{"text_format":"3","workbook":"xlsx","n_sheets":7,"sheets":["Operating Lines","MT (Op Lines)","MT (Full)","Lewis","Lewis DIY","VLE","xy"],"not_rendered":{"charts":6,"macros":1,"defined_names":153},"unopened":[{"sheet":"MT (Op Lines)","index":1,"reason":"not_a_worksheet"},{"sheet":"MT (Full)","index":2,"reason":"not_a_worksheet"},{"sheet":"xy","index":6,"reason":"not_a_worksheet"}],"read":"whole","date_system":"1904"}

{"sheet":"Operating Lines","index":0,"n_rows":27,"n_cols":14,"rows_kept":27}
["Open Steam Data"]
["F =",{"v":100,"d":"100.0"},null,"Specifications"]
["z =",{"v":0.2,"d":"0.200"},{"$nulls":10},"D =",{"$f":"+B10","v":{"v":25.3246751321054,"d":"25.3"}}]
["R =",{"v":2,"d":"2.00"},{"$nulls":10},"xD =",{"$f":"+B6","v":{"v":0.75,"d":"0.750"}}]
["% V =",0.5]
["xD =",{"v":0.75,"d":"0.750"}]
["xB =",{"v":0.01,"d":"0.010"}]
[null,null,"V =",{"$f":"(1+B4)*B10","v":{"v":75.97402539631621,"d":"76.0"}}]
["B = ",{"v":100.64936492076983,"d":"100.6"},"L =",{"$f":"B4*B10","v":{"v":50.6493502642108,"d":"50.6"}},{"$nulls":3},"V =",{"$f":"+D8","v":{"v":75.97402539631621,"d":"76.0"}},{"$nulls":3},"L =",{"$f":"+D9","v":{"v":50.6493502642108,"d":"50.6"}}]
["D =",{"v":25.3246751321054,"d":"25.3"},"V' =",{"$f":"+B11","v":{"v":25.974039425093178,"d":"26.0"}}]
["S =",{"v":25.974039425093178,"d":"26.0"},"L ' =",{"$f":"+D9+B2*(1-B5)","v":{"v":100.6493502642108,"d":"100.6"}}]
[{"$nulls":5},"x","y","F =",{"$f":"+B2","v":{"v":100,"d":"100.0"}}]
["B MB:",{"$f":"B2*B3-B9*B7-B10*B6","v":{"v":1.7132499863237172E-9,"d":"0.00000000"}},"TOL","m =",{"$f":"+D9/D8","v":{"v":0.6666666666666666,"d":"0.667"}},{"$f":"+B6","v":{"v":0.75,"d":"0.750"}},{"$f":"+B6","v":{"v":0.75,"d":"0.750"}},"z =",0.2]
["T MB:",{"$f":"B2+B11-B9-B10","v":{"v":-6.2778204679148075E-7,"d":"-0.00000063"}},null,"b =",{"$f":"B6*B10/D8","v":{"v":0.25,"d":"0.250"}},{"v":0.09000000417792656,"d":"0.090"},{"v":0.31000000278528494,"d":"0.310"},"% V =",{"$f":"+B5","v":0.5}]
["PS:",{"$f":"+B11+B2*B5-(1+B4)*B10","v":{"v":1.4028776973873391E-5,"d":"0.00001403"}}]
["TOL:",{"$f":"+E13*F14+E14-G14","v":{"v":-5.551115123125783e-16,"d":"-0.00000000"}},"Feed","m =",{"$f":"-B5/(1-B5)","v":{"v":-1,"d":"-1.000"}},{"v":0,"d":"0.000"},{"$f":"+E16*F16+E17","v":{"v":0.4,"d":"0.400"}},"V' =",{"$f":"+D10","v":{"v":25.974039425093178,"d":"26.0"}},{"$nulls":3},"L' =",{"$f":"+D11","v":{"v":100.6493502642108,"d":"100.6"}}]
["Feed Line:",{"$f":"+(G14-B3)/(F14-B3)+B5/(1-B5)","v":{"v":-6.3301925035119666E-8,"d":"-0.00000006"}},null,"b =",{"$f":"+B3*(B5+(1-B5))/(1-B5)","v":{"v":0.4,"d":"0.400"}},{"$f":"+B3","v":{"v":0.2,"d":"0.200"}},{"$f":"+E16*F17+E17","v":{"v":0.2,"d":"0.200"}}]
