(33a) ITM Syngas: Ceramic Membrane Technology for Lower Cost Conversion of Natural Gas | AIChE

(33a) ITM Syngas: Ceramic Membrane Technology for Lower Cost Conversion of Natural Gas

Authors 

Repasky, J. M. - Presenter, Air Products and Chemicals, Inc.
Carolan, M. F. - Presenter, Air Products and Chemicals, Inc.
Studer, D. W. - Presenter, Air Products and Chemicals, Inc.
Lowe, C. M. - Presenter, Chevron Energy Technology Company
Gerdes, K. F. - Presenter, Chevron Energy Technology Company
Smit, J. - Presenter, Sasol Technology (Pty) Ltd
Bremen, B. - Presenter, Sasol Technology (Pty) Ltd


The ITM Syngas Team, led by Air Products and including Chevron, Sasol, Ceramatec, and other partners, in collaboration with the U.S. Department of Energy, is developing Ion Transport Membrane (ITM) technology for the production of synthesis gas, a mixture of hydrogen and carbon monoxide. The ITM Syngas process is a breakthrough technology that combines air separation and high-temperature synthesis gas generation processes into a single ceramic membrane reactor, with potential for significant savings in the capital cost of synthesis gas production. Because synthesis gas is a feedstock for a range of different processes, ITM Syngas represents a technology platform that has numerous applications, such as hydrogen, clean fuels and chemicals. ITM ceramic membranes are fabricated from non-porous, mixed-metal oxides and operate with exceptionally high oxygen flux and selectivity. Oxygen from low-pressure air permeates, as oxygen ions, through the ceramic membrane and is consumed through chemical reactions, thus creating a chemical driving force that pulls oxygen ions across the membrane at high rates. The oxygen reacts with natural gas in a partial oxidation process to produce synthesis gas. Significant advances continue to be made in developing and scaling up the ITM Syngas technology. This paper describes technical advances in development and testing of commercial-size ceramic membranes and the ITM Syngas reactor system. Recent laboratory and pilot unit test results will be discussed. A summary of recent GTL process optimization and economic analysis will also be presented.

Acknowledgement/Disclaimer This technology has been supported in part by the U. S. Department of Energy under Contract Number DE-FC26-97FT96052. The Government reserves for itself and others acting on its behalf a royalty-free, nonexclusive, irrevocable, worldwide license for governmental purposes to publish, distribute, translate, duplicate, exhibit and perform this copyrighted paper. A significant portion of this report was prepared by Air Products and Chemicals, Inc. pursuant to a Cooperative Agreement partially funded by the United States Department of Energy, and neither Air Products and Chemicals, Inc. nor any of its contractors or subcontractors nor the United States Department of Energy, nor any person acting on behalf of either: 1. Makes any warranty or representation, express or implied, with respect to the accuracy, completeness, or usefulness of the information contained in this report, or that the use of any information, apparatus, method, or process disclosed in this report may not infringe privately owned rights; or 2. Assumes any liabilities with respect to the use of, or for damages resulting from the use of, any information, apparatus, method, or process disclosed in this report. Reference herein to any specific commercial products, process, or service by trade name, trademark, manufacturer, or otherwise, does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States Department of Energy. The views and opinions of authors expressed herein do not necessarily state or reflect those of the United States Department of Energy.

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