Propylene Oxide from Propylene & Hydrogen Peroxide - Cost Analysis - Propylene Oxide E61A

Propylene Oxide from Propylene & Hydrogen Peroxide - Cost Analysis - Propylene Oxide E61A
Author: Intratec
Publisher: Intratec
Total Pages: 102
Release: 2019-09-17
Genre: Business & Economics
ISBN:

This report presents a cost analysis of Propylene Oxide (PO) production from chemical grade (CG) propylene and hydrogen peroxide. The process under analysis is similar to the hydrogen peroxide to Propylene Oxide (HPPO) process jointly developed by Evonik and Uhde. This report was developed based essentially on the following reference(s): US 20030092920, issued to Evonik Degussa GmbH in 2003 Keywords: Evonik, Degussa, Uhde, Oxidation, Epoxidation, HPPO

PG Propylene Production from RG Propylene - Cost Analysis - Propylene E61A

PG Propylene Production from RG Propylene - Cost Analysis - Propylene E61A
Author: Intratec
Publisher: Intratec
Total Pages: 102
Release: 2019-09-17
Genre: Business & Economics
ISBN:

This report presents a cost analysis of Polymer Grade (PG) Propylene production from refinery grade (RG) propylene. The process examined consists of a deethanizer column and a conventional high-pressure Propylene-Propane Splitter system, comprised of two towers. In this process, a propane stream is generated as by-product. This report was developed based essentially on the following reference(s): (1) "Propene", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition (2) Arons, J. d. S., van der Kooi, H. & Sankaranarayanan, K., "Separations", Efficiency and Sustainability in the Energy and Chemical Industries Keywords: PG Propylene, Propene, RG Propylene, Distillation, P-P Splitter

Butanol Production from Propylene and Syngas - Cost Analysis - Butanol E61A

Butanol Production from Propylene and Syngas - Cost Analysis - Butanol E61A
Author: Intratec
Publisher: Intratec
Total Pages: 102
Release: 2019-09-17
Genre: Business & Economics
ISBN:

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 developed by JM Davy and Union Carbide, employing Selector 10 catalyst. In this process, the production ratio of n- to iso-butyraldehyde in the oxo reaction is about 10. The isobutyraldehyde is separated as a by-product and the n-butyraldehyde is hydrogenated to form n-Butanol as the final product. This report was developed based essentially on the following reference(s): Keywords: Oxo Alcohol, Butyl Alcohol, n-Butanol, Johnson Matthey, Dow, LP Oxo, SELECTOR

Adipic Acid from Benzene and Propylene - Cost Analysis - Adipic Acid E61A

Adipic Acid from Benzene and Propylene - Cost Analysis - Adipic Acid E61A
Author: Intratec
Publisher: Intratec
Total Pages: 102
Release: 2019-09-17
Genre: Business & Economics
ISBN:

This report presents a cost analysis of Adipic Acid production from benzene and propylene. The process examined is a typical hydrogenation process. In this process, the Adipic Acid plant is integrated upstream with a plant for phenol production from benzene and propylene, and a plant for nitric acid production. Acetone is generated as by-product. This report was developed based essentially on the following reference(s): (1) "Phenol", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition (2) "Cyclohexanol and Cyclohexanone", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition Keywords: Hexanedioic Acid, Ketone/Alcohol Oil, Alkylation, Oxidation, Cumene, Cumene Hydroperoxide, CHP, KA Oil, Cyclohexanone, Cyclohexanol

Hydrogen Production from Vaccumm Residue - Cost Analysis - Hydrogen E61A

Hydrogen Production from Vaccumm Residue - Cost Analysis - Hydrogen E61A
Author: Intratec
Publisher: Intratec
Total Pages: 102
Release: 2019-09-17
Genre: Business & Economics
ISBN:

This report presents a cost analysis of Hydrogen production from vacuum residue. The process examined is a typical non-catalytic partial oxidation process. This process uses as raw material the bottom product from a vacuum distillation unit, known as vacuum residue. This report was developed based essentially on the following reference(s): Keywords: H2, Water-gas Shifting, Reformer, Non-catalytic Partial Oxidation

