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Propylene Production From Ethylene Cost Analysis Propylene E21a
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Book Synopsis Propylene Production from Ethylene - Cost Analysis - Propylene E21A by : Intratec
Download or read book Propylene Production from Ethylene - Cost Analysis - Propylene E21A written by Intratec and published by Intratec. This book was released on 2017-06-01 with total page 106 pages. Available in PDF, EPUB and Kindle. Book excerpt: This report presents a cost analysis of Polymer Grade (PG) Propylene production from ethylene using two integrated processes: dimerization and metathesis The processes examined are similar to CB&I Lummus technologies: Ethylene Dimerization Technology and Olefins Conversion Technology (OCT). In these processes, ethylene is first dimerized into butenes, and then, Propylene is produced through a metathesis reaction of 2-butene and ethylene. This report was developed based essentially on the following reference(s): (1) US Patent 8440874, issued to Lummus Technology and BASF in 2013 (2) US Patent 4242531, issued to Phillips Petroleum Company in 1980 Keywords: PG Propylene, Olefins Dimerization, Olefins Disproportionation, Lummus OCT, Olefins Metathesis, Phillips Triolefin, Propene, Ethene, On-Purpose Propylene Production
Book Synopsis Epichlorohydrin Production from Propylene - Cost Analysis - ECH E21A by : Intratec
Download or read book Epichlorohydrin Production from Propylene - Cost Analysis - ECH E21A written by Intratec and published by Intratec. This book was released on 2019-09-17 with total page 102 pages. Available in PDF, EPUB and Kindle. Book excerpt: This report presents a cost analysis of Epichlorohydrin production from propylene and chlorine. The process examined is a typical dehydrochlorination process. This process involves three main steps: (i) chlorination of propylene to allyl chloride; (ii) addition of hypochlorous acid to the allyl chloride formed yielding glycerol dichlorohydrins, and (iii) treatment of the glycerol – dichlorohydrin mixture with a base, yielding Epichlorohydrin product. 99.9 wt.% Epichlorohydrin is obtained. This report was developed based essentially on the following reference(s): Rowe, C.E., 'Chlorohydrins', Chemical Processing Handbook, 1993 Keywords: 3-Chloropropene, Hypochlorous Acid, HOCl, Chlorination
Book Synopsis Butyl Acrylate Production from Propylene and Butanol - Cost Analysis - Butyl Acrylate E21A by : Intratec
Download or read book Butyl Acrylate Production from Propylene and Butanol - Cost Analysis - Butyl Acrylate E21A written by Intratec and published by Intratec. This book was released on 2017-06-01 with total page 102 pages. Available in PDF, EPUB and Kindle. Book excerpt: This report presents a cost analysis of n-Butyl Acrylate production from chemical grade propylene and n-butanol The process examined is a typical propylene oxidation, followed by a typical esterification process. In this process, propylene passes through a two-stage vapor phase oxidation to generate an acrylic acid-containing gas, from which acrylic acid is recovered via absorption in water. The aqueous acrylic acid solution is purified via light solvent extraction to ester-grade acrylic acid to be combined with n-butanol in a esterification reactor to generate crude a crude ester stream that is furhter purified to generate high-purity butyl acrylate. This report was developed based essentially on the following reference(s): (1) "Acrylic Acid", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition (2) "Acrylic Acid and Derivatives", Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition Keywords: Propene, Air Oxidation, Propenoic Acid, Nippon Shokubai, Rohm & Haas, Dow, Esterification, Nippon Shokubai, Mitsubishi, BASF
Book Synopsis Ethylene Production via Cracking of Ethane/Propane - Cost Analysis - Ethylene E21A by : Intratec
