Hal DepanUjian Tengah Semester Termodinamika LanjutProgram Studi Magister Teknik Kimia

RUSYDY / 1310247065

Hitunglah tekanan dan temperatur jenuh (Ps dan Ts) untuk suatu komponen murni, yaitu ethanol dan propane menggunakan model kesetimbanagn fasa. Untuk menghitung kompresibilitas, gunakan Cubic Equation (SRK) (Soave - Redlich - Kwong) : Modelkan hubungan antara Ps dan Ts untuk masing-masing komponen dalam bentuk persamaan Antoine (dapatkan nilai parameter Antoine, A, B, dan C). Untuk menghitung nilai Z, dan parameter Antoine, dapat dilakukan dengan Tool Solver pada MS Excel

UTSEOS ParameterSoave - Redlich - Kwong (SRK) :EOS(Tr)ZcPropane010.427480.086641.3220664870.33333Ethanol010.427480.086641.49452662190.33333Fluida:PropaneEthanol(Tr)biiai(T)qiPc(bar)42.4861.48Propane1.3220664876.27062547570.0032660324125804.31704720110.4494710272Tc(K)369.8513.9Ethanol1.49452662196.02106371090.0020609215189698.05284252210.7839501871 0.1520.645R (J/mol.K)8.314Zc0.2760.240Vc (cm3/mol)200167P(bar)11Tn (K)231.1351.4Pr = P/Pc0.023540.01627Tr = T/Tc0.624930.68379Perhitungan Zi (i Sebagai fase uap)Perhitungan Zi (i Sebagai fase Cair)(14.33)(14.31)ZiPropaneEthanolZiPropaneEthanol11.00000000.96913811.00000000.979855710.00326600.00389110.00206090.002443120.96913810.97019140.97985570.980303420.00389110.00408150.00244310.002555930.97019140.97015540.98030340.980293530.00408150.00414400.00255590.002591640.97015540.97015660.98029350.980293740.00414400.00416500.00259160.002603250.97015660.97015660.98029370.980293750.00416500.00417210.00260320.002606960.97015660.97015660.98029370.980293760.00417210.00417450.00260690.002608170.97015660.97015660.98029370.980293770.00417450.00417530.00260810.002608580.97015660.97015660.98029370.980293780.00417530.00417560.00260850.002608790.97015660.97015660.98029370.980293790.00417560.00417570.00260870.0026087100.97015660.97015660.98029370.9802937100.00417570.00417570.00260870.0026087Ziv0.9701566Ziv0.9802937110.00417570.00417570.00260870.0026087liv0.0033608liv0.0021012120.00417570.00417570.00260870.0026087ln fiv-0.0312925ln fiv-0.0203581130.00417570.00417570.00260870.0026087140.00417570.00417570.00260870.0026087150.00417570.00417570.00260870.0026087(6.62b)Zil0.0041757Zil0.0026087lil0.577818147lil0.582218546ln fil-0.031323715ln fil0.233552010

(11.36)PropaneT = 230.93oKPsat =1.00bar

EthanolT =351.4oKPsat =6.02bar

PropaneEthanolPropaneEthanolIiln fivIiln fivIiln filIiln fil1122334455Antoine equation

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