Acrylic Acid Production from Propylene - Cost Analysis - Acrylic Acid E11A
Acrylic Acid Production from Propylene - Cost Analysis - Acrylic Acid E11A

Author: Intratec

Publisher: Intratec

Published: 2017-06-01

Total Pages: 101

ISBN-13: 1641480734

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This report presents a cost analysis of Ester-Grade Acrylic Acid (EAA) production from chemical grade (CG) propylene The process examined is a typical propylene oxidation. 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 (EAA), which is used in the production of acrylic esters. This report was developed based essentially on the following reference(s): "Acrylic Acid", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition Keywords: Propene, Air Oxidation, Propenoic Acid, Nippon Shokubai, Rohm & Haas, Dow

Acrylonitrile Production from Propylene - Cost Analysis - Acrylonitrile E11A
Acrylonitrile Production from Propylene - Cost Analysis - Acrylonitrile E11A

Author: Intratec

Publisher: Intratec

Published: 2017-06-01

Total Pages: 104

ISBN-13: 1641480394

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This report presents a cost analysis of Acrylonitrile production from chemical grade (CG) propylene The process examined is a fluidized bed propylene ammoxidation process. In this process, propylene 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): "Acrylonitrile", Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition Keywords: Propene, Propenenitrile, INEOS, Sohio, Fluidized Bed Reactor

Acrolein Production from Propylene - Cost Analysis - Acrolein E11A
Acrolein Production from Propylene - Cost Analysis - Acrolein E11A

Author: Intratec

Publisher: Intratec

Published: 2019-09-17

Total Pages: 102

ISBN-13:

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This report presents a cost analysis of Acrolein production from propylene. In this typical process, propylene is oxidized with air, producing acrolein. Acrylic acid Diethylene glycol (DEG) and triethylene glycol (TEG) are also generated as by-products in the process. This report was developed based essentially on the following reference(s): Keywords: Propenal, Acrylic Aldehyde, Oxidation, Propene

Butyl Acrylate Production from Acrylic Acid and Butanol - Cost Analysis - Butyl Acrylate E11A
Butyl Acrylate Production from Acrylic Acid and Butanol - Cost Analysis - Butyl Acrylate E11A

Author: Intratec

Publisher: Intratec

Published: 2017-06-01

Total Pages: 100

ISBN-13: 1641480866

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This report presents a cost analysis of n-Butyl Acrylate production from ester grade acrylic acid and n-butanol The process examined is a typical esterification process. This report was developed based essentially on the following reference(s): (1) "Acrylic Acid and Derivatives", Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition (2) US Patent 6320070, issued to BASF in 2001 Keywords: Esterification, Nippon Shokubai, Mitsubishi, BASF

Polylactic Acid Production - Cost Analysis - PLA E11A
Polylactic Acid Production - Cost Analysis - PLA E11A

Author: Intratec

Publisher: Intratec Solutions

Published: 2016-05-01

Total Pages: 47

ISBN-13: 1945324996

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This report presents a cost analysis of Polylactic Acid (PLA) production from lactic acid using a melt process. The process examined is similar to NatureWorks process. In this process, an 88 wt% lactic acid solution in water 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 8674056, issued to NatureWorks in 2014; (2) EP Patent 1247808, issued to Cargill in 2003 Keywords: Lactide, 2-Hydroxypropanoic Acid, Dow, Biodegradable Polymer

Polyacrylonitrile Production - Cost Analysis - PAN E11A
Polyacrylonitrile Production - Cost Analysis - PAN E11A

Author: Intratec

Publisher: Intratec

Published: 2019-09-17

Total Pages: 102

ISBN-13:

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This report presents a cost analysis of Polyacrylonitrile (PAN) Precursor production. In this process, acrylonitrile is polymerized with methyl acrylate comonomer via aqueous dispersion polymerization and the polymer formed is subsequently converted to fiber through wet spinning. This report was developed based essentially on the following reference(s): (1) "Acrylic Fibers," Encyclopedia of Polymer Science and Technology (2) Morgan, P., Carbon Fibers and Their Composites, 2005 Keywords: Polyacrylonitrile, Carbon Fiber, Acrylic Fiber, Suspension Polymerization, Acrylonitrile, Wet Spinning