Download or read book Ethylene Production via Cracking of Ethane/Propane - Cost Analysis - Ethylene E21A written by Intratec and published by Intratec Solutions. This book was released on 2019-09-17 with total page 102 pages. Available in PDF, EPUB and Kindle. Book excerpt: This report presents a cost analysis of polymer grade (PG) Ethylene production starting from an ethane/propane mixture at a volume ratio of 4:1. A typical steam cracking process with front-end demethanization is employed. In this process, a mix of 80 vol% ethane and 20 vol% propane is thermally cracked in pyrolysis furnaces. In addition to polymer grade Ethylene, the process also generates polymer grade propylene and hydrogen-rich gas. This report was developed based essentially on the following reference(s): "Ethylene", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition Keywords: Ethene, Propene, Hydrocarbon Pyrolysis, Cracking Furnace, Lummus, KBR, Technip, Linde, S&W
Book Synopsis Impact Polypropylene via Gas Process - Cost Analysis - PP E21A by : Intratec
Download or read book Impact Polypropylene via Gas Process - Cost Analysis - PP E21A written by Intratec and published by Intratec. This book was released on 2019-09-17 with total page 103 pages. Available in PDF, EPUB and Kindle. Book excerpt: 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 LyondellBasell Spherizone process. This process is based on the polymerization of PG propylene and ethylene in a multi-zone circulating reactor. This report was developed based essentially on the following reference(s): Keywords: PG Propylene, Propene, Ethene, MZCR, Gas-Phase Reactor, Bimodal
Book Synopsis Butanol Production from Propylene and Syngas - Cost Analysis - Butanol E21A by : Intratec
Download or read book Butanol Production from Propylene and Syngas - Cost Analysis - Butanol E21A written by Intratec and published by Intratec Solutions. This book was released on 2016-05-01 with total page 52 pages. Available in PDF, EPUB and Kindle. Book excerpt: This report presents a cost analysis of n-Butanol production from propylene and syngas. The process examined is similar to the LP OXO technology jointly licensed by JM Davy and Dow, employing Selector 30 catalyst. In this process, the production ratio of n- to iso-butyraldehyde in the oxo reaction is about 30. The isobutyraldehyde is separated as a by-product and the n-butyraldehyde is hydrogenated to form n-Butanol as the final 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) Keywords: Oxo Alcohol, Butyl Alcohol, n-Butanol, Johnson Matthey, Dow, LP Oxo, SELECTOR
Book Synopsis Dimethyl Carbonate Production from Ethylene Carbonate - Cost Analysis - DMC E21A by : Intratec
Download or read book Dimethyl Carbonate Production from Ethylene Carbonate - Cost Analysis - DMC E21A written by Intratec and published by Intratec. This book was released on 2019-09-17 with total page 102 pages. Available in PDF, EPUB and Kindle. Book excerpt: This report presents a cost analysis of Dimethyl Carbonate (DMC) production from ethylene carbonate and methanol. The process examined is a typical transesterification process. In this process, ethylene carbonate and methanol are converted into dimethyl carbonate (DMC) and ethylene glycol in a reactive distillation column and purified DMC is obtained through an extractive distillation. Monoethylene glycol is generated as by-product. This report was developed based essentially on the following reference(s): Keywords: Transesteification, ethylene arbonate, DMC, methanol, MEG
Book Synopsis Ethylene Dichloride Production from Ethylene and HCl - Cost Analysis - EDC E21A by : Intratec
Download or read book Ethylene Dichloride Production from Ethylene and HCl - Cost Analysis - EDC E21A written by Intratec and published by Intratec. This book was released on 2019-09-17 with total page 102 pages. Available in PDF, EPUB and Kindle. Book excerpt: This report presents a cost analysis of Ethylene Dichloride (EDC) production from ethylene and hydrogen chloride using an oxychlorination process. The process examined is similar to OxyVinyls process. This process involves an oxygen-based chlorination step, which is carried out in fluidized-bed reactors. This report was developed based essentially on the following reference(s): (1) US Patent 7585806, issued to OxyVinyls in 2009 (2) US Patent 5292703, originally issued to The Geon Company (assigned to OxyVinyls in 1999) Keywords: Ethene, 1,2-Dichloroethane, Mitsui, Fluidized-Bed Reactor