Caprolactam Production from Toluene - Cost Analysis - Caprolactam E61A

Caprolactam Production from Toluene - Cost Analysis - Caprolactam E61A
Author: Intratec
Publisher: Intratec
Total Pages: 102
Release: 2019-09-17
Genre: Business & Economics
ISBN:

This report presents a cost analysis of Caprolactam production from toluene. The process examined involves the following steps: toluene is oxidized to benzoic acid; benzoic acid is hydrogenated to hexahydrobenzoic acid; and hexahydrobenzoic acid is converted to caprolactam. This report was developed based essentially on the following reference(s): Keywords: SNIA, Viscosa, Oxidation, Hydrogenation, Lactam, Caproic Acid

Polycarbonate Production from Phenol - Cost Analysis - PC E61A

Polycarbonate Production from Phenol - Cost Analysis - PC E61A
Author: Intratec
Publisher: Intratec
Total Pages: 102
Release: 2019-09-17
Genre: Business & Economics
ISBN:

This report presents a cost analysis of Polycarbonate (PC) production from phenol, phosgene and acetone. The process examined is a typical melt process. In this process, the Polycarbonate plant is integrated with a plant for bisphenol A (BPA) production from phenol and acetone and a plant for diphenyl carbonate (DPC) production from phenol and phosgene. The process is based on the transesterification reaction of BPA with diphenyl carbonate to produce Polycarbonate. This report was developed based essentially on the following reference(s): Keywords: Thermoplastic Polymer, Polycondensation, SABIC, Mitsubishi, Asahi

Benzene Production from Heavy Aromatics - Cost Analysis - Benzene E61A

Benzene Production from Heavy Aromatics - Cost Analysis - Benzene E61A
Author: Intratec
Publisher: Intratec
Total Pages: 102
Release: 2019-09-17
Genre: Business & Economics
ISBN:

This report presents a cost analysis of Benzene production from toluene and heavy aromatics. The process examined is a typical transalkylation process. In this process, mixed xylenes are generated as by-product. This report was developed based essentially on the following reference(s): (1) US Patent 9006125, issued to Exxonmobil in 2015 (2) US Patent 5942651, issued to Mobil Oil in 1999 Keywords: TA, BTX, Aromatics, UOP Tatoray, Toray, ExxonMobil TransPlus, Chinese Petroleum Corporation, CPC, Axens, KBR ATA, Advanced TransAlkylation, GTC GT-TransAlk

Methionine Hydroxy Analog Production Process - Cost Analysis - Methionine E61A

Methionine Hydroxy Analog Production Process - Cost Analysis - Methionine E61A
Author: Intratec
Publisher: Intratec
Total Pages: 102
Release: 2017-06-01
Genre: Business & Economics
ISBN: 1641480289

This report presents a cost analysis of Methionine Hydroxy Analog production from acrolein, methyl mercaptan, and hydrogen cyanide (HCN) The process examined is similar to a process developed by Novus. In this process methional is produced from acrolein and methyl mercaptan. The methional reacts with hydrogen cyanide to produce hydroxy methylthiobutyronitrile (HMBN) intermediate, which is hydrolyzed to Methionine Hydroxy Analog. The product is recovered from the reaction medium via a solvent extraction. This report was developed based essentially on the following reference(s): (1) US Patent 6458997B2, issued to Novus International, Inc. in 2002 (2) US Patent 6320076, issued to Novus International, Inc. in 2001 Keywords: MHA, HMTBA, HMBN, 3-Methylmercapto Propionaldehyde, MMP, Methional, Propenal, Methanethiol, Essential Amino Acid

Renewable Diesel from Soybean Oil - Cost Analysis - Diesel E61A

Renewable Diesel from Soybean Oil - Cost Analysis - Diesel E61A
Author: Intratec
Publisher: Intratec
Total Pages: 102
Release: 2019-09-17
Genre: Business & Economics
ISBN:

This report presents a cost analysis of Renewable Diesel production from soybean oil. The process examined is similar to Neste Oil NExBTL process. In this process, propane is generated as by-product. This report was developed based essentially on the following reference(s): Keywords: Fatty Acid Methyl Ester, FAME, Glycerin, Transesterification, Refined Vegetable Oil, Deglycerolization