[]
[null,null,"BOL","m =",{"$f":"+D11/D10","v":{"v":3.874997978442074,"d":"3.875"}},{"$f":"+B7","v":{"v":0.01,"d":"0.010"}},{"v":0,"d":"0.000"}]
[{"$nulls":3},"b =",{"$f":"-B7*B9/D10","v":{"v":-0.038749985427193046,"d":"-0.039"}},{"$f":"+F14","v":{"v":0.09000000417792656,"d":"0.090"}},{"$f":"+G14","v":{"v":0.31000000278528494,"d":"0.310"}}]
[]
["Instructions:",{"$nulls":6},"S =",{"$f":"+B11","v":{"v":25.974039425093178,"d":"26.0"}},{"$nulls":3},"B =",{"$f":"+B9","v":{"v":100.64936492076983,"d":"100.6"}}]
["1. Input F, z, R, %V, xD, xB",{"$nulls":11},"xB =",{"$f":"+B7","v":{"v":0.01,"d":"0.010"}}]
["2. Run Solver. It will find the operating lines."]
["3. The operating lines automatically generate on next page."]
["4. Print MT (Op Lines) for a graphical solution."]
["5. Lewis can be used to generate the steps. Experts only!"]

{"sheet":"Lewis","index":3,"n_rows":33,"n_cols":15,"rows_kept":33,"merged":[[2,3,2,5]]}
["Open Steam Distillation of Ethanol/Water"]
[{"$nulls":7},"P (mm Hg) =",760,null,"Antoine Constants"]
["x","y","T ","Wilson Equation",null,null,"pB","pT","BP",null,null,"A","B","C","D"]
["(mol B/mol)","(mol B/mol)","(oC)","F","gE","gW","(mm Hg)","(mm Hg)","(mm Hg)",null,"Ethanol",{"v":8.1122,"d":"8.112"},1592.864,226.184,{"v":0.20022,"d":"0.2002"}]
[{"$f":"+'Operating Lines'!B7","v":{"v":0.01,"d":"0.010"}},{"v":0,"d":"0.000"},{"v":100,"d":"100.0"},{"$f":"+$O$4/(A5+(1-A5)*$O$4)-$O$5/((1-A5)+A5*$O$5)","v":{"v":0.14444276766812958,"d":"0.1444"}},{"$f":"+EXP(-LN(A5+$O$4*(1-A5))+(1-A5)*D5)","v":{"v":5.540966653505429,"d":"5.541"}},{"$f":"+EXP(-LN((1-A5)+$O$5*A5)-A5*D5)","v":{"v":1.0004009542060621,"d":"1.000"}},{"$f":"10^($L$4-$M$4/(C5+$N$4))","v":{"v":1693.8320477388859,"d":"1694"}},{"$f":"10^($L$5-$M$5/($N$5+C5))","v":{"v":759.9830433084104,"d":"760"}},null,null,"Water",{"v":7.96681,"d":"7.967"},{"v":1668.21,"d":"1668.210"},{"v":228,"d":"228.000"},{"v":0.81564,"d":"0.8156"}]
[{"$f":"+A5","v":{"v":0.01,"d":"0.010"}},{"$f":"+A6*E6*G6/I2","v":{"v":0.11123682210949892,"d":"0.111"}},{"v":96.9958338176527,"d":"97.0"},{"$f":"+$O$4/(A6+(1-A6)*$O$4)-$O$5/((1-A6)+A6*$O$5)","v":{"v":0.14444276766812958,"d":"0.1444"}},{"$f":"+EXP(-LN(A6+$O$4*(1-A6))+(1-A6)*D6)","v":{"v":5.540966653505429,"d":"5.541"}},{"$f":"+EXP(-LN((1-A6)+$O$5*A6)-A6*D6)","v":{"v":1.0004009542060621,"d":"1.000"}},{"$f":"10^($L$4-$M$4/(C6+$N$4))","v":{"v":1525.7262873028828,"d":"1526"}},{"$f":"10^($L$5-$M$5/($N$5+C6))","v":{"v":682.0093890999786,"d":"682"}},{"$f":"$I$2-A6*G6*E6-(1-A6)*H6*F6","v":{"v":0,"d":"0.00000"}}]
