Acetic Acid Production From Methanol Cost Analysis Acetic Acid E21a
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Acetic Acid Production from Methanol - Cost Analysis - Acetic Acid E21A by Intratec Pdf
This report presents a cost analysis of Acetic Acid production from methanol and carbon monoxide The process examined is a typical carbonylation process. In this process, the carbonylation is promoted by an iodide rhodium liquid catalyst. The liquid product is sent to a set of distillation columns to recover the Acetic Acid. This report was developed based essentially on the following reference(s): (1) "Acetic Acid", Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition (2) US Patent 6458996, issued to BP Chemicals in 2002 Keywords: Ethanoic Acid, Monsanto, Iodomethane
Acetaldehyde Production from Acetic Acid - Cost Analysis - Acetaldehyde E21A by Intratec Pdf
This report presents a cost analysis of Acetaldehyde production from acetic acid. The process examined is a typical hydrogenation process. In this process, ethyl acetate is generated as by-product. This report was developed based essentially on the following reference(s): Keywords: Ethanal, Eastman Chemical, Acetic Acid Ethyl Ester
Acetic Anhydride from Acetic Acid and Acetone - Cost Analysis - Acetic Anhydride E21A by Intratec Pdf
This report presents a cost analysis of Acetic Anhydride production from acetic acid and acetone. The process examined is carried out in two steps: the pyrolysis of acetone to ketene; and the reaction of ketene with acetic acid to produce Acetic Anhydride. This report was developed based essentially on the following reference(s): Keywords: Ethanoic Anhydride, Ketene Absorption
Acetic Acid Production from Acetaldehyde - Cost Analysis - Acetic Acid E11A by Intratec Pdf
This report presents a cost analysis of Acetic Acid production from acetaldehyde and oxygen The process examined is a typical liquid-phase oxidation process. In this process, the oxidation occurs with manganous acetate as catalyst. Unreacted acetaldehyde is condensed and recycled back to the reactor. The liquid product is sent to a set of distillation columns to recover the Acetic Acid. This report was developed based essentially on the following reference(s): Keywords: Ethanoic Acid, Ethanal, Oxidation Reaction, Liquid-Phase Oxidation, Air
Acrylic Acid Production from Glycerol - Cost Analysis - Acrylic Acid E21A by Intratec Pdf
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
Acetic Acid Production from Ethane - Cost Analysis - Acetic Acid E31A by Intratec Pdf
This report presents a cost analysis of Acetic Acid production from ethane. In this process, ethane is oxidized forming Acetic Acid. This report was developed based essentially on the following reference(s): Keywords: Ethane Direct Oxidation, EDO, SABIC, Saudi Arabia Basic Industries Corporation
Polyoxymethylene from Methanol and Acetic Anhydride - Cost Analysis - POM E21A by Intratec Pdf
This report presents a cost analysis of Polyacetal Resins (also known as Polyoxymethylene, POM) production starting from methanol and acetic anhydride The process examined is a conventional silver-catalyzed process with methanol recycle, combined with one owned by DuPont for producing the POM. In this process, methanol is converted to Formaldehyde (37wt% solution) over a silver catalyst. The formaldehyde (37wt% solution) is concentrated to a purity higher than 99.9wt% by means of two distillation steps and a treatment step. High purity formaldehyde is then polymerized in an inert cyclohexane medium. This report was developed based essentially on the following reference(s): (1) "Formaldehyde", Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition (2) "Acetal Resins", Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition (3) US Patent 2768994, issued to Du Pont in 1956 Keywords: Acetyl resin, polyoxymethylene (POM) resins, polymer of formaldehyde, DuPont, polyformaldehyde, Formalin, silver catalyst, Uhde Inventa Fischer, EMS, formaldehyde solution, incomplete conversion
Vinyl Acetate from Acetic Acid and Acetylene - Cost Analysis - VAM E21A by Intratec Pdf
This report presents a cost analysis of Vinyl Acetate Monomer (VAM) from acetic acid and acetylene In the process examined, acetic acid and acetylene react in the vapor phase in the presence of a supported metal catalyst to produce vinyl acetate. This report was developed based essentially on the following reference(s): (1) "Vinyl Esters," Ullmann's Encyclopedia of Industrial Chemistry, 7th edition (2) US Patent 3415872, issued to Blaw Knox in 1968 Keywords: Ethenyl Acetate, Ethanoic Acid, Acetylene, Wacker
Ethyl Acetate Production from Ethanol - Cost Analysis - Ethyl Acetate E21A by Intratec Pdf
