Acetone Production from Propylene - Cost Analysis - Acetone E11A

Acetone Production from Propylene - Cost Analysis - Acetone 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 Acetone production from propylene. The process examined is a typical hydration/dehydrogenation process. In this process, propylene is directly hydrated in a catalytic reactor, producing isopropanol. Then, isopropanol is dehydrogenated in the vapor phase in a fixed bed catalyst reactor to produce acetone. This report was developed based essentially on the following reference(s): Keywords: Propanone, Fixed-Bed Reactor, Catalytic Reactor, Isopropyl Alcohol, 2-Propanol


Acetone Production from Propylene - Cost Analysis - Acetone E11A

Acetone Production from Propylene - Cost Analysis - Acetone E11A

Author: Intratec

Publisher: Intratec

Published: 2017-06-01

Total Pages: 102

ISBN-13: 1641480718

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This report presents a cost analysis of Acetone production from propylene The process examined is a typical hydration/dehydrogenation process. In this process, propylene is directly hydrated in a catalytic reactor, producing isopropanol. Then, isopropanol is dehydrogenated in the vapor phase in a fixed bed catalyst reactor to produce acetone. This report was developed based essentially on the following reference(s): Keywords: Propanone, Fixed-Bed Reactor, Catalytic Reactor, Isopropyl Alcohol, 2-Propanol


Acetone Production from Propylene - Cost Analysis - Acetone E12A

Acetone Production from Propylene - Cost Analysis - Acetone E12A

Author: Intratec

Publisher: Intratec

Published: 2019-09-17

Total Pages: 102

ISBN-13:

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This report presents a cost analysis of Acetone production from propylene. The process examined is a typical direct oxidation process. This report was developed based essentially on the following reference(s): Keywords: Propanone, Isopropyl Alcohol, 2-Propanol, Wacker Chemie, Hoechst


Methyl Methacrylate from Acetone - Cost Analysis - MMA E11A

Methyl Methacrylate from Acetone - Cost Analysis - MMA E11A

Author: Intratec

Publisher: Intratec

Published: 2017-06-01

Total Pages: 102

ISBN-13: 1641481196

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This report presents a cost analysis of Methyl Methacrylate (MMA) production from acetone, ammonia and natural gas The process examined is similar to Evonik Aveneer process. In this process, hydrogen cyanide, acetone and methanol are used as raw materials for the production of MMA. Different from the conventional acetone cyanohydrin (ACH) process, this process does not use sulfuric acid. The hydrogen cyanide used is generated from ammonia and natural gas in an on-site unit. This report was developed based essentially on the following reference(s): (1) US Patent 8569539, issued to Evonik in 2013 (2) US Patent 20120232305, issued to Evonik in 2012 (3) US Patent 20080194875, issued to Evonik in 2008 Keywords: Propanone, Hydrolysis, Transesterification, Dehydration, Prussic Acid


Isopropyl Alcohol Production from RG Propylene - Cost Analysis - Isopropanol E11A

Isopropyl Alcohol Production from RG Propylene - Cost Analysis - Isopropanol E11A

Author: Intratec

Publisher: Intratec Solutions

Published: 2019-09-17

Total Pages: 103

ISBN-13:

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This report presents a cost analysis of Isopropanol production from refinery grade (RG) propylene. The process examined is a typical indirect propylene hydration process. In this process, RG propylene reacts with sulfuric acid to form isopropyl alcohol sulfates. Those sulfates are then reacted with water to form Isopropanol. This report was developed based essentially on the following reference(s): "Isopropyl Alcohol", Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition Keywords: Isopropanol, isopropyl alcohol, IPA, indirect propylene hydration, evonik degussa


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


Isopropyl Alcohol Production from RG Propylene - Cost Analysis - Isopropanol E11A

Isopropyl Alcohol Production from RG Propylene - Cost Analysis - Isopropanol E11A

Author: Intratec

Publisher: Intratec

Published: 2017-06-01

Total Pages: 103

ISBN-13: 1641481099

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This report presents a cost analysis of Isopropanol production from refinery grade (RG) propylene The process examined is a typical indirect propylene hydration process. In this process, RG propylene reacts with sulfuric acid to form isopropyl alcohol sulfates. Those sulfates are then reacted with water to form Isopropanol. This report was developed based essentially on the following reference(s): "Isopropyl Alcohol", Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition Keywords: Isopropanol, isopropyl alcohol, IPA, indirect propylene hydration, evonik degussa


Isopropyl Alcohol Production from Acetone - Cost Analysis - Isopropanol E31A

Isopropyl Alcohol Production from Acetone - Cost Analysis - Isopropanol E31A

Author: Intratec

Publisher: Intratec

Published: 2017-06-01

Total Pages: 104

ISBN-13: 164148053X

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This report presents a cost analysis of Isopropanol production from acetone The process examined is a typical acetone hydrogenation process. In this process, acetone hydrogenation is carreid out in liquid phase, in a fixed bed reactor, catalyzed by a Raney nickel catalyst. This report was developed based essentially on the following reference(s): (1) US Patent 8283504, issued to Mitsui Chemicals in 2012 (2) US Patent 20150083578, issued to LG Chem, LTD in 2015 (3) US Patent 6930213, issued to INEOS Phenol GMBH (former Phenolchemie GmbH & Co. KG) in 2006 Keywords: Isopropanol, isopropyl alcohol, IPA, acetone hydrogenation, lummus, polimeri europa, versalis


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 Solutions

Published: 2019-09-17

Total Pages: 104

ISBN-13:

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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