http://rdf.ncbi.nlm.nih.gov/pubchem/patent/SU-1012958-A1
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_f66ef3531a6afd71d58af1d3fcf408d9 |
| classificationIPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01B17-04 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-14 |
| filingDate | 1981-01-09-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 1983-04-23-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_d5613575c5b33b89b8694eb73a227146 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_378cff079a6fe296c32bfb11457affb5 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_37c51781c5b4d710cb07ea650cfd7055 |
| publicationDate | 1983-04-23-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | SU-1012958-A1 |
| titleOfInvention | Method of processing hydrogen sulphide to elemental sulphur |
| abstract | 1. METHOD OF PROCESSING OF HYDROGEN HYDROGEN ON ELEMENTARY SULFUR, including: the absorption of hydrogen sulfide from the fuel gas with an aqueous solution. ammonium bisulfite sulfite, the regeneration of the saturated absorbent by contacting with a gas containing sulfur dioxide to obtain elemental sulfur, which is characterized by the fact that, in order to increase the sulfur yield and reduce the absorption of the absorbent, absorption is carried out first at the temperature TbO C, a then at 30-60 ° C and part of the resulting sulfur or serosoder. The burning compound is burned to produce a gas containing sulfur dioxide, and the honor of the saturated absorbent is evaporated in a gas stream formed by burning the source gas in a gas containing sulfur dioxide to form ammonium sulfite and returning it to the sorption stage. 2, the method according to claim 1, about tl and h ayush and with the fact that the saturated absorption bent for evaporation is fed in the amount of 100-500 g per 1. 3 .. The method according to Claims 1 and 2, that is, that the combustion of the source gas is carried out with an oxidant consumption rate equal to 0.951 .1. . |
| priorityDate | 1981-01-09-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 37.