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Butanol Production From Propylene And Syngas Cost Analysis Butanol E71a
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Book Synopsis Butanol Production from Propylene and Syngas - Cost Analysis - Butanol E71A by : Intratec
Download or read book Butanol Production from Propylene and Syngas - Cost Analysis - Butanol E71A written by Intratec and published by Intratec. This book was released on 2019-09-17 with total page 102 pages. Available in PDF, EPUB and Kindle. Book excerpt: This report presents a cost analysis of n-Butanol production from propylene and syngas. The process examined is similar to the technology jointly developed by Rhodia (former Rhône-Poulenc) and Ruhrchemie. This process relies on a water-soluble rhodium catalyst for the hydroformylation of propylene to form n-butyraldehyde and isobutyraldehyde. 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, Rhodia, Rhône-Poulenc, Ruhrchemie
Book Synopsis Butanol Production from Propylene and Syngas - Cost Analysis - Butanol E21A by : Intratec
Download or read book Butanol Production from Propylene and Syngas - Cost Analysis - Butanol E21A written by Intratec and published by Intratec Solutions. This book was released on 2016-05-01 with total page 52 pages. Available in PDF, EPUB and Kindle. Book excerpt: 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 licensed by JM Davy and Dow, employing Selector 30 catalyst. In this process, the production ratio of n- to iso-butyraldehyde in the oxo reaction is about 30. The isobutyraldehyde is separated as a by-product and the n-butyraldehyde is hydrogenated to form n-Butanol 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) Keywords: Oxo Alcohol, Butyl Alcohol, n-Butanol, Johnson Matthey, Dow, LP Oxo, SELECTOR
Book Synopsis Butanol Production from Propylene and Syngas - Cost Analysis - Butanol E61A by : Intratec
Download or read book Butanol Production from Propylene and Syngas - Cost Analysis - Butanol E61A written by Intratec and published by Intratec. This book was released on 2019-09-17 with total page 102 pages. Available in PDF, EPUB and Kindle. Book excerpt: 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
Book Synopsis Butanol Production from Ethanol - Cost Analysis - Butanol E31A by : Intratec
Download or read book Butanol Production from Ethanol - Cost Analysis - Butanol E31A written by Intratec and published by Intratec. This book was released on 2019-09-17 with total page 102 pages. Available in PDF, EPUB and Kindle. Book excerpt: This report presents a cost analysis of n-Butanol production from ethanol. In this process, ethanol is dimerized into n-Butanol via the Guerbet reaction. This report was developed based essentially on the following reference(s): (1) US Patent 20160326075A1, issued to Abengoa Bionergia Nuevas Tecnlogias SA in 2016 (2) US Patent 9018426, issued to Celanese International Corporation in 2015 (3) US Patent 8318990, issued to Mitsubishi Chemcal Corporation in 2012 Keywords: Dimerization, Mitsubishi Chemical Corporation, Dimeric Alcohol
Book Synopsis Bio-Butanol Production from Corn - Cost Analysis - Butanol E11A by : Intratec
Download or read book Bio-Butanol Production from Corn - Cost Analysis - Butanol E11A written by Intratec and published by Intratec Solutions. This book was released on 2019-09-17 with total page 102 pages. Available in PDF, EPUB and Kindle. Book excerpt: This report presents a cost analysis of bio-based Butanol production from corn. The process examined is a typical Acetone-Butanol-Ethanol (ABE) fermentation process. In this process, acetone and ethanol are generated as by-products. This report was developed based essentially on the following reference(s): Tao, L., et al., "Comparative techno-economic analysis and reviews of n-butanol production from corn grain and corn stover", Biofuels, Bioprod. Bioref. 8:342–361, 2014 Keywords: Butyl Alcohol, Biomass, Biofuel, Milling
Book Synopsis Techno-economic Analysis of Butanol Production Through Acetone-butanol-ethanol Fermentation by : Nawa Raj Baral
Download or read book Techno-economic Analysis of Butanol Production Through Acetone-butanol-ethanol Fermentation written by Nawa Raj Baral and published by . This book was released on 2016 with total page 357 pages. Available in PDF, EPUB and Kindle. Book excerpt: Butanol is a next generation liquid biofuel, which can be produced through acetone-butanol-ethanol (ABE) fermentation using lignocelluloses including agricultural residues, forest residues, and energy crops. While butanol is superior to ethanol in terms of fuel properties, its commercial production is still encumbering due to low product yield, energy intensive recovery method and butanol toxicity to microbes. However, recent developments of simultaneous saccharification, fermentation and recovery techniques have potential to reduce these problems and improve butanol yield. Before commercial deployment, these recent developments on ABE fermentation technology require a thorough assessment of techno-economic feasibilities and bottlenecks. Thus, the main objective of this research was to assess the techno-economic feasibility of a biorefinery producing 113.5 million liters per year (30 million gallons per year) butanol through ABE fermentation. This study compared different components of butanol production system including feedstock supply logistics, pretreatment, fermentation and recovery, and stillage utilization methods. All the techno-economic models were developed in modeling software-SuperPro Designer. Different process and operating parameters for different components were gathered from existing literature and used as the main input to the models. Corn stover feedstock supply logistics cost ($/metric ton, dry) was estimated to be 112.1 when corn stover feedstock was assumed to be directly transported from field edge to biorefinery. This mode of feedstock transportation was found to be feasible for the biorefinery capacity considered in this study. Sulfuric acid pretreatment was found to be the most economic process with sugar production cost ($/kg) of 0.42 when compared to other most common pretreatment processes considered in this study such as steam explosion, ammonia fiber explosion, ionic liquid and biological. Based on current state of these different recovery methods, such as conventional distillation, vacuum recovery, gas stripping and liquid-liquid extraction, the lower butanol production cost ($/L) of 1.27 ($1.54/L-gasoline equivalent) was found under gas stripping recovery method. Other recovery methods require further research and development efforts to be competitive with gas stripping. Moreover, estimated stillage processing cost ($/L-butanol produced) of direct combustion system and fast pyrolysis system were found to be 0.15 and 0.17, respectively. Based on current state of technology, stillage utilization with direct combustion was found to be an economic stillage utilization method due to the lower stillage utilization cost. Integrating the most economic options discussed so far, the butanol production cost ($/L) at 95 % confidence interval was found to be 0.69-1.57 and 1.34-2.53 with and without considering byproducts’ credit, respectively. Energy conversion efficiency for the overall butanol production process was about 53.83 %. With further improvement in butanol yield of 30 g/100 g fermentable sugars, 98 wt% butanol recovery, glucose and xylose yield of 90 g/100 g initial glucan and xylan, feedstock supply cost of $64/metric ton (dry) and commercial selling value for acetone of $0.79/L, butanol production cost through ABE fermentation could be reduced to $0.47/L-butanol ($0.57/L-gasoline equivalent). This cost is very optimistic at present state of technology, which requires further research and development efforts to be economically competitive with last two years average corn ethanol cost of $0.37/L ($0.55/L-gasoline equivalent) and last 15 years average gasoline price of $0.65/L.
