Propylene Production From Propane Cost Analysis Propylene E33a
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| Author | : Intratec |
| Publisher | : Intratec Solutions |
| Total Pages | : 53 |
| Release | : 2016-03-01 |
| Genre | : Business & Economics |
| ISBN | : 1945324252 |
This report presents a cost analysis of Polymer Grade (PG) Propylene production from propane using a dehydrogenation process. The process examined is similar to Uhde STAR process. In this process, Propylene is produced through two dehydrogenation steps: a steam reforming step followed by oxyreaction. 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 7678956, issued to Uhde in 2010 Keywords: PG Propylene, Steam Active Reforming, Thyssenkrupp, Propene, PDH, On-Purpose Propylene Production
| Author | : Intratec |
| Publisher | : Intratec |
| Total Pages | : 102 |
| Release | : 2019-09-17 |
| Genre | : Business & Economics |
| ISBN | : |
This report presents a cost analysis of Polymer Grade (PG) Propylene production from propane using a dehydrogenation process. The process examined is similar to Uhde STAR process. In this process, Propylene is produced through two dehydrogenation steps: a steam reforming step followed by oxyreaction. Hydrogen is also generated as a by-product. This report was developed based essentially on the following reference(s): (1) US Patent 7678956, issued to Uhde in 2010 (2) US Patent 5389342, issued to Pillips in 1995 (assigned to Uhde in 2001) Keywords: PG Propylene, Steam Active Reforming, Thyssenkrupp, Propene, PDH, On-Purpose Propylene Production
| Author | : Intratec |
| Publisher | : Intratec Solutions |
| Total Pages | : 53 |
| Release | : 2016-03-01 |
| Genre | : Business & Economics |
| ISBN | : 1945324244 |
This report presents a cost analysis of Polymer Grade (PG) Propylene production from propane using a dehydrogenation process. The process examined is similar to CB&I Lummus CATOFIN process. In this process, the dehydrogenation reaction is carried out in a fixed-bed reactor. 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 20120014846, issued to Lummus Technology in 2012; (2) US Patent 8101541, issued to Sud-Chemie in 2012 Keywords: PG Propylene, Clariant, Sud-Chemie, Propene, PDH, On-Purpose Propylene Production
| Author | : Intratec Solutions |
| Publisher | : |
| Total Pages | : 54 |
| Release | : 2016-03 |
| Genre | : |
| ISBN | : 9781945324215 |
This report presents alternatives for producing PG Propylene from different feedstocks and a cost comparison of these alternatives, across different countries. More specifically, the report compares the costs of PG Propylene production through the following pathways:* Pathway 1: Propylene Production from Light Naphtha* Pathway 2: Propylene Production from Ethylene and Butenes* Pathway 3: Propylene Production from Propane (with Hydrogen Generation)Pathway 1 corresponds to a steam cracker for Propylene production (ethylene as co-product). In Pathway 2, Propylene is produced via metathesis reaction of ethylene with 2-butene (present in raffinate-2 feedstock). In Pathway 3, propane is dehydrogenated to Propylene with hydrogen generated being valued as fuel. The analysis presented in this report includes:* A comparison of the economic potential of the pathways listed above in several countries, comprising: * Comparative analysis of capital costs * Comparative analysis of production costs * Comparison between product price and raw materials costs of each pathway * An overview of each production pathway, including: * Raw material(s) consumption figures and product(s) generated * Related technology licensors and block flow diagram of representative industrial processes Keywords: Propene, Ethene, Steam Cracking, PDH, Propane Dehydrogenation, Olefins Conversion Technology, OCT
| Author | : Intratec |
| Publisher | : Intratec Solutions |
| Total Pages | : 52 |
| Release | : 2016-03-01 |
| Genre | : Business & Economics |
| ISBN | : |
This is a free full sample report offered by Intratec Solutions to demonstrate, in advance, the type of information you will get when you buy one of our reports, offering the same standard and structure (types of graphs, tables and descriptions) that you will find in all of our Cost Analysis Overview reports. This report presents alternatives for producing PG Propylene from different feedstocks and a cost comparison of these alternatives, across different countries. More specifically, the report compares the costs of PG Propylene production through the following pathways: * Pathway 1: Propylene Production from Light Naphtha * Pathway 2: Propylene Production from Ethylene and Butenes * Pathway 3: Propylene Production from Propane (with Hydrogen Generation) Pathway 1 corresponds to a steam cracker for Propylene production (ethylene as co-product). In Pathway 2, Propylene is produced via metathesis reaction of ethylene with 2-butene (present in raffinate-2 feedstock). In Pathway 3, propane is dehydrogenated to Propylene with hydrogen generated being valued as fuel. The analysis presented in this report includes: * A comparison of the economic potential of the pathways listed above in several countries, comprising: - Comparative analysis of capital costs - Comparative analysis of production costs * Comparison between product price and raw materials costs of each pathway - An overview of each production pathway, including: - Raw material(s) consumption figures and product(s) generated - Related technology licensors and block flow diagram of representative industrial processes Keywords: Propene, Ethene, Steam Cracking, PDH, Propane Dehydrogenation, Olefins Conversion Technology, OCT