Methyl Acrylate from Acrylic Acid - Cost Analysis - Methyl Acrylate E11A
Methyl Acrylate from Acrylic Acid - Cost Analysis - Methyl Acrylate E11A

Author: Intratec

Publisher: Intratec

Published: 2017-06-01

Total Pages: 102

ISBN-13: 164148117X

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This report presents a cost analysis of Methyl Acrylate production from acrylic acid and methanol The process examined is a typical esterification process. In this process, acrylic acid and methanol are esterified in a fixed-bed reactor producing Methyl Acrylate. This report was developed based essentially on the following reference(s): Keywords: Methyl Alcohol, Lower Alkyl Acrylate, Methyl Prop-2-Enoate

Ethyl Acrylate from Acrylic Acid - Cost Analysis - Ethyl Acrylate E11A
Ethyl Acrylate from Acrylic Acid - Cost Analysis - Ethyl Acrylate E11A

Author: Intratec

Publisher: Intratec Solutions

Published: 2019-09-17

Total Pages: 102

ISBN-13:

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This report presents a cost analysis of Ethyl Acrylate production from acrylic acid and ethanol. The process examined is a typical esterification process. In this process, acrylic acid and ethanol are esterified in a fixed-bed reactor producing Ethyl Acrylate. This report was developed based essentially on the following reference(s): Keywords: Ethyl Alcohol, Lower Alkyl Acrylate, Ethyl Propenoate

Acrylic Acid Production from Propane - Cost Analysis - Acrylic Acid E91A
Acrylic Acid Production from Propane - Cost Analysis - Acrylic Acid E91A

Author: Intratec

Publisher: Intratec

Published: 2017-06-01

Total Pages: 102

ISBN-13: 1641480572

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This report presents a cost analysis of Ester-Grade Acrylic Acid (EAA) production from propane The process examined is a novel process for propane oxidation. In this process, propane is fed to an oxydehydrogenation reactor in the presence of steam to form propylene. The propylene-containing gas 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 (EAA). This report was developed based essentially on the following reference(s): (1) "Acrylic Acid and Derivatives", Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition (2) US Patent 6492548, issued to Union Carbide in 2002 Keywords: Propene, Air Oxidation, Propenoic Acid, Nippon Shokubai, Rohm & Haas, Dow

Industrial Environmental Chemistry
Industrial Environmental Chemistry

Author: Donald T. Sawyer

Publisher: Springer Science & Business Media

Published: 2013-12-11

Total Pages: 310

ISBN-13: 1489923209

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This monograph consists of manuscripts submitted by invited speakers who participated in the symposium "Industrial Environmental Chemistry: Waste Minimization in Industrial Processes and Remediation of Hazardous Waste," held March 24-26, 1992, at Texas A&M University. This meeting was the tenth annual international symposium sponsored by the Texas A&M Industry-University Cooperative Chemistry Program (IUCCP). The program was developed by an academic-industrial steering committee consisting of the co-chairmen, Professors Donald T. Sawyer and Arthur E. Martell of the Texas A&M University Chemistry Department, and members appointed by the sponsoring companies: Bernie A. Allen, Jr., Dow Chemical USA; Kirk W. Brown, Texas A&M University; Abraham Clearfield, Texas A&M University; Greg Leyes, Monsanto Company; Jay Warner, Hoechst-Celanese Corporation; Paul M. Zakriski, BF Goodrich Company; and Emile A. Schweikert, Texas A&M University (IUCCP Coordinator). The subject of this conference reflects the interest that has developed in academic institutions and industry for technological solutions to environmental contamination by industrial wastes. Progress is most likely with strategies that minimize waste production from industrial processes. Clearly the key to the protection and preservation of the environment will be through R&D that optimizes chemical processes to minimize or eliminate waste streams. Eleven of the papers are directed to waste minimization. An additional ten papers discuss chemical and biological remediation strategies for hazardous wastes that contaminate soils, sludges, and water.