Methanol Production From Natural Gas Cost Analysis Methanol E12a
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Author | : Intratec |
Publisher | : Intratec Solutions |
Total Pages | : 102 |
Release | : 2019-09-17 |
Genre | : Business & Economics |
ISBN | : |
This report presents a cost analysis of large-scale Methanol production from natural gas. The process examined employs combined reforming for syngas generation similarly to the technologies developed by the following companies: Lurgi, Toyo, KBR, Johnson Matthey/Davy and Haldor-Topsoe. In this process, natural gas is converted into syngas in two steps: steam reforming and autothermal reforming. In the steam reformer, the natural gas reacts with steam and, in the secondary (autothermal) reformer, it reacts with oxygen. The syngas generated is then converted to Methanol. This report was developed based essentially on the following reference(s): (1) US Patent 8629190, issued to Lurgi in 2014 (2) US Patent 8388864, issued to Lurgi in 2013 Keywords: Synthesis Gas, Lurgi MegaMethanol, Johnson Matthey, JM Davy Technologies, Toyo, Kellogg Brown and Root, KBR, Johnson Matthey/Davy, Haldor-Topsoe
Author | : Intratec |
Publisher | : Intratec |
Total Pages | : 102 |
Release | : 2019-09-17 |
Genre | : Business & Economics |
ISBN | : |
This report presents a cost analysis of Syngas (Synthesis Gas) production from natural gas. The process examined is a conventional steam reforming process. This report was developed based essentially on the following reference(s): Keywords: Methane, Carbon Monoxide, Steam Reforming, SMR
Author | : Intratec |
Publisher | : Intratec |
Total Pages | : 101 |
Release | : 2019-09-17 |
Genre | : Business & Economics |
ISBN | : |
This report presents a cost analysis of Hydrogen production from natural gas. The process examined is a typical partial oxidation process. In this process, natural gas passes through a thermal partial oxidation, generating carbon monoxide and hydrogen at ratios of approximately 2:1. In order to increase hydrogen output, the partial oxidation product is sent to a gas shift converter, to which steam is added to react with carbon monoxide, generating carbon dioxide and more hydrogen. Finally, the gaseous stream is purified in a pressure swing adsorber (PSA) and high-purity hydrogen is obtained. This report was developed based essentially on the following reference(s): "Hydrogen", Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition Keywords: H2, NG, POX, Catalytic Partial Oxidation, Texaco, Shell
Author | : Intratec |
Publisher | : Intratec |
Total Pages | : 102 |
Release | : 2017-06-01 |
Genre | : Business & Economics |
ISBN | : 1641480262 |
This report presents a cost analysis of large-scale Methanol production from natural gas The process examined is a typical arrangement based on conventional steam reforming of natural gas for syngas generation. Natural gas is sent to the steam reformer for producing syngas, which is then converted to Methanol. This report was developed based essentially on the following reference(s): "Methanol", Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition Keywords: Synthesis gas, conventional methanol process, large-scale methanol
Author | : Intratec |
Publisher | : Intratec Solutions |
Total Pages | : 101 |
Release | : 2019-09-17 |
Genre | : Business & Economics |
ISBN | : |
This report presents a cost analysis of large-scale Methanol production from natural gas. The process examined is similar to JM Catalysts LCM Process. In this process, natural gas passes through a gas heated reformer to be converted into syngas, which is then converted to Methanol. This report was developed based essentially on the following reference(s): (1) US Patent 7087652, issued to Johnson Matthey in 2006 (2) "Methanol", Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition Keywords: JM Catalysts, Leading Concept Methanol, autothermal reformer, gas heated reformer
Author | : A. Stratton |
Publisher | : |
Total Pages | : 70 |
Release | : 1982 |
Genre | : Chemical industry |
ISBN | : |
Author | : |
Publisher | : |
Total Pages | : 64 |
Release | : 1989 |
Genre | : Methanol as fuel |
ISBN | : |
Author | : A E. Hokanson |
Publisher | : |
Total Pages | : 26 |
Release | : 1977 |
Genre | : Alcohol as fuel |
ISBN | : |
Author | : Sunggyu Lee |
Publisher | : CRC Press |
Total Pages | : 254 |
Release | : 1989-12-04 |
Genre | : Science |
ISBN | : 9780849346101 |
This easy-to-read work is a comprehensive review which focuses primarily on catalytic methanol synthesis. It includes a historic summary of the development of methanol synthesis technology, as well as extensive discussions on statistical experimental design, fabrication and operation of laboratory scale systems. This unique volume also discusses various new catalysts and processes, with special attention to the thermodynamics of methanol synthesis-especially in relation to the new liquid phase process. The comprehensive and practical approach to chemical and synfuel process development makes it an excellent reference in methanol synthesis, reactor design, and scale-up. Written as a practical guide to researchers who are involved in hands-on process research, this book is also a valuable asset to practicing chemical engineers and graduate students interested in reaction engineering, thermodynamics, catalyst development and process design.
Author | : |
Publisher | : |
Total Pages | : |
Release | : 1991 |
Genre | : Methanol as fuel |
ISBN | : |
The Alternative Motor Fuels Act of 1988 (Public Law 100-494), Section 400EE, states that the Secretary of Energy ... shall study methanol plants, including the costs and practicability of such plants that are (A) capable of utilizing current domestic supplies of unutilized natural gas; (B) relocatable; or (C) suitable for natural gas to methanol conversion by natural gas distribution companies ... '' The purpose of this report is to characterize unutilized gas within the lower 48 states and to perform an economic analysis of methanol plants required by the act. The approach with regard to unutilized lower 48 gas is to (1) compare the costs of converting such gas to methanol against the expected price of gasoline over the next 20 years, and (2) compare the economics of converting such gas to methanol against the economics of using the gas as a pipeline-transported fuel. This study concludes that remote gas and low-Btu gas generally cannot be converted to methanol at costs near the expected competitive value of gasoline because of the poor economies of scale of small methanol plants.