http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CA-1102328-A
Outgoing Links
Predicate | Object |
---|---|
assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_d669af06cb2abbcd6823699582a97002 |
classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D1-18 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01F25-72 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01F23-405 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07D251-28 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01F23-511 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01F3-12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01F3-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01F5-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07D251-28 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D1-18 |
filingDate | 1979-11-19-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate | 1981-06-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c5fff5838a10e083c483c25228e67ba6 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_788246b2d9b8187adb80d34d3e29544d http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_58efff9addc5517b84a304e63fa6feb6 |
publicationDate | 1981-06-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | CA-1102328-A |
titleOfInvention | Process for producing suspensions or solutions of cyanuric chloride in organic solvents |
abstract | ABSTRACT OF THE DISCLOSURE The invention relates to the production of suspensions or solutions of cyanuric chloride in aqueous organic solvents at high speeds of mixing and low production temperatures and thus with a low degree of hydrolysis by injecting liquid cyanuric chloride through a nozzle, which is installed in the upper end of a mixing device, in a countercurrent to the solvent which rises upwards from a nozzle or nozzles and is injected above the breast-like taper in the lower open end of the apparatus. The chamber walls thus are always covered with an uninterrupted liquid layer. The process can be carried out at standard pressure as well as at excess pressure or at negative gauge pressure. At negative gauge pressure the system is cooled by evaporation of the solvent. |
priorityDate | 1978-11-20-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 41.