http://rdf.ncbi.nlm.nih.gov/pubchem/patent/GB-946830-A
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_9aa694d7d277529ddad12d81865f1b19 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B7-03 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B7-09 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B7-13 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B7-096 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01B7-13 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01B7-09 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01B7-03 |
| filingDate | 1960-08-23-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 1964-01-15-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | GB-946830-A |
| titleOfInvention | Halogen production |
| abstract | Halogens are produced by the oxidation of inorganic halides, e.g. hydrogen chloride, hydrogen bromide, hydrogen iodide, nitrosyl chloride, nitrosyl bromide, nitrosyl iodide, ammonium chloride and ammonium bromide, in the presence of a metal- or silica-containing oxidation catalyst and a dissimilar material comprising a clay desiccant having at least 0.5% by weight reversible water content and a crystalline structure up to at least 1400 DEG F. The catalyst which may be chromium sesquioxide, chromium, potassium chromate, cerium oxide, manganese dioxide, uranium trioxide, cupric chloride, a mixture of ferric oxide and ferric chloride, a mixture of chromium sesquioxide and alumina, calcium chloride or silica gel may be supported on a carrier, e.g. silica, alumina or pumice or on the clay desiccant. When copper chloride is employed as catalyst, an alkali metal salt, e.g. potassium chloride, or rare earth metal is preferably added. The clay is preferably a bentonitic clay such as montmorillonite, beidellite nontranite, hectorite, saponite or sauconite. The reaction is preferably carried out with the catalyst and clay in a fluid bed with countercurrent introduction of the gaseous and/or liquid materials comprising the oxidizing agent and inorganic halide although the solids may be disposed as fixed beds in a plurality of reaction zones with gaseous materials being introduced alternatively to each of the zones and with simultaneous regeneration of the solid material in the zone in which introduction of the reactants has been discontinued. The oxidation of the inorganic chloride is preferably carried out at a temperature of 600-1000 DEG F. at a pressure of 30-160 p.s.i.g. using molecular oxygen, air, ozone, nitric acid, oxides of nitrogen or peroxides as oxidizing agents. When the desiccant has absorbed 0.5-4% by weight of water the contact with the reactants may be discontinued and the clay may be regenerated by heating it to 950-1400 DEG F. under from atmospheric pressure to 150 p.s.i.g. for from 10 minutes to one hour in the presence of nitrogen gas. The absorption properties of the clay may be improved by partially activating it by leaching or boiling with hydrochloric or sulphuric acid. Specifications 584,790 and 676,667 are referred to. |
| isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-0134295-A1 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-5707919-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-4857295-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/EP-0711599-A1 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-9808785-A1 |
| priorityDate | 1959-09-01-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
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