[{"$f":"+(B7-$C$29)/$C$28","v":{"v":0.038706293105472404,"d":"0.039"}},{"$f":"+B6","v":{"v":0.11123682210949892,"d":"0.111"}},{"v":97,"d":"97.0"},{"$f":"+$O$4/(A7+(1-A7)*$O$4)-$O$5/((1-A7)+A7*$O$5)","v":{"v":0.04458927051929662,"d":"0.0446"}},{"$f":"+EXP(-LN(A7+$O$4*(1-A7))+(1-A7)*D7)","v":{"v":4.515144060617386,"d":"4.515"}},{"$f":"+EXP(-LN((1-A7)+$O$5*A7)-A7*D7)","v":{"v":1.00545038869271,"d":"1.005"}},{"$f":"10^($L$4-$M$4/(C7+$N$4))","v":{"v":1525.949514420983,"d":"1526"}},{"$f":"10^($L$5-$M$5/($N$5+C7))","v":{"v":682.1127287015477,"d":"682"}}]
[{"$f":"+A7","v":{"v":0.038706293105472404,"d":"0.039"}},{"$f":"+A8*G8*E8/760","v":{"v":0.2894095097028575,"d":"0.289"}},{"v":91.60533471126071,"d":"91.6"},{"v":0.04458927051929662,"d":"0.0446"},{"v":4.515144060617386,"d":"4.515"},{"v":1.00545038869271,"d":"1.005"},{"v":1258.5578918205406,"d":"1259"},{"v":558.7483755880517,"d":"559"},{"$f":"$I$2-A8*G8*E8-(1-A8)*H8*F8","v":{"v":-4.4409325596461713E-5,"d":"-0.00004"}},null,"Equilibrium Calculations/Leaving Streams"]
[{"$f":"+(B9-$C$29)/$C$28","v":{"v":0.08468636550411457,"d":"0.085"}},{"$f":"+B8","v":{"v":0.2894095097028575,"d":"0.289"}},{"v":91.432591527382,"d":"91.4"},{"v":-0.0813487054316776,"d":"-0.0813"},{"v":3.4642410720921277,"d":"3.464"},{"v":1.0228829556776189,"d":"1.023"},{"v":1250.682653925302,"d":"1251"},{"v":555.1286154533586,"d":"555"},null,null,"Operating Line Calculations/Passing Streams"]
[{"$f":"+A9","v":{"v":0.08468636550411457,"d":"0.085"}},{"v":0.41511498589502577,"d":"0.415"},{"v":87.33243226505975,"d":"87.3"},{"v":-0.0813487054316776,"d":"-0.0813"},{"v":3.4642410720921277,"d":"3.464"},{"v":1.0228829556776189,"d":"1.023"},{"v":1075.376157185538,"d":"1075"},{"v":474.7755318379294,"d":"475"},{"v":-1.1902401388397266E-4,"d":"-0.00012"}]
[{"$f":"+(B11-$C$23)/$C$22","v":{"v":0.24767247884253865,"d":"0.248"}},{"$f":"+B10","v":{"v":0.41511498589502577,"d":"0.415"}},{"v":89.22567785449633,"d":"89.2"},{"v":-0.35198275444921956,"d":"-0.3520"},{"v":1.9265574403940324,"d":"1.927"},{"v":1.1432929593624572,"d":"1.143"},{"v":1153.6044596291158,"d":"1154"},{"v":510.57751057705303,"d":"511"}]
[{"$f":"+A11","v":{"v":0.24767247884253865,"d":"0.248"}},{"v":0.5584849283996717,"d":"0.558"},{"v":82.32913305714042,"d":"82.3"},{"v":-0.35198275444921956,"d":"-0.3520"},{"v":1.9265574403940324,"d":"1.927"},{"v":1.1432929593624572,"d":"1.143"},{"v":889.5397031688108,"d":"890"},{"v":390.1169453847379,"d":"390"},{"v":-1.2955501330225161E-4,"d":"-0.00013"}]
