Propylene Oxide Production from Propylene - Cost Analysis - Propylene Oxide E22A


Book Description

This report presents a cost analysis of Propylene Oxide (PO) production from chemical grade (CG) propylene. The process examined is a hydro-oxidation process similar to Bayer process. This report was developed based essentially on the following reference(s): Keywords: Bayer, Dow




Propylene Oxide Production from Propylene - Cost Analysis - Propylene Oxide E22A


Book Description

This report presents a cost analysis of Propylene Oxide (PO) production from chemical grade (CG) propylene The process examined is a hydro-oxidation process similar to Bayer process. This report was developed based essentially on the following reference(s): Keywords: Bayer, Dow




Epichlorohydrin Production from Propylene - Cost Analysis - ECH E22A


Book Description

This report presents a cost analysis of Epichlorohydrin production from propylene and chlorine. The process examined is similar to Daiso's Allyl Alcohol route. In this process, propylene is subjected to direct oxidation and further hydrolysis to obtain allyl alcohol. This intermediate undergoes chlorination and, after a final step of alkaline epoxidation, Epichlorohydrin is obtained. This report was developed based essentially on the following reference(s): Keywords: Allyl alcohol route, Daiso, alkaline epoxidation




Sucrose-Based Polyether Production - Cost Analysis - Polyether E22A


Book Description

This report presents a cost analysis of Sucrose-Based Polyether production from propylene oxide. The process examined is a typical alkoxylation process. In this process, sucrose is used as starter in the reaction. This report was developed based essentially on the following reference(s): Keywords: Sucrose-Based Polyol, PO, Propoxylation




Biobased Adipic Acid Production from Glucose - Cost Analysis - Adipic Acid E22A


Book Description

This report presents a cost analysis of Bio-Adipic Acid production from glucose syrup. The process examined is a two-step catalytic process similar to Rennovia process. In this process, glucose is first oxidized to produce glucaric acid, which is then hydrogenated to produce Adipic Acid. The process uses a 70 wt% glucose-water syrup as raw material. This report examines one-time costs associated with the construction of a United States-based plant and the continuing costs associated with the daily operation of such a plant. More specifically, it discusses: * Capital Investment, broken down by: - Total fixed capital required, divided in production unit (ISBL); infrastructure (OSBL) and contingency - Alternative perspective on the total fixed capital, divided in direct costs, indirect costs and contingency - Working capital and costs incurred during industrial plant commissioning and start-up * Production cost, broken down by: - Manufacturing variable costs (raw materials, utilities) - Manufacturing fixed costs (maintenance costs, operating charges, plant overhead, local taxes and insurance) - Depreciation and corporate overhead costs * Raw materials consumption, products generation and labor requirements * Process block flow diagram and description of industrial site installations (production unit and infrastructure) This report was developed based essentially on the following reference(s): US Patent 8669397, issued to Rennovia in 2014 Keywords: Bioadipic Acid, Hexanedioic Acid, Dextrose, Glucose Oxidation, Glucaric Acid Hydrogenation, Green Adipic Acid, Renewable Feedstock




Chlorine Production from Hydrogen Chloride - Cost Analysis - Chlorine E22A


Book Description

This report presents a cost analysis of secondary Chlorine production from hydrogen chloride. The process examined is similar to the ThyssenKrupp Uhde hydrogen chloride electrolysis process. In this process, a hydrogen chloride solution in water is decomposed electrolytically in a diaphragm cell, producing Chlorine. Hydrogen is generated as by-product This report was developed based essentially on the following reference(s): "Chlorine", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition Keywords: Secondary chlorine, hydrogen chloride waste treatment, HCl, cholrine recovery




Impact Polypropylene via Gas Process - Cost Analysis - PP E22A


Book Description

This report presents a cost analysis of Polypropylene (PP) impact copolymer production from polymer grade (PG) propylene and ethylene using a gas phase polymerization process. The process examined is similar to Grace UNIPOL process. This process is based on the polymerization of gaseous PG propylene and ethylene in fluidized-bed reactors. This report was developed based essentially on the following reference(s): Keywords: PG Propylene, Propene, Ethene, Dow, Gas-Phase Reactor, Fluidized Bed Reactor




Hydrochloric Acid Production - Cost Analysis - HCl E22A


Book Description

This report presents a cost analysis of Hydrochloric Acid (HCl) production from sodium chloride and sulfuric acid. 'The process examined is based on the Mannheim process. In this process, sodium chloride reacts with sulfuric acid at elevated temperatures in a fluidized bed reactor, producing Hydrochloric Acid and sodium sulfate, a by-product. This report was developed based essentially on the following reference(s): Keywords: Hydrochloric Acid, Direct Synthesis




Paraxylene Production from Toluene - Cost Analysis - Paraxylene E22A


Book Description

This report presents a cost analysis of para-Xylene production from toluene. The process examined is a selective toluene disproportionation process (STDP). In this process, toluene undergoes a selective disproportionation reaction to produce xylenes (mainly p-Xylene) and benzene. Then, benzene is separated as a by-product and p-Xylene is recovered in a crystallization unit. This report was developed based essentially on the following reference(s): (1) US Patent 7230152, issued to UOP in 2007 (2) US Patent 4097543, issued to ExxonMobil in 1978 Keywords: Mixed Xylenes, C8 Aromatics, PX-Plus, Badger/Niro




Reformate Production from Naphtha - Cost Analysis - Reformate E22A


Book Description

This report presents a cost analysis of Aromatic Reformate production from naphtha using a catalytic reforming process. The process examined is similar to Chevron Phillips Aromax process. In this process, hydrogen is generated as by-product. This report was developed based essentially on the following reference(s): US Patent 4,645,586, issued to Chevron Chemical in 1987 Keywords: Reformer, BTX, CP Chem, Fixed Bed Reforming, Toluene, On-Purpose Benzene Production