Book Synopsis Ethylene Glycol Production from Carbon Dioxide - Cost Analysis - MEG E21A by : Intratec
Download or read book Ethylene Glycol Production from Carbon Dioxide - Cost Analysis - MEG E21A written by Intratec and published by Intratec. This book was released on 2019-09-17 with total page 101 pages. Available in PDF, EPUB and Kindle. Book excerpt: This report presents a cost analysis of Monoethylene Glycol (MEG) production from carbon dioxide (CO2) using an electrochemical process. The process examined is similar to Liquid Light process. In this process, CO2 is electrochemically converted to oxalic acid, which is then hydrogenated to MEG. This report was developed based essentially on the following reference(s): US Patents 20140221684 and 20140206895, both issued to Liquid Light in 2014 Keywords: Ethylene Glycol, Fiber Grade, Hydrogen Bromide, Bromine, 1,2-Ethanediol
Book Synopsis Polytrimethylene Terephthalate Production - Cost Analysis - PTT E21A by : Intratec
Download or read book Polytrimethylene Terephthalate Production - Cost Analysis - PTT E21A written by Intratec and published by Intratec. This book was released on 2019-09-17 with total page 102 pages. Available in PDF, EPUB and Kindle. Book excerpt: This report presents a cost analysis of Polytrimethylene Terephthalate (PTT) production starting from glucose syrup and terephthalic acid. The process examined combines a process similar to DuPont process for generating propanediol and a process similar to Degussa (now Evonik) process for producing PTT. In this process, a 70 wt% glucose-water syrup is used as raw material. This report was developed based essentially on the following reference(s): Keywords: 1,3-Polypropylene Terephthalate, TPA, Dimethyl Terephthalate, DMT, Bio-PDO, Trimethylene Glycol, PTT, Aerobic Fermentation
Book Synopsis Diphenyl Carbonate from Ethylene Oxide and Phenol - Cost Analysis - DPC E21A by : Intratec
Download or read book Diphenyl Carbonate from Ethylene Oxide and Phenol - Cost Analysis - DPC E21A written by Intratec and published by Intratec Solutions. This book was released on 2019-09-17 with total page 102 pages. Available in PDF, EPUB and Kindle. Book excerpt: This report presents a cost analysis of Diphenyl Carbonate (DPC) production from ethylene oxide and phenol. The process examined is similar to Asahi Kasei process. In this process, dimethyl carbonate (DMC) intermediate is initially produced from ethylene oxide and methanol. Then, DMC and phenol react to produce DPC. Ethylene glycol is generated as by-product in the process. This report was developed based essentially on the following reference(s): US Patent 20090163734, issued to Asahi Kasei in 2009 Keywords: Phenyl Carbonate, EO, Carbonation, Transesterification, Reactive Distillation
Book Synopsis Acrylic Acid Production from Glycerol - Cost Analysis - Acrylic Acid E21A by : Intratec
Download or read book Acrylic Acid Production from Glycerol - Cost Analysis - Acrylic Acid E21A written by Intratec and published by Intratec Solutions. This book was released on 2019-09-17 with total page 103 pages. Available in PDF, EPUB and Kindle. Book excerpt: This report presents a cost analysis of Ester-Grade Acrylic Acid (EAA) production from crude glycerol. The two-step process examined is similar to Arkema process. In this process, crude glycerol (at 85 wt% purity) obtained as by-product of biodiesel plants, is used as the main raw material. After purification, glycerol is dehydrated to acrolein and subsequently oxidized. The final product obtained is EAA, which is used in the production of acrylic esters. This report was developed based essentially on the following reference(s): US Patent 2010/0168471 A1, issued to Arkema in 2010 Keywords: Glicerin, Dehydration, Oxidation, Unsaturated Carboxylic Acid, Propenoic Acid
Book Synopsis Acrylonitrile Production from Propane - Cost Analysis - Acrylonitrile E21A by : Intratec
