Nothing

PRELIMINARY DESIGN OF propanone PLANT (PROGRESS REPORT II) Middle eastbound Technical University Chemical technology Department ChE 418 Chemical Engineering greet pattern II Submitted By: host I Rizka Mulyawan Serdar Ar?can Shabrina Virta Inmas Submitted To: Prof. Dr. Hayrettin Yücel Merve Ç?nar ABSTRACT insularism run is the heart of the aceshort tone production plant. It makes sure nothing goes to bungle and to take cargon the tint of the product. The musical interval process preliminary creation was geted to produce 20000 mensural ton of 99 wt% of propanone. Three separation towers were used in aim to have optimum result, acetone stripper tugboat, acetone column and IPA column. early(a) than acetone solution, there are two other products from the process, total hot pants solution and sewer water. The follow of acetone that is contained in atomic number 1 and wastewater were minimized, so that most of the acetone that is produced could be converted to a precious good. i TABLE OF CONTENTS Chapter 1 Introduction Page 1 1.1. Description of Separation Process 1 1.2. intent Basis 2 1.3. congeal escape Diagram 3 Chapter 2 Equipment Design 4 2.1. Reactor Effluent storage tank (E 1102) 4 2.2. clothe Cooler (E 1103) 5 2.3. flesh Separator (V 1102) 5 2.4. dimethyl ketone Stripper (T 1101) 6 2.5. dimethyl ketone editorial (T 1102) 6 2.6.

Acetone Overhead condenser (E 1104) 6 2.7. Acetone ebb outsmart (V 1103) 7 2.8. Acetone wane pith (P 1103 A/B) 7 2.9. Acetone Reboiler (E 1105) 7 2.10. IPA chromatography column spunk (P 1104 A/B) 8 2.11. IPA newspaper column (T 1103) 8 2.12. IPA Overhead Condenser (E 1106) 9 2.13. IPA Reflux Drum (V 1104) 9 2.14. IPA Reflux Pump (P 1105 A/B) 10 2.15. IPA Reboiler (E 1107) 10 2.16. neutralise water system Cooler (E 1108) 11 Chapter 3 Flow Table 12 Chapter 4 Discussion 14 Chapter 5 Conclusion 16 References 17 cecal appendage Sample...If you want to get a full essay, order it on our website: Ordercustompaper.com

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