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This report presents a cost analysis of 1,4-Butanediol (BDO) production from propylene. In this process, propylene is first converted to allyl alcohol intermediate, which is then converted to BDO. Propanol and 2-methyl-1,3-propanediol are generated as by-products. This report was developed based essentially on the following reference(s): (1) "Butanediols, Butenediol, and Butynediol", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition (2) "Allyl Alcohol and Monoallyl Derivatives", Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition Keywords: Hydroformylation, Hydrogenation, Acetoxylation, Dairen Chemical Corporation, DCC
This report presents a cost analysis of Polymer Grade (PG) Propylene production from methanol using a methanol-to-propylene (MTP) process. The process examined is similar to Lurgi MTP process. This process is carried out in two steps: first, methanol is converted to dimethyl ether (DME), and then DME is converted to Propylene. Gasoline is also generated as by-product in the process. 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 20100063337, issued to Lurgi in 2010 Keywords: PG Propylene, Methyl Alcohol, Propene, On-Purpose Propylene Production
This report presents a cost analysis of hydrous Ethanol production from corn. The process examined is a typical dry milling process. In this process, Distiller's Dried Grain with Solubles (DDGS) is generated as by-product. 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): "Ethanol", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition Keywords: Ethyl Alcohol, Bioethanol, Biomass
This report presents a cost analysis of Vinyl Chloride production from ethylene and chlorine via a balanced process. This typical balanced process combines two ethylene dichloride (EDC) production routes, direct chlorination and oxychlorination, for the production of Vinyl Chloride. By doing so, hydrogen chloride byproduct, produced in the thermal cracking unit, is used as raw material in the oxychlorination unit for additional production of EDC from ethylene. 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): (1) US Patent 7767869, issued to Vinnolit in 2010; (2) US Patent 6235953, issued to Vinnolit in 2001 Keywords: Chloroethene, 1,2-Dichloroethane, Hydrochlorination, INEOS, Vinnolit, Balanced Process
This report presents a cost analysis of DL-Methionine production from acrolein, methyl mercaptan, and hydrogen cyanide (HCN). The process examined is a typical carbonate process. This process is a multi-step process including: methional production; hydantoin intermediate production; reaction of hydantoin with potassium carbonate to produce potassium methioninate; and methioninate conversion to DL-Methionine. 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 20130231501, issued to Evonik in 2013 Keywords: DLM, 3-Methylmercapto Propionaldehyde, MMP, Methional, Propenal, Methanethiol, Essential Amino Acid, Degussa