Abstract
An innovative scheme to separate hydrogen from coal gasification products for end users such as clean energy production is presented. The main approach of this process was the use of catalysts (Me) in a fixed bed reactor that will increase hydrogen purity by CO disproportionation that yields in elemental carbon and CO2. The resulting CO2 immediately reacted with specially modified calcium based component that acts as a CO2 removal material, thus producing carbon-based-gases-free hydrogen. The addition of steam enhanced the efficiency of steam removal. The efficiency of separation did not decrease as a result of one-enrichment-regeneration cycle. The product of this system would result into hydrogen ready for use in fuel cells. This is an abstract of a paper presented at the 2005 AIChE Annual Meeting and Fall Showcase (Cincinnati, OH 10/30/2005-11/4/2005).
| Original language | English |
|---|---|
| Title of host publication | 05AIChE |
| Subtitle of host publication | 2005 AIChE Annual Meeting and Fall Showcase, Conference Proceedings |
| Publisher | American Institute of Chemical Engineers |
| ISBN (Print) | 0816909962, 9780816909964 |
| Publication status | Published - 2005 |
| Event | 05AIChE: 2005 AIChE Annual Meeting and Fall Showcase - Cincinnati, OH, United States Duration: 30 Oct 2005 → 4 Nov 2005 |
Publication series
| Name | AIChE Annual Meeting Conference Proceedings |
|---|---|
| Volume | 2005 |
Conference
| Conference | 05AIChE: 2005 AIChE Annual Meeting and Fall Showcase |
|---|---|
| Country/Territory | United States |
| City | Cincinnati, OH |
| Period | 30/10/05 → 4/11/05 |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 7 Affordable and Clean Energy
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SDG 13 Climate Action
ASJC Scopus subject areas
- General Energy
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