Crude Isophthalic Acid Production Process Cost Analysis Ipa E21a
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Crude Isophthalic Acid Production Process - Cost Analysis - IPA E21A by Intratec Pdf
This report presents a cost analysis of Crude Isophthalic Acid production from m-xylene. The process examined is a typical oxidation process. In this process, p-xylene is oxidized to Isophthalic Acid. The Isophthalic Acid is then separated from the solvent as a Crude Isophthalic Acid (CIA). No further process for purification via hydrogenation is included in this process. This report was developed based essentially on the following reference(s): Keywords: Unsaturated Polyester, UPR, Phthalic Acid, Meta-Xylene, CIA
Purified Isophthalic Acid Production Process - Cost Analysis - IPA E11A by Intratec Pdf
This report presents a cost analysis of Purified Isophthalic Acid (PIA) production from m-xylene. The process examined is a typical oxidation process. In this process, p-xylene is oxidized to Isophthalic Acid. The Isophthalic Acid from reaction is separated as a Crude Isophthalic Acid (CIA) intermediate. The CIA is subjected to purification via hydrogenation in order to obtain PIA as the final product. This report was developed based essentially on the following reference(s): Keywords: Unsaturated Polyester, UPR, Phthalic Acid, Meta-Xylene, PIA
Isophthalic Unsaturated Polyester Production Process - Cost Analysis - UPR E11A by Intratec Pdf
This report presents a cost analysis of Isophthalic Unsaturated Polyester Resin (UPR) production. The process examined is a typical batch process. Resin formulation is mainly based on the following compounds: isophthalic acid, maleic anhydride, propylene glycol and styrene. This report was developed based essentially on the following reference(s): Keywords: UPR, Eastman Chemical, Aldol Reaction, IPA, MAN
Terephthalic Unsaturated Polyester Production Process - Cost Analysis - UPR E21A by Intratec Pdf
This report presents a cost analysis of Terephthalic Unsaturated Polyester Resin (UPR) production. The process examined is a typical batch process. Resin formulation is mainly based on the following compounds: maleic anhydride, diethylene glycol, recycled polyethylene terephthalate (PET), propylene glycol and styrene. This report was developed based essentially on the following reference(s): Keywords: UPR, Eastman Chemical, Aldol Reaction, PET, MAN, DEG
Medium-Purity Terephthalic Acid Production - Cost Analysis - TPA E11A by Intratec Pdf
This report presents a cost analysis of Medium-Purity Terephthalic Acid (MTA) production from p-xylene. The process examined is a typical catalytic oxidation process. In this process, p-xylene is oxidized to Terephthalic Acid. Subsequently, the Terephthalic Acid is crystallized and recovered from the liquor and MTA is obtained 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) This report was developed based essentially on the following reference(s): "Terephthalic Acid, Dimethyl Terephthalate, and Isophthalic Acid", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition Keywords: Para-xylene, TPA, Post-Oxidation Reactor, Mitsubishi, Eastman, Lurgi, Medium Quality, QTA, EPTA
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
Isopropyl Alcohol Production from PG Propylene - Cost Analysis - Isopropanol E21A by Intratec Pdf
This report presents a cost analysis of Isopropanol production from polymer grade (PG) propylene. The process examined is a typical direct propylene hydration process. In this process, both PG propylene and water are reacted in vapor phase to form Isopropanol. This report was developed based essentially on the following reference(s): Keywords: Isopropanol, isopropyl alcohol, IPA, direct propylene hydration,
Terephthalic Acid Production from p-Xylene - Cost Analysis - TPA E12A by Intratec Pdf
This report presents a cost analysis of Purified Terephthalic Acid (PTA) production from p-xylene. The process examined is a conventional catalytic oxidation process. In this process, p-xylene is oxidized to Terephthalic Acid. The Terephthalic Acid from reaction passes through separation and drying steps and Crude Terephthalic Acid (CTA) is obtained as an intermediate. Subsequently, the CTA is subjected to purification via hydrogenation and PTA is separated 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) This report was developed based essentially on the following reference(s): (1) "Terephthalic Acid, Dimethyl Terephthalate, and Isophthalic Acid", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition; (2) EP Patent 0824653, issued to DuPont in 2000 Keywords: Para-xylene, Paraxylene, TPA, CTA, Hydrogenation, Amoco, Catalytic Oxidation, Acetic Acid, BP, X Technology, PET, Polyethylene Terephthalate, Bromine
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
Methacrylic Acid Production from Isobutane - Cost Analysis - MAA E21A by Intratec Pdf
This report presents a cost analysis of Methacrylic Acid (MAA) production starting from isobutane. The process examined is similar to UOP Oleflex process, combined with a typical oxidation process. In this process, the dehydrogenation step is carried out in a moving-bed reactor. This report was developed based essentially on the following reference(s): Keywords: Isobutene, Clariant, Sud-Chemie, Unsaturated Polyester, UPR, MAA, i-Butylene
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
2-Ethylhexanol Production from Butyraldehyde - Cost Analysis - 2-EH E21A by Intratec Pdf
This report presents a cost analysis of 2-Ethylhexanol production starting from n-butyraldehyde and hydrogen In this process, n-butyraldehyde is first condensed to 2-ethylpropilacrolein and then reacted with hydrogen to form 2-Ethylhexanol. This report was developed based essentially on the following reference(s): Keywords: Oxo Alcohol, Butyl Alcohol, Condensation, Hydrogenation, H2, 2-Ethylhexanol