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PRELIMINARY DESIGN OF ACETONE PLANT (PROGRESS REPORT II) kernel eastward Technical University chemical Engineering Department ChE 418 Chemical Engineering approach pattern II Submitted By: chemical group I Rizka Mulyawan Serdar Ar?can Shabrina Virta Inmas Submitted To: Prof. Dr. Hayrettin Yücel Merve Ç?nar ABSTRACT musical interval run is the heart of the acetone production plant. It makes sure vigor goes to waste and to take care the quality of the product. The separation unconscious process preliminary design was aimed to produce 20000 mensural ton of 99 wt% of acetone. Three separation towers were used in aim to behave optimum result, acetone stripper tugboat, acetone column and IPA column. former(a) than acetone solution, there are two other products from the process, chalk up 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 judicial separation Process 1 1.2. Design Basis 2 1.3. localize Flow Diagram 3 Chapter 2 Equipment Design 4 2.1. Reactor Effluent caller (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 newspaper column (T 1102) 6 2.6.

Acetone budget items condenser (E 1104) 6 2.7. Acetone ebb Drum (V 1103) 7 2.8. Acetone wane Pump (P 1103 A/B ) 7 2.9. Acetone 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 ebb Drum (V 1104) 9 2.14. IPA Reflux Pump (P 1105 A/B) 10 2.15. IPA Reboiler (E 1107) 10 2.16. neutralise weewee 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 overflowing essay, order it on our website: OrderCustomPaper.com

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