PRAKTIKUM EVALUASI PERALATANG KILANG Heat Exchanger
KELOMPOK A3
1. Nethania Deva
2. M. kharis firismanda su'udi 3. wisnu aji thiananda
4. pandu daffa akmali 5. Ahmad Zahro Ilmi A. Input Material Stream
Gambar A.1 Input material hidrokarbon
Gambar A.2 Input material water B. Output Material Stream
Gambar B.1 Input material hidrokarbon
Gambar B.2 Input material water C. Evaluasi Peralatan
Gambar C.1 Evaluasi peralatan heat exchanger study cae D. Overall Flowsheet & Grafik
Gambar D.1 Overall flowsheet study case
Gambar D.2 Overall worksheet study case heat exchanger
Gambar D.3 Overall performance study case heat exchanger co-current
Gambar D.4 Overall performance study case heat exchanger counter-current
Gambar D.5 Graphic plot side hidrokarbo and water
Kesimpulana:
1.didapatkan suhu output fluida proses pada he, hidrokarbonout sebesar 135,6 F dan pada waterout 140 f
2.Pada hasil sizing HE ditemukan performa HE dengan LMTD sebesar 0,3751 F sedangkan uncorrected LMTTD sebesar 0,375
