000000003E-4]
[]
["C2H6",0,6.9999999999999994E-5]
[null,38.799999999999997,2.3768402866248777E-5]
[null,100,1.3489628825916516E-5]
[]
["CH4",0,5.0000000000000002E-5]
[null,40,1.8793168168032652E-5]
[null,100,1.2852866599436129E-5]
[]
["O2",0,3.4999999999999997E-5]
[null,40,1.7060823890031217E-5]
[null,100,1.2274392311584074E-5]
[]
["H2",0,1.7E-5]
[null,40,1.3489628825916516E-5]
[null,100,1.2E-5]
[]
["N2",0,1.7E-5]
[null,40,9.0000000000000002E-6]
[null,100,6.0000000000000002E-6]
[]
[]
[]
["COCOによるHenry定数推算",null,null,"EOS/predictiveSRK/(enthalpy)PredictiveSRK"]
["1atm ガスに平衡な水中モル分率"]
["温度℃",0,25,60]
["CO2",1.1000000000000001E-3,5.2999999999999998E-4,2.7E-4]
["SO2",0.12189999999999999,2.8799999999999999E-2,6.8999999999999999E-3]
["H2S",1.57E-3,1.0499999999999999E-3,5.9000000000000003E-4]
["CH4",6.6000000000000005E-5,4.1E-5,2.4000000000000001E-5]
["H2",1.8600000000000001E-5,1.6399999999999999E-5,1.2860000000000001E-5,null,null,null,null,45,60]
["N2",2.58E-5,1.88E-5,1.29E-5,null,null,null,null,0.19700000000000001,0.13400000000000001]
[null,null,45,60]
["NH3",null,0.19700000000000001,0.13400000000000001]
["COCO book p. 43のKによると",null,null,"<henry_NH3.fsk>"]
[null,0,25,60]
["NH3",null,0.61,0.15]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[]
[null,1000,"ft3"]
[null,{"$f":"B80*28.317","v":28317},"L"]
[null,{"$f":"B81/22.4","v":1264.1517857142858},"mol"]
[null,{"$f":"B82*44/1000","v":55.622678571428573},"kg-CO2"]

{"sheet":"COCO_CO2平衡","index":4,"n_rows":18,"n_cols":11,"rows_kept":18,"cut":false,"hidden":false,"merged":[]}
["CO2, CH4　水への溶解度",null,null,null,null,null,null,null,null,"分圧","溶解度"]
["小島　プロセス設計のための相平衡 p. 88",null,null,null,null,null,null,null,null,"MPa","mol frac"]
["25℃ p=1atmに平衡な水中溶解濃度　x [×10-4　モル分率]",null,null,null,null,null,null,"文献値","CO2",0,0]
["CO2 ",6.05,null,null,null,null,null,null,null,0.1013,6.0499999999999996E-4]
["CH4",0.248,null,null,null,null,null,null,null,1.0129999999999999,6.0499999999999998E-3]
[null,null,null,null,null,null,null,null,"CH4",0,0]
[null,{"$f":"B4/B5","v":24.39516129032258},null,null,null,null,null,null,null,0.1013,2.48E-5]
[null,null,null,null,null,null,null,null,null,1.0129999999999999,2.4800000000000001E-4]
[]
[null,null,null,null,null,null,null,"COCO EOS/Predictive SRK/(Enthalpy) ideal or predict SRK"]
[null,null,null,null,null,null,null,null,"CO2",0,0]
[null,null,null,null,null,null,null,null,null,0.1013,5.2999999999999998E-4]
[null,null,null,null,null,null,null,null,null,1.0129999999999999,5.3E-3]
[null,null,null,null,null,null,null,null,"CH4",0,0]
[null,null,null,null,null,null,null,null,null,0.1013,4.0800000000000002E-5]
[null,null,null,null,null,null,null,null,null,1.0129999999999999,4.0999999999999999E-4]
[]
[null,null,null,null,null,null,null,null,null,null,{"$f":"K13/K16","v":12.926829268292684}]