31_Yusuf Arya Yudanto.xlsx - Nama Yusuf Arya Yudanto NIM 40040117640031 2017 A S1 T Teknologi Rekayasa Kimia Industri Dosen Wali Fahmi Arifan ST M Eng

# 31_Yusuf Arya Yudanto.xlsx - Nama Yusuf Arya Yudanto NIM...

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Nama : Yusuf Arya NIM : 40040117640031 S1 T. Teknologi Rekayasa Kimia Dosen Wali : Fahmi Arifan, ST Mata Kuliah / SKS : Separasi Perpindahan M Dosen Pengampu : M. Endy Yulianto 1. Buat diagram kesetimbangan fasa asam asetat, air, dan isopropil-eter! Appendix A.3-24 Geankoplis (Transport Processes and Unit Operation 3rd Editi Water Layer (wt %) Isopropyl Ether Layer (wt %) Water Water 0.00 98.80 1.20 0.00 0.60 99.40 0.69 98.10 1.20 0.18 0.50 99.30 1.41 97.10 1.50 0.37 0.70 98.90 2.89 95.50 1.60 0.79 0.80 98.40 6.42 91.70 1.90 1.93 1.00 97.10 13.30 84.40 2.30 4.82 1.90 93.30 25.50 71.10 3.40 11.40 3.90 84.70 36.70 58.90 4.40 21.60 6.90 71.50 44.30 45.10 10.60 31.10 10.80 58.10 46.40 37.10 16.50 36.20 15.10 48.70 A = DILUENT C = SOLUTE B = SOLVENT Diagram dalam koordinat X, Y VS N Lapisan Air (Fasa Rafinat) Lapisan Isopropil (Fas % Berat B % Berat C 0.00 98.80 1.20 0 0.01215 0.00 0.60 99.40 0.69 98.10 1.20 0.00698 0.01215 0.18 0.50 99.30 1.41 97.10 1.50 0.01431 0.01523 0.37 0.70 98.90 2.89 95.50 1.60 0.02937 0.01626 0.79 0.80 98.40 6.42 91.70 1.90 0.06543 0.01936 1.93 1.00 97.10 13.30 84.40 2.30 0.13613 0.02354 4.82 1.90 93.30 25.50 71.10 3.40 0.26398 0.0352 11.40 3.90 84.70 36.70 58.90 4.40 0.38389 0.04603 21.60 6.90 71.50 44.30 45.10 10.60 0.49553 0.11857 31.10 10.80 58.10 46.40 37.10 16.50 0.55569 0.1976 36.20 15.10 48.70 A.3-24. Acetic Acid-Water-Isopropyl Ether System, Liquid-Liquid Equilibria at 29 Acetic Acid Isopropyl Ether Acetic Acid Isopropyl Ether % Berat C % Berat A X = C/ (A+C) N = B/ (A+C) % Berat A % Berat B 80.00 85.00 90.00 95.00 100.00
0.00 5.00 10.00 15.00 20.00 25.00 30.00 0.00 5.00 10.00 15.00 20.00 25.00 30.00 35.00 40.00 45.00 50.00 55.00 60.00 65.00 70.00 75.00 80.00 Fasa Ekstrak Fasa Rafinat % Berat C % Berat B 0 5 10 15 20 25 30 0 10 20 30 40 50 60 70 80 90 100 % Berat C (Rafinat) % Berat C (Ekstrak)
a Yudanto 1 / 2017 A a Industri T, M. Eng.

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• Spring '17
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• Unit Operation, equilibrium stages

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