http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-H09505587-A
Outgoing Links
Predicate | Object |
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classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01F33-30 |
classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B11-064 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B11-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C29-66 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07D301-26 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07D301-26 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C33-42 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C29-66 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01B11-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01B11-06 |
filingDate | 1994-11-09-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationDate | 1997-06-03-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | JP-H09505587-A |
titleOfInvention | Method of adjusting alkylene oxide |
abstract | (57) [Summary] (1) Optionally, contacting a metal hydroxide or oxide with chlorine to form a metal hypochlorite solution; (2) at least 80 based on hypochlorite. Contacting chlorine with a solution of a metal hypochlorite at a temperature of less than 60 ° C. and a pH of less than 5.5 with sufficient micromixing to obtain the product hypochlorous acid in mol% yield. (3) Step of separating at least a part of hypochlorous acid from an aqueous metal chloride solution of hypochlorous acid called chloride chloride brine, in which case at least 30 mol% of hypochlorous acid is in a liquid phase Solution is desorbed into the vapor phase in equilibrium of hypochlorous acid and dichlorine monoxide from the solution of the vapor stream as droplets having a volume median diameter of less than 500 microns. Spray into; (4) distill residual liquid phase Step of obtaining additional vapor of hypochlorous acid and dichlorine monoxide; (5) Absorption of hypochlorous acid and dichlorine monoxide in low chloride water to produce low chloride hypochlorous acid aqueous solution And (6) a continuous method using a continuous stirred tank reactor for maintaining a uniform steady-state HOCl concentration of 0.2% by weight or less in the reactor, using a low chloride hypochlorous acid aqueous solution as an olefin. Contacting to form the corresponding olefin chlorohydrin; (7) optionally contacting the olefin chlorohydrin with a base to form the corresponding alkylene oxide and salt solution; and (8) optionally salt Separating the alkylene oxide from the solution; (9) optionally chlorine from the chloride brine obtained from at least one of step 3 or step 4 by contacting the chlorate with an acid to convert it to chlorine. Step retrieve the salt; a and (10) optionally including the step of at least 1 Tsueto recirculation step 1 or step 4 chlorate, process for the preparation of an alkylene oxide. By the process according to the invention, alkylene oxides are obtained in particularly high yields, substantially without the formation of by-products. |
isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2016204175-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2008231073-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2010536561-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2001335520-A |
priorityDate | 1993-11-23-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 145.