Download Free Butadiene Production From Ethanol Cost Analysis Butadiene E31a Book in PDF and EPUB Free Download. You can read online Butadiene Production From Ethanol Cost Analysis Butadiene E31a and write the review.

This report presents a cost analysis of 1,3-Butadiene (BD) production from hydrous ethanol. This process consists of a two-stage reaction process. First, ethanol reacts to produce acetaldehyde and then, the acetaldehyde intermediate is reacted with ethanol to produce 1,3-Butadiene. Raffinate is generated as by-product in the process. This report was developed based essentially on the following reference(s): (1) Burla, J., et al., "Two-Step Production of 1,3-Butadiene from Ethanol", University of Pennsylvania, 2012 (2) US Patent 2403741, issued to Carbide & Carbon Chemicals in 1946 Keywords: Ethyl Alcohol, BD, Tubular Reactor, Fixed-Bed Reactor
This report presents a cost analysis of Polypropylene (PP) Random Copolymer production from polymer grade (PG) propylene and ethylene using a bulk phase polymerization process. The process examined is similar to the processes LyondellBasell Spheripol and Mitsui Hypol II. This process is based on the polymerization of liquid PG propylene and PG ethylene in loop reactors. 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): Keywords: PG Propylene, Propene, Tubular Reactor, Liquid-Phase Polymerization
This report presents a cost analysis of Epichlorohydrin production from glycerol. This process is composed of an glycerol hypochlorination coupled with an alkaline epoxidation. 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: Allyl chloride hypochlorination, alkaline epoxidation, CONSER, Spolchemie
This report presents a cost analysis of Vinyl Chloride production from acetylene and hydrochloric acid. The process examined is a typical acetylene hydrochlorination process. In this process, anhydrous hydrogen chloride is reacted in vapor phase with acetylene over a mercuric chloride catalyst producing Vinyl 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: Chloroethene, 1,2-Dichloroethane, Hydrochlorination
This report presents a cost analysis of Homopolymer High Density Polyethylene (HDPE) production starting from polymer grade (PG) ethylene using a slurry loop process. The process described is a slurry loop reactor process, similar to Chevron Phillips CPChem and INEOS Innovene S. In this study, it is considered a single loop reactor polymerization for production of homopolymer HDPE. 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): US Patent 20140256889A1, issued to Chevron Phillips Chemical Company Keywords: Ethene, PE, Loop Reactor, Slurry Reactor, Homopolymer
This report presents a cost analysis of Linear Low Density Polyethylene (LLDPE) production from polymer grade (PG) ethylene and 1-butene using a gas phase process. The process examined is similar to Univation UNIPOL and INEOS Innovene G processes. 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 8957167, issued to Univation in 2015; (2) US Patent 20030171512, issued to Univation in 2003 Keywords: Ethene, PE, Gas Reactor, Copolymer
This report presents a cost analysis of bio-based 1,3-Butadiene (BD) production from glucose syrup using a direct fermentation process. In this process, a 70 wt% glucose-water syrup is used as raw material in an anaerobic fermentation step for Butadiene production. This report was developed based essentially on the following reference(s): Keywords: BD, Dextrose, Glucose Fermentation, Anaerobic Fermentation, Sugarcane, Corn, Green Butadiene, Renewable Feedstock
This report presents a cost analysis of 1,3-Butadiene production from carbon monoxide using a two-step process. The process examined is similar to LanzaTech/Invista process. First, carbon monoxide (CO) is fermented forming 2,3-butanediol (BDO). Then, BDO is catalytically converted to 1,3-Butadiene (BD). Methyl ethyl ketone (MEK) and ethanol are generated as by-products. This report was developed based essentially on the following reference(s): (1) US Patent 20130316412, issued to LanzaTech in 2013 (2) US Patent 9452963 issued to Toray Industries in 2016 Keywords: Orochem, SMB, PNNL, SK Innovation, CO-derived BDO, Bio-Butadiene, Thermo-Catalytic Conversion
This report presents a cost analysis of 1,3-Butadiene production from a crude C4s stream using an extraction process The process examined is similar to Nippon Zeon's crude C4 extractive distillation process. In this process, dimethyl-formamide is used as a solvent in order to extract 1,3-Butadiene from the crude C4 stream, also producing fuel byproduct. This report was developed based essentially on the following reference(s): Keywords: Extractive Distillation, Crude C4s, dimethyl-formamide, C4 Acetylene
This report presents a cost analysis of 1,3-Butadiene (BD) production from n-butane using a dehydrogenation process. The process examined is similar to CB&I Lummus Catadiene process. In the process, n-butane undergoes a dehydrogenation reaction generating a C4s stream containing 1,3-Butadiene. High purity 1,3-Butadiene is obtained after conventional separation steps and an extractive distillation, using n-methylpyrrolidone (NMP) as solvent. Unreacted butane and butenes recovered are recycled to the dehydrogenation. This report was developed based essentially on the following reference(s): (1) "Butadiene," Ullmann's Encyclopedia of Industrial Chemistry, 7th edition (2) "Butadiene, General," Encyclopedia of Chemical Processing and Design Keywords: Houdry Catadiene, Sud-Chemie, Catalytic Dehydrogenation, BD, Fixed-Bed Reactor, BASF, NMP extraction