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This report presents a cost analysis of Sebacic Acid production from castor oil and sodium hydroxide. The process examined is a typical caustic oxidation process. This report was developed based essentially on the following reference(s): Keywords: Decanedioic Acid, Dicarboxylic Acid, 1,8-Octanedicarboxylic Acid
This report presents a cost analysis of Itaconic Acid production from dimethyl succinate (DMS) and formaldehyde. The process examined is based on a catalytic condensation. In this process, succinic acid is generated as by-product. This report was developed based essentially on the following reference(s): US Patent 6664417, issued to Board of Trustees of Michigan State University in 2003 Keywords: Methylenesuccinic Acid, Succinic Acid Methyl Ester, Succinic Anhydride, Formalin, Citraconate, Citraconic Anhydride
This report presents a cost analysis of Polyethylene Terephthalate (PET) production from ethylene glycol and purified terephthalic acid (PTA). The process examined is similar to Invista NG3 process. In this process, PET oligomers are first polymerized in a melt-phase step, and then passed through a solid-state polymerization step. This report was developed based essentially on the following reference(s): US Patents 5786443 and 5730913, both issued to DuPont in 1998 (both assigned to Invista in 2004) Keywords: Thermoplastic Polymer, Polyester, High Intrinsic Viscosity, Melt-Phase Polycondensation
This report presents a cost analysis of Bisphenol A (BPA) production from phenol and acetone. In this process, BPA is produced by the condensation reaction of acetone with phenol. The reaction is catalyzed by hydrogen chloride. 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) Keywords: Carbolic Acid, Propanone, Hooker Chemical, Occidental Chemical, OxyChem
This report presents a cost analysis of 2-Ethylhexanol (2-EH) production from propylene and syngas. The process examined is similar to the LP OXO Selector technology jointly licensed by JM Davy and Dow. 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) Keywords: oxo alcohol, oxo process
This report presents a cost analysis of a typical Aluminium Chloride production process from aluminium metal and chlorine. In the process, chlorine gas is passed through molten aluminium powder in ceramic lined tube shaped reactors, producing Aluminium Chloride. 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) Keywords: Aluminum Trichloride, Aluminium Scrap, Anhydrous Aluminium Chloride
This report presents a cost analysis of High Density Polyethylene (HDPE) bimodal production from polymer grade (PG) ethylene and 1-butene using a slurry process. The process examined is similar to LyondellBasell Hostalen process. 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): LyondellBasell, "Licensed Polyolefin Technologies and Services - Hostalen" Keywords: Ethene, Bimodal, Multimodal, CSTR, Advanced Cascade Process, ACP, Butylene
This report presents a cost analysis of Linear Low Density Polyethylene (LLDPE) production from polymer grade (PG) ethylene and 1-octene using a solution process. The process under analysis is similar to NOVA Chemicals SCLAIRTECH process. 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): EP Patent 0527144, issued to DuPont in 1996 Keywords: Ethene, DuPont Canada, Cyclohexane, Stirred-Reactor, Swing Technology, Multi-Reactor
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
This report presents a cost analysis of Lactic Acid production from glucose syrup using a fermentation process. The process examined is similar to Corbion process. In this process, a 70 wt% glucose-water syrup is used as raw material. The fermentation broth is acidified in order to recover Lactic Acid and the product purification is realized by the use of a solvent. An 88 wt% Lactic Acid solution in water is generated as 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) US Patent 7867736, issued to Purac (now Corbion) in 2011; (2) US Patent 6747173, issued to Purac (now Corbion) in 2004 Keywords: Dextrose, 2-Hydroxypropanoic Acid, Anaerobic Fermentation, Calcium Carbonate, Sulfuric Acid