a) Do an order of magnitude estimation of the capital cost of a plant the produces 80,000 metric tons per year of caprolactam (use Table 6.2 in textbook) b) A reactor vessel cost USD 365,000 in 2012, estimate the cost in 2020 c) Estimate the purchased cost of a distillation column, height 20m, diameter 2m and 10 bar (requires 20mm shell), with 40 trays (bubble cap). The reboiler is a kettle type heat exchanger, area 100m2. The condenser is a U-tube heat exchanger, area 50m2. All need to be in stainless steel. d) Estimate the purchased equipment cost on a 2020 basis of a reciprocating compressor (stempelstmkompressor), driver power 2.0MW. Table 6.2 Process cont correlations Preces \begin{tabular}{l} Caparily \\ anits \\ \hline Mimlbyy \\ \hline \end{tabular} S1= sio. ABS Reain (15s fublec) by emuluien 300.12.146 0. 16. polymeriration. Aeeric Acit to MMibly MMibiy Aerec Acil by Low Water Methanol Cartonylation. Acroleia by propylene oxilution with BiMo catalyst A.fipic acid froen phenet Alikylation (aulphuric acid efifiuent refriguration process) Alkylation (HH proees). Aflyl chloride by propylene: chlorination Alpha olefins (foll range process) Alpha obefins (full range process) Benzene by Sulpholane extraction Benzene by toluene hydrodealkylation Benzene nduction by Bensat Biodiesel (FAME) from vegetable oil bis-HET by Eaaman Glycolysis BTX Armaties by Cyclar process BTX Aromatics by CCR Platfoming Butadiene by extractive distillation Butadiene by Oxo-D plus extrictive distiflation Butene-1 by Alphabutol ethylene dimerization Butene-I by BP Process Caprolactam from nitration-grade toluene Carbon monoxide by steam methane Generic reforming Catalytic Condensation for Gasoline Production Catalytic reformuing by CCR Platforming Coking by Flexicoking including Fluid Coking Coking by Selective Yield Delayed Coking Copolymer polypropylene by INNOVENE