Download or read book Acrylonitrile Production from Propane - Cost Analysis - Acrylonitrile E21A written by Intratec and published by Intratec. This book was released on 2019-09-17 with total page 104 pages. Available in PDF, EPUB and Kindle. Book excerpt: This report presents a cost analysis of Acrylonitrile production from propane using a propane ammoxidation process. The process examined is similar to PTT Asahi Chemical process. In this process, propane and ammonia react to produce Acrylonitrile. Acetonitrile and hydrogen cyanide are generated as by-products. This report was developed based essentially on the following reference(s): US Patent 7919430, issued to Asahi Kasei in 2011 Keywords: Propenenitrile, Asahi Kasei, Fluidized Bed Reactor
Book Synopsis Polychloroprene Production - Cost Analysis - CR E21A by : Intratec
Download or read book Polychloroprene Production - Cost Analysis - CR E21A written by Intratec and published by Intratec. This book was released on 2019-09-17 with total page 103 pages. Available in PDF, EPUB and Kindle. Book excerpt: This report presents a cost analysis of Chloroprene Rubber (also known as Polychloroprene) production from butadiene and chlorine. 'The process examined is a typical vapor phase butadiene chlorination process, followed by a typical emulsion polymerization process. In this process butadiene is first chlorinated producing two chlorinated isomers, 1,4-dichloro 2-butene and 3,4-dichloro 1-butene. In a second step, 1,4-isomers are isomerized to 3,4-dichloro 1-butene. This chemical is then dehydrochlorinated in the presence of caustic soda producing chloroprene and sodium chloride. Finally, chloroprene is polymerized to form Polychloroprene. This report was developed based essentially on the following reference(s): (1) "Chloroprene", Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition (2) "Polychloroprene", Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition Keywords: Dupont, Chloroprene Rubber, Neoprene, Chlorination, Neoprene, Chloroprene Rubber, 2-Chlorobuta-1,3-Diene, Synthetic Rubbers
Book Synopsis Butadiene Production from Butenes - Cost Analysis - Butadiene E21A by : Intratec
Download or read book Butadiene Production from Butenes - Cost Analysis - Butadiene E21A written by Intratec and published by Intratec Solutions. This book was released on 2016-05-01 with total page 52 pages. Available in PDF, EPUB and Kindle. Book excerpt: This report presents a cost analysis of 1,3-Butadiene (BD) production from mixed butenes using an oxidative dehydrogenation process. The process examined is similar to TPC/UOP Oxo-D process. In this process, butenes are catalytically dehydrogenated to produce a crude butadiene stream which is further purified to the final Butadiene product. In the purification step, raffinate is obtained 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): "Butadiene", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition Keywords: Petrotex, Oxidative Dehydrogenation, BD, Fixed-Bed Reactor, BASF, NMP extraction
Book Synopsis Butanediol Production from Succinic Acid - Cost Analysis - Butanediol E21A by : Intratec
Download or read book Butanediol Production from Succinic Acid - Cost Analysis - Butanediol E21A written by Intratec and published by Intratec Solutions. This book was released on 2016-05-01 with total page 52 pages. Available in PDF, EPUB and Kindle. Book excerpt: 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
Book Synopsis LLDPE Production via Slurry Process - Cost Analysis - LLDPE E21A by : Intratec
Download or read book LLDPE Production via Slurry Process - Cost Analysis - LLDPE E21A written by Intratec and published by Intratec Solutions. This book was released on 2016-05-01 with total page 52 pages. Available in PDF, EPUB and Kindle. Book excerpt: This report presents a cost analysis of Linear Low Density Polyethylene (LLDPE) production from polymer grade (PG) ethylene and 1-hexene using a slurry process. The process examined is similar to Chevron Phillips 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 20120282144, issued to Chevron in 2012; (2) US Patent 7629421, issued to Chevron in 2009 Keywords: Ethene, PE, Isobutane, Slurry Reactor, Loop Reactor