[{"$f":"+(B13-$C$23)/$C$22","v":{"v":0.4627273925995075,"d":"0.463"}},{"$f":"+B12","v":{"v":0.5584849283996717,"d":"0.558"}},{"v":87.64092594918965,"d":"87.6"},{"v":-0.5406320982761667,"d":"-0.5406"},{"v":1.3114399391625995,"d":"1.311"},{"v":1.4040116805547849,"d":"1.404"},{"v":1087.8142238637186,"d":"1088"},{"v":480.4617942171899,"d":"480"}]
[{"$f":"+A13","v":{"v":0.4627273925995075,"d":"0.463"}},{"v":0.6479183493958407,"d":"0.648"},{"v":79.9629243368795,"d":"80.0"},{"v":-0.5406320982761667,"d":"-0.5406"},{"v":1.3114399391625995,"d":"1.311"},{"v":1.4040116805547849,"d":"1.404"},{"v":811.4471821347806,"d":"811"},{"v":354.7249219525376,"d":"355"},{"v":-8.4820738038615673E-5,"d":"-0.00008"}]
[{"$f":"+(B15-$C$23)/$C$22","v":{"v":0.596877524093761,"d":"0.597"}},{"$f":"+B14","v":{"v":0.6479183493958407,"d":"0.648"}},{"v":86.44949124980008,"d":"86.4"},{"v":-0.621002865051248,"d":"-0.6210"},{"v":1.1489766067128526,"d":"1.149"},{"v":1.6278201622936763,"d":"1.628"},{"v":1040.4270535920741,"d":"1040"},{"v":458.8108330163137,"d":"459"}]
[{"$f":"+A15","v":{"v":0.596877524093761,"d":"0.597"}},{"v":0.7053458522489616,"d":"0.705"},{"v":79.0102614528862,"d":"79.0"},{"v":-0.621002865051248,"d":"-0.6210"},{"v":1.1489766067128526,"d":"1.149"},{"v":1.6278201622936763,"d":"1.628"},{"v":781.6625356592859,"d":"782"},{"v":341.25798896694414,"d":"341"},{"v":-5.7786378647506353E-5,"d":"-0.00006"}]
[{"$f":"+(B17-$C$23)/$C$22","v":{"v":0.6830187783734425,"d":"0.683"}},{"$f":"+B16","v":{"v":0.7053458522489616,"d":"0.705"}},{"v":85.52045185847287,"d":"85.5"},{"v":-0.6649254332793366,"d":"-0.6649"},{"v":1.0850338701899045,"d":"1.085"},{"v":1.8017194641423468,"d":"1.802"},{"v":1004.6758285422319,"d":"1005"},{"v":442.49982289518994,"d":"442"}]
[{"$f":"+A17","v":{"v":0.6830187783734425,"d":"0.683"}},{"v":0.7483769427738194,"d":"0.748"},{"v":78.54543259074613,"d":"78.5"},{"v":-0.6649254332793366,"d":"-0.6649"},{"v":1.0850338701899045,"d":"1.085"},{"v":1.8017194641423468,"d":"1.802"},{"v":767.4640685094894,"d":"767"},{"v":334.84469141454605,"d":"335"},{"v":-4.2348465683517134E-5,"d":"-0.00004"}]
[{"$f":"+(B19-$C$23)/$C$22","v":{"v":0.7475654141607291,"d":"0.748"}},{"$f":"+B18","v":{"v":0.7483769427738194,"d":"0.748"}},{"v":84.77373952274525,"d":"84.8"},{"v":-0.6951534797234218,"d":"-0.6952"},{"v":1.0513034111775579,"d":"1.051"},{"v":1.9502649936650127,"d":"1.950"},{"v":976.685491497952,"d":"977"},{"v":429.7442304229587,"d":"430"}]
[]
[{"$nulls":3},"x","y","Instructions:","1) Select the pressure. Most examples are for 1 atm = 760 mm Hg."]
