For the isopropyl alcohol to acetone process flowsheet given in Appendix B, Figure B.10.1, list the minimum input information required to obtain mass and energy balances for this process. Using the process simulator available to you, simulate the isopropyl alcohol to acetone process, and compare your results to those given in Table B.10.1.

Figure B.10.1

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V-1101 IPA Feed Drum P-1101A/B IPA Feed Pumps Process Water Isopropyl Alcohol V-1101 LIC E-1101 IPA Feed Vaporizer (FIC P-1101A/B R-1101 IPA Reactor hps E-1101 R-1101 E-1102 Reactor Effluent Cooler (3) 234 /2.16 (TIC) CW E-1103 Trim Cooler P-1102A/B E-1102 407 2.66 45 1.77 P-1102A/B Reactor Heater Pumps (4) 357 3.00 rw air E-1103 20 1.63 poc ng H-1101 Reactor Furnace H-1101 (8 5 V-1102 Phase Separator V-1102 FIC T-1101 6 14) 9 T-1101 T-1102 E-1104 Acetor Acetone Acetone Stripp Column Overhead Reflux Reboiler Reflux Condenser Drum Ips 61 1.20 T-1102 E-1105 33 V-1103 E-1105 P-1103A/B P-1104A/B T-1103 E-1106 Acetone Acetone Acetone IPA IPA IPA Column Column Overhead Condenser Pumps Pumps 66 CW E-1104 F (FIC Der (PIC P-1104 A/B V-1103 (LIC P-1103 A/B Ips T-1103 E-1107 16 19 (LIC) Temperature, °C Pressure, bar CW FIC E-1107 V-1104 P-1105A/B E-1108 IPA IPA IPA Waste- Reboiler Reflux Reflux water Drum Pumps Cooler E-1106 V-1104 P-1105 A/B CW LIC E-1108 45 1.26 Hydrogen Acetone Wastewater