This report presents a cost analysis of Ethyl Acetate production from ethanol. The process examined is similar to the Johnson Matthey's DAVY ethyl acetate technology. In this process, Ethyl Acetate is produced in a two‐stage reaction: ethanol is dehydrogenated to acetaldehyde, which further reacts with ethanol to form Ethyl Acetate. This report was developed based essentially on the following reference(s): (1) US Patent 6,632,330 issued to Davy Process Technology Limited (2) US Patent 6,809,217 issued to Davy Process Technology Limited Keywords: Dehydrogenation, Ethyl Acetate, EA, DPT, Johnson Matthey
Methanol Production from Syngas - Cost Analysis - Methanol E21A by Intratec Pdf
This report presents a cost analysis of Methanol production starting from synthesis gas (syngas). In the process examined, the methanol synthesis is carried out in a dual reactor system, which consists in an isothermal reactor combined in series with a gas-cooled reactor. This report was developed based essentially on the following reference(s): Keywords: Methyl Alcohol, Catalytic Synthesis
Ethyl Acetate Production from Ethylene and Acid Acetic - Cost Analysis - Ethyl Acetate E31A by Intratec Pdf
This report presents a cost analysis of Ethyl Acetate production from ethylene and acetic acid. In this process, ethyl acetate is produced via a direct addition reaction of acetic acid to ethylene. The process under analysis is similar to two processes developed independently: the AVADA process, owned by INEOS and formerly owned by BP, and Showa Denko's Direct Addition Process. This report was developed based essentially on the following reference(s): US Patent 6,794,535 issued to BP Chemicals Limited Keywords: AVADA, Ethyl Acetate, EA, BP
Ethyl Acetate Production from Ethanol and Acid Acetic - Cost Analysis - Ethyl Acetate E11A by Intratec Pdf
This report presents a cost analysis of Ethyl Acetate production from ethanol and acid acetic. In this process, Ethyl Acetate is produced by continuous esterification of acetic acid and ethanol. This report was developed based essentially on the following reference(s): "Esterification", Enciclopedia of chemical technology, 5th edition Keywords: Esterification, Ethyl Acetate, Reactive Distillation
Polyethylene Furanoate Production from Glucose - Cost Analysis - PEF E21A by Intratec Pdf
This report presents a cost analysis of Polyethylene Furanoate (PEF) production starting from glucose and monoethylene glycol (MEG). The process examined is similar to the Avantium YXY process, followed by a process that copolymerizes FDCA and MEG. In this process, a 70 wt% glucose-water syrup feed is isomerized to fructose. Then, fructose is converted to methoxy methyl furan (MMF) intermediate, which is oxidized to FDCA. This process generates methyl acetate and methyl levulinate as by-products. The FDCA generated and MEG are polymerized to PEF in two polymerization steps in order to obtain Bottle-Grade PEF. This report was developed based essentially on the following reference(s): (1) US Patent 8519167, issued to Furanix Technologies B.V. in 2013 (2) US Patent 20160024039, issued to Furanix Technologies B.V. in 2016 (3) WO Patent 2015137807, issued to Furanix Technologies in 2015 Keywords: Polyethylene Furanoate, PEF, Green FDCA, Hydroxyl Methyl Furfural, HMF, Purified Terephthalic Acid, Polyethylene 2,5-Furandicarboxylate, MEG
Acetic Acid Production from Butane - Cost Analysis - Acetic Acid E41A by Intratec Pdf
This report presents a cost analysis of Acetic Acid production from n-butane. The process examined is an n-butane oxidation process. This report was developed based essentially on the following reference(s): Keywords: Ethanoic Acid, Celanese, Hoechst, Oxidation
Methanol Production from Natural Gas - Cost Analysis - Methanol E12A by Intratec Pdf
This report presents a cost analysis of large-scale Methanol production from natural gas. The process examined employs combined reforming for syngas generation similarly to the technologies developed by the following companies: Lurgi, Toyo, KBR, Johnson Matthey/Davy and Haldor-Topsoe. In this process, natural gas is converted into syngas in two steps: steam reforming and autothermal reforming. In the steam reformer, the natural gas reacts with steam and, in the secondary (autothermal) reformer, it reacts with oxygen. The syngas generated is then converted to Methanol. 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 8629190, issued to Lurgi in 2014; (2) US Patent 8388864, issued to Lurgi in 2013 Keywords: Synthesis Gas, Lurgi MegaMethanol, Johnson Matthey, JM Davy Technologies, Toyo, Kellogg Brown and Root, KBR, Johnson Matthey/Davy, Haldor-Topsoe