["TOL","m =",{"$f":"+'Operating Lines'!E13","v":{"v":0.6666666666666666,"d":"0.667"}},{"$f":"+'Operating Lines'!F13","v":{"v":0.75,"d":"0.750"}},{"$f":"+'Operating Lines'!G13","v":{"v":0.75,"d":"0.750"}},null,"2) Start with page \"Operating Lines\".  Input all relevant data and run Solver "]
[null,"b =",{"$f":"+'Operating Lines'!E14","v":{"v":0.25,"d":"0.250"}},{"$f":"+'Operating Lines'!F14","v":{"v":0.09000000417792656,"d":"0.090"}},{"$f":"+'Operating Lines'!G14","v":{"v":0.31000000278528494,"d":"0.310"}},null,"to complete the overall mole balances. All flow rates are auto copied to this page."]
[{"$nulls":6},"3) The following are set and don't need to be changed:"]
["Feed","m =",{"$f":"+'Operating Lines'!E16","v":{"v":-1,"d":"-1.000"}},{"$f":"+'Operating Lines'!F16","v":{"v":0,"d":"0.000"}},{"$f":"+'Operating Lines'!G16","v":{"v":0.4,"d":"0.400"}},null,"    x is set to xB (Copied from page Operating Lines)."]
[null,"b =",{"$f":"+'Operating Lines'!E17","v":{"v":0.4,"d":"0.400"}},{"$f":"+'Operating Lines'!F17","v":{"v":0.2,"d":"0.200"}},{"$f":"+'Operating Lines'!G17","v":{"v":0.2,"d":"0.200"}},null,"    yE = pE xEgE/P"]
[{"$nulls":6},"    T is found by iteration of BP"]
["BOL","m =",{"$f":"+'Operating Lines'!E19","v":{"v":3.874997978442074,"d":"3.875"}},{"$f":"+'Operating Lines'!F19","v":{"v":0.01,"d":"0.010"}},{"$f":"+'Operating Lines'!G19","v":{"v":0,"d":"0.000"}},null,"    pB and pT are the partial pressures at T using Antoine's Eq."]
[null,"b =",{"$f":"+'Operating Lines'!E20","v":{"v":-0.038749985427193046,"d":"-0.039"}},{"$f":"+'Operating Lines'!F20","v":{"v":0.09000000417792656,"d":"0.090"}},{"$f":"+'Operating Lines'!G20","v":{"v":0.31000000278528494,"d":"0.310"}},null,"4) Run Solver on this page to make the BP criteria equal to zero. The cell contains"]
[{"$nulls":6},"    P - pE xE gE - pW (1-xE) gW."]
[{"$nulls":6},"5) Check graph on page MT (McCabe-Thiele) to see if correct feed location chosen."]
[{"$nulls":6},"  If not correct, copy correct BOL/TOL to the x value. "]
[{"$nulls":6},"6) If you change pressure, you will need to adjust T axis on TXY VLE."]

