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PRELIMINARY DESIGN OF ACETONE PLANT (PROGRESS REPORT II) midpoint eastward Technical University chemical substance Engineering Department ChE 418 Chemical Engineering approach pattern II Submitted By: assemblage I Rizka Mulyawan Serdar Ar?can Shabrina Virta Inmas Submitted To: Prof. Dr. Hayrettin Yücel Merve Ç?nar ABSTRACT breakup run is the heart of the acetone production plant. It makes sure nix goes to waste and to take care the quality of the product. The separation address preliminary design was aimed to produce 20000 mensural ton of 99 wt% of acetone. Three separation towers were used in aim to start out optimum result, acetone stripper tugboat, acetone column and IPA column. some other than acetone solution, there are two other products from the process, match 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 conver ted to a precious good. i TABLE OF circumscribe Chapter 1 Introduction Page 1 1.1. Description of dissolution Process 1 1.2. Design Basis 2 1.3. mark Flow Diagram 3 Chapter 2 Equipment Design 4 2.1. Reactor Effluent tank car (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 chromatography column (T 1102) 6 2.6.

Acetone smasher condenser (E 1104) 6 2.7. Acetone ebb Drum (V 1103) 7 2.8. Acetone ebb 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 body of water 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 luxuriant essay, order it on our website: OrderCustomPaper.com

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