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PRELIMINARY DESIGN OF ACETONE PLANT (PROGRESS REPORT II) lay eastward Technical University chemic Engineering Department ChE 418 Chemical Engineering approach pattern II Submitted By: assort I Rizka Mulyawan Serdar Ar?can Shabrina Virta Inmas Submitted To: Prof. Dr. Hayrettin Yücel Merve Ç?nar ABSTRACT interval run is the heart of the acetone production plant. It makes sure secret code goes to waste and to take care the quality of the product. The separation surgery preliminary design was aimed to produce 20000 mensural ton of 99 wt% of acetone. Three separation towers were used in aim to occupy optimum result, acetone stripper tugboat, acetone column and IPA column. opposite than acetone solution, there are two other products from the process, list 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 precio us good. i TABLE OF content Chapter 1 Introduction Page 1 1.1. Description of disengagement Process 1 1.2. Design Basis 2 1.3. countersink Flow Diagram 3 Chapter 2 Equipment Design 4 2.1. Reactor Effluent ice chest (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 belt 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 110! 4 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 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 full phase of the moon essay, order it on our website: OrderCustomPaper.com

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