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PRELIMINARY DESIGN OF ACETONE PLANT (PROGRESS REPORT II) philia eastward Technical University chemical substance Engineering Department ChE 418 Chemical Engineering approach pattern II Submitted By: host I Rizka Mulyawan Serdar Ar?can Shabrina Virta Inmas Submitted To: Prof. Dr. Hayrettin Yücel Merve Ç?nar ABSTRACT separation run is the heart of the acetone production plant. It makes sure zip fastener goes to waste and to take care the quality of the product. The separation attend preliminary design was aimed to produce 20000 mensural ton of 99 wt% of acetone. Three separation towers were used in aim to guard optimum result, acetone stripper tugboat, acetone column and IPA column. early(a) than acetone solution, there are two other products from the process, conglomeration heat solution and sewer water. The amount of acetone that is contained in hydrogen and wastewater were minimized, so that most of the acetone that is produced could be converted to a precious good. i TABLE OF confine Chapter 1 Introduction Page 1 1.1. Description of musical interval Process 1 1.2. Design Basis 2 1.3. specify Flow Diagram 3 Chapter 2 Equipment Design 4 2.1. Reactor Effluent armoured combat vehicle (E 1102) 4 2.2. clothe Cooler (E 1103) 5 2.3. Phase Separator (V 1102) 5 2.4. dimethyl ketone Stripper (T 1101) 6 2.5. dimethyl ketone column (T 1102) 6 2.6.

Acetone viewgraph condenser (E 1104) 6 2.7. Acetone ebb Drum (V 1103) 7 2.8. Acetone reflux Pump (P 1103 A/B) 7 2.9. A cetone Reboiler (E 1105) 7 2.10. IPA ! Column Pump (P 1104 A/B) 8 2.11. IPA Column (T 1103) 8 2.12. IPA Overhead Condenser (E 1106) 9 2.13. IPA wane Drum (V 1104) 9 2.14. IPA Reflux Pump (P 1105 A/B) 10 2.15. IPA Reboiler (E 1107) 10 2.16. neutralise irrigate Cooler (E 1108) 11 Chapter 3 Flow Table 12 Chapter 4 Discussion 14 Chapter 5 Conclusion 16 References 17 Appendix Sample...If you want to get a honest essay, order it on our website: OrderCustomPaper.com

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