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Butanol Production From Propylene And Syngas Cost Analysis Butanol E61a
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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 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 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.
Book Synopsis Process Synthesis and Process Intensification by : Ben-Guang Rong
Download or read book Process Synthesis and Process Intensification written by Ben-Guang Rong and published by Walter de Gruyter GmbH & Co KG. This book was released on 2017-09-25 with total page 477 pages. Available in PDF, EPUB and Kindle. Book excerpt: Process synthesis and process intensification are becoming state-of-the-art scientific fields that provide the methods and tools to improve process technologies in terms of high energy efficiency, low capital investment, low emissions, improved safety, and less hazardous byproducts to achieve sustainable products and processes. The book covers manufacturing processes from both fossil- and biomass-based feedstocks for graduate students.
Book Synopsis Chemorheology of Polymers by : Peter J. Halley
Download or read book Chemorheology of Polymers written by Peter J. Halley and published by Cambridge University Press. This book was released on 2009-05-28 with total page 445 pages. Available in PDF, EPUB and Kindle. Book excerpt: Understanding the dynamics of reactive polymer processes allows scientists to create new, high-value, high-performance polymers. This book is an indispensable resource for researchers and practitioners working in this area. It includes coverage of thermoplastics, thermoset and reactive polymers, together with practical industrial processes and modern chemorheological models and tools.
Book Synopsis Advances in Regenerative Medicine by : Sabine Wislet
Download or read book Advances in Regenerative Medicine written by Sabine Wislet and published by BoD – Books on Demand. This book was released on 2011-11-21 with total page 420 pages. Available in PDF, EPUB and Kindle. Book excerpt: Even if the origins of regenerative medicine can be found in Greek mythology, as attested by the story of Prometheus, the Greek god whose immortal liver was feasted on day after day by Zeus' eagle; many challenges persist in order to successfully regenerate lost cells, tissues or organs and rebuild all connections and functions. In this book, we will cover a few aspects of regenerative medicine highlighting major advances and remaining challenges in cellular therapy and tissue/organ engineering.
Author :Fernando Israel Gómez-Castro Publisher :Walter de Gruyter GmbH & Co KG ISBN 13 :3110596121 Total Pages :338 pages Book Rating :4.1/5 (15 download)
Book Synopsis Process Intensification by : Fernando Israel Gómez-Castro
Download or read book Process Intensification written by Fernando Israel Gómez-Castro and published by Walter de Gruyter GmbH & Co KG. This book was released on 2019-10-21 with total page 338 pages. Available in PDF, EPUB and Kindle. Book excerpt: Intensified processes have found widespread application in the chemical and petrochemical industries. The use of intensified systems allows for a reduction of operating costs and supports the “greening” of chemical processes. However, the design of intensified equipment requires special methodologies. This book describes the fundamentals and applications of these design methods, making it a valuable resource for use in both industry and academia.
Book Synopsis Applications in Design and Simulation of Sustainable Chemical Processes by : Alexandre C. Dimian
Download or read book Applications in Design and Simulation of Sustainable Chemical Processes written by Alexandre C. Dimian and published by Elsevier. This book was released on 2019-08-08 with total page 754 pages. Available in PDF, EPUB and Kindle. Book excerpt: Applications in Design and Simulation of Sustainable Chemical Processes addresses the challenging applications in designing eco-friendly but efficient chemical processes, including recent advances in chemistry and catalysis that rely on renewable raw materials. Grounded in the fundamental knowledge of chemistry, thermodynamics, chemical reaction engineering and unit operations, this book is an indispensable resource for developing and designing innovating chemical processes by employing computer simulations as an efficient conceptual tool. Targeted to graduate and post graduate students in chemical engineering, as well as to professionals, the book aims to advance their skills in process innovation and conceptual design. The work completes the book Integrated Design and Simulation of Chemical Processes by Elsevier (2014) authored by the same team. Includes comprehensive case studies of innovative processes based on renewable raw materials Outlines Process Systems Engineering approach with emphasis on systematic design methods Employs steady-state and dynamic process simulation as problem analysis and flowsheet creation tool Applies modern concepts, as process integration and intensification, for enhancing the sustainability
Book Synopsis Advanced Distillation Technologies by : Anton A. Kiss