{"sheet":"Lewis DIY","index":4,"n_rows":29,"n_cols":15,"rows_kept":29,"merged":[[2,3,2,5]]}
["Open Steam Distillation of Ethanol/Water"]
[{"$nulls":7},"P (mm Hg) =",760,null,"Antoine Constants"]
["x","y","T ","Wilson Equation",null,null,"pB","pT","BP",null,null,"A","B","C","D"]
["(mol B/mol)","(mol B/mol)","(oC)","F","gE","gW","(mm Hg)","(mm Hg)","(mm Hg)",null,"Ethanol",{"v":8.1122,"d":"8.112"},1592.864,226.184,{"v":0.20022,"d":"0.2002"}]
[{"$nulls":10},"Water",{"v":7.96681,"d":"7.967"},{"v":1668.21,"d":"1668.210"},{"v":228,"d":"228.000"},{"v":0.81564,"d":"0.8156"}]
[]
[]
[{"$nulls":10},"Equilibrium Calculations/Leaving Streams"]
[{"$nulls":10},"Operating Line Calculations/Passing Streams"]
{"$rows_empty":11}
[{"$nulls":3},"x","y"]
["TOL","m =",{"$f":"+'Operating Lines'!E13","v":{"v":0.6666666666666666,"d":"0.667"}},{"$f":"+'Operating Lines'!F13","v":{"v":0.75,"d":"0.750"}},{"$f":"+'Operating Lines'!G13","v":{"v":0.75,"d":"0.750"}}]
[null,"b =",{"$f":"+'Operating Lines'!E14","v":{"v":0.25,"d":"0.250"}},{"$f":"+'Operating Lines'!F14","v":{"v":0.09000000417792656,"d":"0.090"}},{"$f":"+'Operating Lines'!G14","v":{"v":0.31000000278528494,"d":"0.310"}}]
[]
["Feed","m =",{"$f":"+'Operating Lines'!E16","v":{"v":-1,"d":"-1.000"}},{"$f":"+'Operating Lines'!F16","v":{"v":0,"d":"0.000"}},{"$f":"+'Operating Lines'!G16","v":{"v":0.4,"d":"0.400"}}]
[null,"b =",{"$f":"+'Operating Lines'!E17","v":{"v":0.4,"d":"0.400"}},{"$f":"+'Operating Lines'!F17","v":{"v":0.2,"d":"0.200"}},{"$f":"+'Operating Lines'!G17","v":{"v":0.2,"d":"0.200"}}]
[]
["BOL","m =",{"$f":"+'Operating Lines'!E19","v":{"v":3.874997978442074,"d":"3.875"}},{"$f":"+'Operating Lines'!F19","v":{"v":0.01,"d":"0.010"}},{"$f":"+'Operating Lines'!G19","v":{"v":0,"d":"0.000"}}]
[null,"b =",{"$f":"+'Operating Lines'!E20","v":{"v":-0.038749985427193046,"d":"-0.039"}},{"$f":"+'Operating Lines'!F20","v":{"v":0.09000000417792656,"d":"0.090"}},{"$f":"+'Operating Lines'!G20","v":{"v":0.31000000278528494,"d":"0.310"}}]

{"sheet":"VLE","index":5,"n_rows":105,"n_cols":15,"rows_kept":105,"merged":[[2,3,2,5],[18,10,18,11]]}
["Ethanol-Water VLE"]
[{"$nulls":7},"P (mm Hg) =",760,null,"Antoine Constants"]
["x","y","T ","Wilson Equation",null,null,"pB","pT","BP",null,null,"A","B","C","D"]
["(mol B/mol)","(mol B/mol)","(oC)","F","gE","gW","(mm Hg)","(mm Hg)","(mm Hg)",null,"Ethanol",{"v":8.1122,"d":"8.112"},1592.864,226.184,{"v":0.20022,"d":"0.2002"}]
