Download Free Butanediol Production From Butadiene Cost Analysis Butanediol E51a Book in PDF and EPUB Free Download. You can read online Butanediol Production From Butadiene Cost Analysis Butanediol E51a and write the review.

This report presents a cost analysis of 1,4-Butanediol (BDO) production from butadiene (BD). The process examined is similar to Mitsubishi Chemical process. This report was developed based essentially on the following reference(s): CA Patent 2215544, issued to Mitsubishi Chemical in 1998 Keywords: Acetoxylation, Acetic Acid
This report presents a cost analysis of second generation Ethanol production from wood chips via a thermochemical process. The process examined is similar to the one reported by the National Renewable Energy Laboratory (NREL). In this process, biomass is subjected to gasification generating syngas, which is then converted to hydrous Ethanol. The process employs concepts similar to those proposed in patents issued to Range Fuels. Mixed alcohols are generated as by-products. 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): Phillips, S., et al., "Thermochemical Ethanol via Indirect Gasification and Mixed Alcohol Synthesis of Lignocellulosic Biomass, " Report NREL/TP-510-41168, National Renewable Energy Laboratory (NREL), 2007 Keywords: Ethyl Alcohol, Bioethanol, Lignocellulosic Biomass, 2nd Generation, Cellulosic Sugar, Hemicelluloses, Cellulose
This report presents a cost analysis of 1,4-Butanediol (BDO) production from maleic anhydride. The process examined is similar to JM Davy process. In this process, tetrahydrofuran (THF) is generated as by-product. This report was developed based essentially on the following reference(s): (1) WO Patent 2006037957, issued to Johnson Matthey Davy Technologies in 2006 (2) WO Patent 9743234, issued to Kvaerner in 1997 Keywords: KPT, Hydrogenation, Butyrolactone, GBL, Dehydration, Dimethyl Maleate
This report presents a cost analysis of 1,4-Butanediol (BDO) production from succinic acid using a hydrogenation process. The process examined is similar to BioAmber 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): (1) US Patent 20110245515, issued to BioAmber in 2011; (2) WO Patent 2012158180, issued to BioAmber in 2012 Keywords: BDO, Butanedioic Acid, Fixed-Bed Reactor, Hydrogenation
This report presents a cost analysis of bio-based 1,4-Butanediol (BDO) production from glucose syrup using a direct fermentation process. The process examined is similar to Genomatica process. In this process, a 70 wt% glucose-water syrup is used 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): (1) US Patent 20130109069, issued to Genomatica in 2013; (2) US Patent 8597918, issued to Genomatica in 2013 Keywords: BDO, Dextrose, Glucose Fermentation, Aerobic Fermentation, Green Butanediol, Renewable Feedstock
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 1,4-Butanediol (BDO) production from acetylene and formaldehyde. The process examined is a typical acetylene-based Reppe process. Acetylene and an aqueous solution of formaldehyde (37 wt%) react to produce 1,4-butynediol. The butynediol is then hydrogenated to produce BDO. 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) US Patent 7759531, issued to BASF in 2010 Keywords: BDO, Ethyne, Fixed-Bed Reactor, Catalytic Reactor
This report presents a cost analysis of 1,4-Butanediol (BDO) production from propylene oxide. The process examined is similar to LyondellBasell process. In this process, propylene oxide is first isomerized 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) US Patent 2017/0144953, issued to LyondellBasell in 2017 (2) US Patent 7279606, issued to LyondellBasell in 2007 (3) US Patent 6969780, issued to LyondellBasell in 2005 Keywords: Hydroformylation, Synthesis Gas, Hydrogenation, Isomerization, Kuraray
This report presents a cost analysis of bio-based 1,4-Butanediol (BDO) production from glucose syrup. The two-step process examined is similar to Myriant/JM Davy process. BDO is produced via succinic acid intermediate produced from glucose fermentation. The process uses a 70 wt% glucose-water syrup as raw material and generates ammonium sulfate and tetrahydrofuran (THF) as by-products. This report was developed based essentially on the following reference(s): (1) US Patent 8778656, issued to Myriant in 2014 (2) US Patent 20140350308, issued to Johnson Matthey Davy Technologies in 2014 Keywords: Dextrose, Esterification, Methanol, Hydrogenation, Butanedioic Acid
This report presents a cost analysis of bio-based 1,4-Butanediol (BDO) production from glucose syrup. The process examined consists of two steps: a fermentation step for the production of succinic acid; and the hydrogenation of the succinic acid to produce Butanediol. Glucose-water syrup (70 wt%) is used as raw material. This report was developed based essentially on the following reference(s): (1) WO Patent 2009082050, issued to Korea Advanced Institute of Science & Technology (KAIST) in 2009 (2) US Patent 6008384, issued to DuPont in 1999 (assigned to Invista in 2007) Keywords: BDO, Dextrose, Glucose Fermentation, Butanedioic Acid, DuPont, Green Butanediol, Renewable Feedstock