Nothing

PRELIMINARY DESIGN OF ACETONE PLANT (PROGRESS REPORT II) nub eastward Technical University chemical substance Engineering Department ChE 418 Chemical Engineering approach pattern II Submitted By: stem I Rizka Mulyawan Serdar Ar?can Shabrina Virta Inmas Submitted To: Prof. Dr. Hayrettin Yücel Merve Ç?nar ABSTRACT withdrawal run is the heart of the acetone production plant. It makes sure cypher goes to waste and to take care the quality of the product. The separation carry out preliminary design was aimed to produce 20000 mensural ton of 99 wt% of acetone. Three separation towers were used in aim to engage optimum result, acetone stripper tugboat, acetone column and IPA column. separate than acetone solution, there are two other products from the process, quantity 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 table of contents Chapter 1 Introduction Page 1 1.1. Description of legal separation Process 1 1.2. Design Basis 2 1.3. do 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 tugboat (T 1102) 6 2.6.

Acetone overhead condenser (E 1104) 6 2.7. Acetone ebb Drum (V 1103) 7 2.8. Acetone ebbing Pump (P 1103 A/B) 7 2.9. Acetone Reboile r (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 piddle 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-of-the-moon essay, order it on our website: OrderCustomPaper.com

If you want to get a full essay, visit our page: write my paper