Download or read book Advanced Distillation Technologies written by Anton A. Kiss and published by John Wiley & Sons. This book was released on 2013-02-26 with total page 301 pages. Available in PDF, EPUB and Kindle. Book excerpt: Distillation has historically been the main method for separating mixtures in the chemical process industry. However, despite the flexibility and widespread use of distillation processes, they still remain extremely energy inefficient. Increased optimization and novel distillation concepts can deliver substantial benefits, not just in terms of significantly lower energy use, but also in reducing capital investment and improving eco-efficiency. While likely to remain the separation technology of choice for the next few decades, there is no doubt that distillation technologies need to make radical changes in order to meet the demands of the energy-conscious society. Advanced Distillation Technologies: Design, Control and Applications gives a deep and broad insight into integrated separations using non-conventional arrangements, including both current and upcoming process intensification technologies. It includes: Key concepts in distillation technology Principles of design, control, sizing and economics of distillation Dividing-wall column (DWC) – design, configurations, optimal operation and energy efficient and advanced control DWC applications in ternary separations, azeotropic, extractive and reactive distillation Heat integrated distillation column (HIDiC) – design, equipment and configurations Heat-pump assisted applications (MVR, TVR, AHP, CHRP, TAHP and others) Cyclic distillation technology – concepts, modeling approach, design and control issues Reactive distillation – fundamentals, equipment, applications, feasibility scheme Results of rigorous simulations in Mathworks Matlab & Simulink, Aspen Plus, Dynamics and Custom Modeler Containing abundant examples and industrial case studies, this is a unique resource that tackles the most advanced distillation technologies – all the way from the conceptual design to practical implementation. The author of Advanced Distillation Technologies, Dr. Ir. Anton A. Kiss, has been awarded the Hoogewerff Jongerenprijs 2013. Find out more (website in Dutch)...
Book Synopsis Process Intensification and Integration for Sustainable Design by : Dominic C. Y. Foo
Download or read book Process Intensification and Integration for Sustainable Design written by Dominic C. Y. Foo and published by John Wiley & Sons. This book was released on 2020-12-01 with total page 344 pages. Available in PDF, EPUB and Kindle. Book excerpt: Presents comprehensive coverage of process intensification and integration for sustainable design, along with fundamental techniques and experiences from the industry Drawing from fundamental techniques and recent industrial experiences, this book discusses the many developments in process intensification and integration and focuses on increasing sustainability via several overarching topics such as Sustainable Manufacturing, Energy Saving Technologies, and Resource Conservation and Pollution Prevention Techniques. Process Intensification and Integration for Sustainable Design starts discussions on: shale gas as an option for the production of chemicals and challenges for process intensification; the design and techno-economic analysis of separation units to handle feedstock variability in shale gas treatment; RO-PRO desalination; and techno-economic and environmental assessment of ultrathin polysulfone membranes for oxygen-enriched combustion. Next, it looks at process intensification of membrane-based systems for water, energy, and environment applications; the design of internally heat-integrated distillation column (HIDiC); and graphical analysis and integration of heat exchanger networks with heat pumps. Decomposition and implementation of large-scale interplant heat integration is covered, as is the synthesis of combined heat and mass exchange networks (CHAMENs) with renewables. The book also covers optimization strategies for integrating and intensifying housing complexes; a sustainable biomass conversion process assessment; and more. Covers the many advances and changes in process intensification and integration Provides side-by-side discussions of fundamental techniques and recent industrial experiences to guide practitioners in their own processes Presents comprehensive coverage of topics relevant, among others, to the process industry, biorefineries, and plant energy management Offers insightful analysis and integration of reactor and heat exchanger network Looks at optimization of integrated water and multi-regenerator membrane systems involving multi-contaminants Process Intensification and Integration for Sustainable Design is an ideal book for process engineers, chemical engineers, engineering scientists, engineering consultants, and chemists.
Book Synopsis Organic Rankine Cycles for Waste Heat Recovery by : Silvia Lasala
Download or read book Organic Rankine Cycles for Waste Heat Recovery written by Silvia Lasala and published by BoD – Books on Demand. This book was released on 2020-05-13 with total page 122 pages. Available in PDF, EPUB and Kindle. Book excerpt: This book comprises five chapters on developed research activities on organic Rankine cycles. The first section aims to provide researchers with proper modelling (Chapter 1) and experimental (Chapter 2) tools to calculate and empirically validate thermophysical properties of ORC working fluids. The second section introduces some theoretical and experimental studies of organic Rankine cycles for waste heat recovery applications: a review of different supercritical ORC (Chapter 3), ORC for waste heat recovery from fossil-fired power plants (Chapter 4), the experimental detailed characterization of a small-scale ORC of 3 kW operating with either pure fluids or mixtures (Chapter 5).