[{"v":0,"d":"0.00"},{"$f":"+A5*G5*E5/760","v":{"v":0,"d":"0.000"}},{"v":100.00062490569105,"d":"100.0"},{"$f":"+$O$4/(A5+(1-A5)*$O$4)-$O$5/((1-A5)+A5*$O$5)","v":{"v":0.18435999999999997,"d":"0.1844"}},{"$f":"+EXP(-LN(A5+$O$4*(1-A5))+(1-A5)*D5)","v":{"v":6.005636932836824,"d":"6.006"}},{"$f":"+EXP(-LN((1-A5)+$O$5*A5)-A5*D5)","v":{"v":1,"d":"1.000"}},{"$f":"10^($L$4-$M$4/(C5+$N$4))","v":{"v":1693.8685363849156,"d":"1694"}},{"$f":"10^($L$5-$M$5/($N$5+C5))","v":{"v":760.0000000000008,"d":"760"}},{"$f":"$I$2-A5*G5*E5-(1-A5)*H5*F5","v":{"v":0,"d":"0.00000"}},null,"Water",{"v":7.96681,"d":"7.967"},{"v":1668.21,"d":"1668.210"},{"v":228,"d":"228.000"},{"v":0.81564,"d":"0.8156"}]
[0.01,{"$f":"+A6*G6*E6/760","v":{"v":0.11123682210949863,"d":"0.111"}},{"v":96.99583381765267,"d":"97.0"},{"$f":"+$O$4/(A6+(1-A6)*$O$4)-$O$5/((1-A6)+A6*$O$5)","v":{"v":0.14444276766812958,"d":"0.1444"}},{"$f":"+EXP(-LN(A6+$O$4*(1-A6))+(1-A6)*D6)","v":{"v":5.540966653505429,"d":"5.541"}},{"$f":"+EXP(-LN((1-A6)+$O$5*A6)-A6*D6)","v":{"v":1.0004009542060621,"d":"1.000"}},{"$f":"10^($L$4-$M$4/(C6+$N$4))","v":{"v":1525.7262873028787,"d":"1526"}},{"$f":"10^($L$5-$M$5/($N$5+C6))","v":{"v":682.0093890999786,"d":"682"}},{"$f":"$I$2-A6*G6*E6-(1-A6)*H6*F6","v":{"v":0,"d":"0.00000"}}]
[0.02,{"v":0.1902167586069709,"d":"0.190"},{"v":94.70079982609741,"d":"94.7"},{"v":0.10736158132294937,"d":"0.1074"},{"v":5.138152456880939,"d":"5.138"},{"$f":"+EXP(-LN((1-A7)+$O$5*A7)-A7*D7)","v":{"v":1.0015479797371363,"d":"1.002"}},{"$f":"10^($L$4-$M$4/(C7+$N$4))","v":{"v":1406.777414201664,"d":"1407"}},{"$f":"10^($L$5-$M$5/($N$5+C7))","v":{"v":627.024545503468,"d":"627"}},{"v":0,"d":"0.00000"},null,"Instructions:","1) Select the pressure. Most examples are for 1 atm = 760 mm Hg."]
[0.03,{"v":0.2491213958176398,"d":"0.249"},{"v":92.8924046555087,"d":"92.9"},{"v":0.07281232395699855,"d":"0.0728"},{"v":4.786430600560518,"d":"4.786"},{"v":1.0033674389117961,"d":"1.003"},{"v":1318.5348096292214,"d":"1319"},{"v":586.3427833807414,"d":"586"},{"v":0,"d":"0.00000"},null,null,"2) Run Solver to make the BP criteria equal to zero. The cell contains"]
[0.04,{"v":0.294719855418708,"d":"0.295"},{"v":91.432591527382,"d":"91.4"},{"v":0.040532771557451386,"d":"0.0405"},{"v":4.477296647059676,"d":"4.477"},{"v":1.005797153279279,"d":"1.006"},{"v":1250.682653925302,"d":"1251"},{"v":555.1286154533586,"d":"555"},{"v":0,"d":"0.00000"},null,null,"    P - pE xE gE - pW (1-xE) gW."]
