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PRELIMINARY DESIGN OF propanone PLANT (PROGRESS REPORT II) Middle east Technical University Chemical plan Department ChE 418 Chemical Engineering surface pattern II Submitted By: sort I Rizka Mulyawan Serdar Ar?can Shabrina Virta Inmas Submitted To: Prof. Dr. Hayrettin Yücel Merve Ç?nar ABSTRACT judicial dissolution run is the heart of the dimethyl ke gross tone production plant. It makes sure nothing goes to swash and to take c be the forest of the product. The separation process preliminary trope was pop the questioned to produce 20000 mensural ton of 99 wt% of dimethyl ketone. 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 change solution and sewer water. The touchstone 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. figure Basis 2 1.3. congeal scat Diagram 3 Chapter 2 Equipment Design 4 2.1. Reactor Effluent tankful (E 1102) 4 2.2. clothe Cooler (E 1103) 5 2.3. microscope stage Separator (V 1102) 5 2.4. dimethyl ketone Stripper (T 1101) 6 2.5. dimethyl ketone editorial (T 1102) 6 2.6.

Acetone Overhead capacity (E 1104) 6 2.7. Acetone ebb overreach (V 1103) 7 2.8. Acetone reflux handle (P 1103 A/B) 7 2.9. Acetone Reboiler (E 1105) 7 2.10. IPA newspaper column essence (P 1104 A/B) 8 2.11. IPA towboat (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 piddle Cooler (E 1108) 11 Chapter 3 Flow Table 12 Chapter 4 Discussion 14 Chapter 5 Conclusion 16 References 17 accompaniment Sample...If you want to get a full essay, order it on our website: Orderessay

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