| Author | : Intratec |
| Publisher | : Intratec Solutions |
| Total Pages | : 102 |
| Release | : 2019-09-17 |
| Genre | : Business & Economics |
| ISBN | : |
This report presents a cost analysis of Polymer Grade (PG) Propylene production from propane using a dehydrogenation process. The process examined is similar to UOP Oleflex process. In this process, the dehydrogenation reaction is carried out in a moving-bed reactor. This report was developed based essentially on the following reference(s): (1) US Patent 20120108877, issued to UOP in 2012 (2) US Patent 5457256, issued to UOP in 1995 Keywords: PG Propylene, Continuous Catalyst Regeneration, CCR, Propene, PDH, On-Purpose Propylene Production
| Author | : Intratec |
| Publisher | : Intratec Solutions |
| Total Pages | : 82 |
| Release | : 2013-03-26 |
| Genre | : Technology & Engineering |
| ISBN | : 148395112X |
The growing exploitation of shale gas in the United States raised the propane availability, reducing its prices. This, coupled with growing demand for propylene, made of the propane dehydrogenation (PDH) a promising alternative for on-purpose propylene production. The technical aspects of a PDH process similar to the Lummus CATOFIN technology are reviewed. The analysis also includes estimates for both the capital investment and the operating costs of typical plants on the US Gulf Coast and in China. This study follows the same pattern as all Technology Economics studies developed by Intratec. About Technology Economics Technology Economics studies are advisory services ordered by leading chemical companies, which are disclosed to public after an agreeded upon period of time. All Technology Economics studies are based on the same rigorous methodology and well-defined structure, encompassing: Process flow diagrams and material balances Raw material and utility consumptions Major equipment sizing Inside and outside battery limits capital costs Detailed fixed and variable manufacturing expenses
| Author | : Ka Ng |
| Publisher | : Butterworth-Heinemann |
| Total Pages | : 512 |
| Release | : 2001-11 |
| Genre | : |
| ISBN | : 9780750671347 |
| Author | : Intratec |
| Publisher | : Intratec Solutions |
| Total Pages | : 52 |
| Release | : 2016-03-02 |
| Genre | : Business & Economics |
| ISBN | : 1945324279 |
This report presents a cost analysis of Polymer Grade (PG) Propylene production from refinery grade (RG) propylene. The process examined consists of a typical purification process. In this process, a propane stream is generated as by-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): "Propene", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition Keywords: PG Propylene, Propene, RG Propylene, Distillation, P-P Splitter
| Author | : Stanley M. Walas |
| Publisher | : Butterworth-Heinemann |
| Total Pages | : 689 |
| Release | : 2013-10-22 |
| Genre | : Science |
| ISBN | : 1483145085 |
Phase Equilibria in Chemical Engineering is devoted to the thermodynamic basis and practical aspects of the calculation of equilibrium conditions of multiple phases that are pertinent to chemical engineering processes. Efforts have been made throughout the book to provide guidance to adequate theory and practice. The book begins with a long chapter on equations of state, since it is intimately bound up with the development of thermodynamics. Following material on basic thermodynamics and nonidealities in terms of fugacities and activities, individual chapters are devoted to equilibria primarily between pairs of phases. A few topics that do not fit into these categories and for which the state of the art is not yet developed quantitatively have been relegated to a separate chapter. The chapter on chemical equilibria is pertinent since many processes involve simultaneous chemical and phase equilibria. Also included are chapters on the evaluation of enthalpy and entropy changes of nonideal substances and mixtures, and on experimental methods. This book is intended as a reference and self-study as well as a textbook either for full courses in phase equilibria or as a supplement to related courses in the chemical engineering curriculum. Practicing engineers concerned with separation technology and process design also may find the book useful.
