pubmed-article:10863018 | rdf:type | pubmed:Citation | lld:pubmed |
pubmed-article:10863018 | lifeskim:mentions | umls-concept:C0006701 | lld:lifeskim |
pubmed-article:10863018 | lifeskim:mentions | umls-concept:C0038777 | lld:lifeskim |
pubmed-article:10863018 | lifeskim:mentions | umls-concept:C0009264 | lld:lifeskim |
pubmed-article:10863018 | lifeskim:mentions | umls-concept:C0443286 | lld:lifeskim |
pubmed-article:10863018 | lifeskim:mentions | umls-concept:C2603343 | lld:lifeskim |
pubmed-article:10863018 | lifeskim:mentions | umls-concept:C1709845 | lld:lifeskim |
pubmed-article:10863018 | pubmed:issue | 1 | lld:pubmed |
pubmed-article:10863018 | pubmed:dateCreated | 2000-9-8 | lld:pubmed |
pubmed-article:10863018 | pubmed:abstractText | A quantitative study of the influence of inlet sulfur dioxide concentration (600-3000 ppm), relative humidity (20-60%), reactor temperature (56-86 degrees C) and different amounts (0-30 wt.%) of inorganic additives (NaCl, CaCl(2) and NaOH) on gas desulfurization has been carried out in a continuous downflow fixed-bed reactor containing calcium hydroxide diluted with silica sand. Results show that the reaction rate does not depend on sulfur dioxide partial pressure (zero-order kinetics) and that the temperature and the relative humidity have a positive influence on reaction rate. An apparent activation energy of 32 kJ/mol Ca(OH)(2) has been estimated for the reaction. An empirical reaction rate equation at 71.5 degrees C and 36.7% relative humidity that includes the type and amount of additive is proposed. It has been found that calcium chloride is the best additive studied because it allows for a higher degree of sulfur dioxide removal. | lld:pubmed |
pubmed-article:10863018 | pubmed:language | eng | lld:pubmed |
pubmed-article:10863018 | pubmed:journal | http://linkedlifedata.com/r... | lld:pubmed |
pubmed-article:10863018 | pubmed:citationSubset | IM | lld:pubmed |
pubmed-article:10863018 | pubmed:chemical | http://linkedlifedata.com/r... | lld:pubmed |
pubmed-article:10863018 | pubmed:chemical | http://linkedlifedata.com/r... | lld:pubmed |
pubmed-article:10863018 | pubmed:chemical | http://linkedlifedata.com/r... | lld:pubmed |
pubmed-article:10863018 | pubmed:chemical | http://linkedlifedata.com/r... | lld:pubmed |
pubmed-article:10863018 | pubmed:status | MEDLINE | lld:pubmed |
pubmed-article:10863018 | pubmed:month | Aug | lld:pubmed |
pubmed-article:10863018 | pubmed:issn | 0304-3894 | lld:pubmed |
pubmed-article:10863018 | pubmed:author | pubmed-author:TejeroJJ | lld:pubmed |
pubmed-article:10863018 | pubmed:author | pubmed-author:IborraMM | lld:pubmed |
pubmed-article:10863018 | pubmed:author | pubmed-author:IzquierdoJ... | lld:pubmed |
pubmed-article:10863018 | pubmed:author | pubmed-author:FitéCC | lld:pubmed |
pubmed-article:10863018 | pubmed:author | pubmed-author:CunillFF | lld:pubmed |
pubmed-article:10863018 | pubmed:issnType | Print | lld:pubmed |
pubmed-article:10863018 | pubmed:day | 28 | lld:pubmed |
pubmed-article:10863018 | pubmed:volume | 76 | lld:pubmed |
pubmed-article:10863018 | pubmed:owner | NLM | lld:pubmed |
pubmed-article:10863018 | pubmed:authorsComplete | Y | lld:pubmed |
pubmed-article:10863018 | pubmed:pagination | 113-23 | lld:pubmed |
pubmed-article:10863018 | pubmed:dateRevised | 2009-11-3 | lld:pubmed |
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pubmed-article:10863018 | pubmed:year | 2000 | lld:pubmed |
pubmed-article:10863018 | pubmed:articleTitle | Kinetic study of the reaction between sulfur dioxide and calcium hydroxide at low temperature in a fixed-bed reactor. | lld:pubmed |
pubmed-article:10863018 | pubmed:affiliation | Chemical Engineering Department, Faculty of Chemistry, University of Barcelona, C/ Martí i Franqués 1, 08028, Barcelona, Spain. felipe@angel.qui.ub.es | lld:pubmed |
pubmed-article:10863018 | pubmed:publicationType | Journal Article | lld:pubmed |
pubmed-article:10863018 | pubmed:publicationType | Research Support, Non-U.S. Gov't | lld:pubmed |