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Catalytic for Chemical Manufacture

Award Information
Agency: Department of Energy
Branch: N/A
Contract: DE-FG02-06ER84576
Agency Tracking Number: 80855S06-I
Amount: $750,000.00
Phase: Phase II
Program: SBIR
Solicitation Topic Code: 22
Solicitation Number: DE-FG01-05ER05-28
Timeline
Solicitation Year: 2006
Award Year: 2007
Award Start Date (Proposal Award Date): N/A
Award End Date (Contract End Date): N/A
Small Business Information
12345 W. 52nd Ave.
Wheat Ridge, CO 80033
United States
DUNS: 181947730
HUBZone Owned: No
Woman Owned: No
Socially and Economically Disadvantaged: No
Principal Investigator
 Girish Srinivas
 Dr
 (303) 940-2300
 gsrinivas@tda.com
Business Contact
 John Wright
Title: Mr
Phone: (303) 940-2300
Email: jdwright@tda.com
Research Institution
N/A
Abstract

Sulfuric acid, which is used primarly in the manufacture of phosphate fertilizers, is produced in greater volume than any other industrial chemical. Sulfuric acid is made by first burning sulfur to produce SO2, reacting the SO2 over a catalyst to produce SO3, and then absorbing the SO3 into water to produce the acid. Conversion in the catalytic process is limited by equilibrium ¿ if the process can be operated at a lower temperature, the conversion of SO2 to SO3 could be increased. TDA has developed a novel low temperature catalyst for the oxidation of sulfur dioxide for sulfuric acid manufacture. This project will demonstrate the effectiveness of a new catalyst operates at temperatures 50-80°C lower than commercial catalysts, thereby providing greater per-pass conversion of sulfur dioxide to sulfur trioxide. Phase I synthesized and tested a series of catalysts and compared their activity with several commercially available catalysts. The new catalyst significantly outperformed the commercial catalysts at the lower temperatures and was stable in a preliminary lifetime test. An economic analysis indicated that the slightly increased cost of the new catalyst would be more than offset by its benefits. In Phase II, the catalyst will be further improved by examining both the composition and preparation method. In order to ensure good catalyst lifetime, an automated test system, which can run unattended for weeks at a time, will be designed and built. Test data will first be used to provide feedback to the catalyst optimiztion task, and then to test the catalyst¿s durability. Finally, we will determine the cost of manufacturing the catalyst followed by an economic analysis of using the catalyst for sulfuric acid manufacturing. Commercial Applications and Other Benefits as described by the awardee: A low temperature sulfur dioxide oxidation catalyst should substantially lower energy use in sulfuric acid manufacture while increasing throughput and lowering sulfur emissions. Increasing the conversion rate would reduce the amount of feedstock used, increase the energy efficiency of the sulfuric acid plant, and significantly lower sulfur emissions.

* Information listed above is at the time of submission. *

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