The process for making cyclohexane by saturation of benzene consists of a feed-effluent heat exchanger, a saturation
Question:
The process for making cyclohexane by saturation of benzene consists of a feed-effluent heat exchanger, a saturation reactor and a product stabilizer column. Estimate the cost of a plant that produces 200,000 metric tons per year (200 kte/y) of cyclohexane using the correlation in Table 6.2 and Bridgewater’s method.
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Table 6.2 Process cost correlations Process ABS Resin (15% Rubber) by emulsion polymerization Acetic Acid by Cativa process Acetic Acid by Low Water Methanol Carbonylation Acrolein by propylene oxidation with Bi/Mo catalyst Adipic acid from phenol Alkylation (sulphuric acid effluent refrigeration process) Alkylation (HF process) Allyl chloride by propylene chlorination Alpha olefins (full range process) Alpha olefins (full range process) Benzene by Sulpholane extraction Benzene reduction by Bensat Biodiesel (FAME) from vegetable oil bis-HET by Eastman Glycolysis BTX Aromatics by Cyclar process BTX Aromatics by CCR Platforming Butadiene by extractive distillation Butadiene by Oxo-D plus extractive distillation Butene-1 by Alphabutol ethylene dimerization Caprolactam from nitration-grade toluene Carbon monoxide by steam methane reforming Catalytic Condensation for Gasoline Production Catalytic reforming by CCR Platforming Coking by Flexicoking including Fluid Coking Coking by Selective Yield Delayed Coking Copolymer polypropylene by INNOVENE Licensor Generic ВР Celanese Generic Generic Stratco/ DuPont UOP Generic Chevron Phillips Shell UOP/Shell UOP Generic Eastman BP/UOP UOP UOP/BASF Texas Petrochem. Axens SNIA BPD S. p.A. Generic UOP UOP ExxonMobil Foster Wheeler/UOP BP Capacity units MMlb/y MMlb/y MMlb/y MMIb/y MMlb/y bpd bpd MMlb/y MMIb/y MMIb/y MMgal/y bpd MMlb/y MMlb/y tpy tpy MMIb/y MMIb/y tpy tpy MMscf/y bpd bpd bpd bpd MMIb/y Slower 50 500 500 30 300 4,000 5,000 80 400 400 50 8,000 100 50 5,000 2,000 15,000 Supper 15,000 300 15,000 2,000 2,000 300 150 1000 20,000 200,000 800,000 200,000 100 100 12,000 250 1,200 1,000 200 15,000 40,000 120,000 500 200 30,000 6,000 60,000 40,000 a 60,000 12.146 8.146 0.6 7.793 0.6 0.0275 0.6 2.747 0.6 0.500 0.6 0.044 0.6 0.6 800,000 500 500 11.314 0.6 0.015 5.514 0.6 900 6.809 10,000 30,000 0.222 3.474 0.6 2.772 0.6 5.240 3.533 0.6 0.160 0.6 0.153 0.6 7.581 0.6 n 0.363 0.6 0.0251 0.6 0.179 0.6 0.321 0.6 0.343 0.109 3.430 0.6 0.6 0.6 0.6 0.6 0.68 0.6 ct Go t
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From Table 62 the cost correlation for the Axens process for benzene saturation gives That we have obtained two very different answers Bridgewaters co...View the full answer
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Related Book For
Chemical Engineering Design
ISBN: 9780081025994
6th Edition
Authors: Ray Sinnott, R.K. Sinnott, Sinnott Gavin Towler
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