http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CS-265109-B1
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_1a086d7d05c65d71f47a094d2b6f6a8d http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_9629d03d070e97f6ef2863f12e8ca7d9 http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_8fc7280d0c803e23ee63b7c2383a992a http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_66174db8a09b66fdd6db8bc4c544e65b http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_92a71140722485ff12649818604ae46a |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-34 |
| filingDate | 1987-01-03-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_100bdb388d79438090772c34008ab718 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_5bcef605b08498fa31e8c4ab30956e05 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_74bfb9ecaa769d6fd6fdf49454453bb5 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_269ec7a7312070db265a2a4d7132d653 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_4b339d7643712273922c5f418503517e |
| publicationDate | 1989-10-13-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CS-265109-B1 |
| titleOfInvention | Method of dry removal of sulfur oxides, hydrogen fluoride and hydrogen chloride from flue gases and waste gases containing water vapor |
| abstract | Method of dry removal of sulfur oxidesnhydrogen fluoride and hydrogen chloride from flue gas and waste gasngases containing water vapor contactingnwith calcium oxide or hydroxide particles,nbeing at concentrationnCO2 in gases is less than 0.1% volnsuitable sorption range of SO2 250 to 500 ° Cnpreferably 350 to 450 ° C, in the presence of concentrationsnCO2 above 0.1% by volume is appropriatenwithin the SO2 capture temperature range of 250 ton350 ° C, with NOX to SO2 concentration rationin the range of 0.1 to 1, a temperature range is suitablentrapping SO 2 at 150 to 350 ° C, preferablyn200 to 300 ° C, in the presence of HCl and or HFnin gases at volume concentrations belown0.5% is the appropriate SO2 sorption temperature rangenHCl and HF 200 to 400 ° C, preferably 250 to 400 ° Cn350 ° C. The procedure can be used for removalnSOX and optionally HF and HCl from flue gasnpower plants, heating plants, and incinerators;nremoving SOX, HF and HCl from waste roastersncolor metallurgy gases - such as roasting,nagglomeration, melting and electrolysis |
| priorityDate | 1987-01-03-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 40.