[0.05,{"v":0.33106756982985003,"d":"0.331"},{"v":90.23096009556981,"d":"90.2"},{"v":0.010295618893289227,"d":"0.0103"},{"v":4.203959163366706,"d":"4.204"},{"v":1.0087843254442581,"d":"1.009"},{"v":1197.0209190575729,"d":"1197"},{"v":530.4859826211587,"d":"530"},{"v":0,"d":"0.00000"},null,null,"3) The following are set and don't need to be changed:"]
[0.06,{"v":0.3607389090593249,"d":"0.361"},{"v":89.22567785449633,"d":"89.2"},{"v":-0.018097146345880777,"d":"-0.0181"},{"v":3.9609412711706224,"d":"3.961"},{"v":1.0122838980731774,"d":"1.012"},{"v":1153.6044596291158,"d":"1154"},{"v":510.57751057705303,"d":"511"},{"v":1.1937117960769683E-12,"d":"0.00000"},null,null,"    x is set from 0 to 1 by 0.01."]
[0.07,{"v":0.38544484805856216,"d":"0.385"},{"v":88.37296231640552,"d":"88.4"},{"v":-0.04481881569469981,"d":"-0.0448"},{"v":3.743786140390644,"d":"3.744"},{"v":1.0162572466480417,"d":"1.016"},{"v":1117.8068463293332,"d":"1118"},{"v":494.1830575584968,"d":"494"},{"v":0,"d":"0.00000"},null,null,"    yE = pE xEgE/P"]
[0.08,{"v":0.40636578469588225,"d":"0.406"},{"v":87.64092594918965,"d":"87.6"},{"v":-0.07002170162355925,"d":"-0.0700"},{"v":3.5488366211090487,"d":"3.549"},{"v":1.0206711295468174,"d":"1.021"},{"v":1087.8142238637186,"d":"1088"},{"v":480.4617942171899,"d":"480"},{"v":0,"d":"0.00000"},null,null,"    T is found by iteration of BP"]
[0.09,{"v":0.42434167652965743,"d":"0.424"},{"v":87.00579491573804,"d":"87.0"},{"v":-0.09384021961558131,"d":"-0.0938"},{"v":3.3730684661237342,"d":"3.373"},{"v":1.0254968383675127,"d":"1.025"},{"v":1062.3353035685639,"d":"1062"},{"v":468.8162565159245,"d":"469"},{"v":5.684341886080801e-13,"d":"0.00000"},null,null,"    pB and pT are the partial pressures at T using Antoine's Eq."]
[{"v":0.1,"d":"0.10"},{"v":0.4399860288127337,"d":"0.440"},{"v":86.44949124980008,"d":"86.4"},{"v":-0.1163934424065114,"d":"-0.1164"},{"v":3.2139627736821947,"d":"3.214"},{"v":1.0307095054216882,"d":"1.031"},{"v":1040.4270535920741,"d":"1040"},{"v":458.8108330163137,"d":"459"},{"v":6.821210263296962e-13,"d":"0.00000"},null,null,"4) If you change pressure, you will need to adjust T axis on TXY VLE."]
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[{"v":0.3,"d":"0.30"},{"v":0.5825342798832291,"d":"0.583"},{"v":81.59242707612685,"d":"81.6"},{"v":-0.4085062687554572,"d":"-0.4085"},{"v":1.7068955029876778,"d":"1.707"},{"v":1.1965569341748103,"d":"1.197"},{"v":864.5833950903364,"d":"865"},{"v":378.79392378379094,"d":"379"},{"v":0,"d":"0.00000"}]
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