http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-20000005331-A

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http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C17-21
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http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-26
filingDate 1997-04-04-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_01c4e03b0f458aad4df8c1d2aec802f4
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_539af6e15c9e73695a39c4906a20438f
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_f722821d65998fb303bafaa3e2a895b8
publicationDate 2000-01-25-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber KR-20000005331-A
titleOfInvention Process for producing halogenated propane containing fluorine substituted in terminal carbon
abstract The process of the invention discloses a process for the preparation of compounds of formula CF 3 CHXCF 3-z Y z , wherein X and Y are independently selected from the group consisting of H and Cl, z is 0 or 1. The process of the invention comprises (1) a compound of formula CCl 3 CHXCCl 3-z Y z , a compound of formula CCl 2-z Y z = CXCCl 3 , a compound of formula CCl 2 = CXCCl 3-z Y z , wherein X And Y is independently selected from the group consisting of H and Cl, z is 0 or 1) and a starting material selected from the group consisting of mixtures thereof in contact with hydrogen fluoride at a temperature of less than 200 ° C. (It is a saturated compound of the formula C 3 HXY z Cl 6-zx F x and an olefin compound of the formula C 3 XY Z Cl 5-Zy F y , wherein x is an integer of 1 to 6-z, and y is 1 To at least 90 mole% of a compound selected from the group consisting of 1 to 5-z, and up to about 40 mole% of CF 3 CHXCF 3-z Y z ;n n n (2) vapor-contacting hydrogen fluoride with a compound selected from the group consisting of the saturated compound prepared in step (1) and the olefinic compound at a temperature of 200 ° C. to about 400 ° C. in the presence of a fluorination catalyst; Andn n n (3) a sufficient amount of the saturated compound prepared in step (1) (where x is an integer of 1 to 5-z) and the olefinic compound at a temperature of 200 ° C. to about 400 ° C. in the presence of a vapor phase fluorination catalyst Vapor phase reacting with hydrogen to provide a total selectivity to at least about 90% of CF 3 CHXCF 3-z Y z based on the amount of starting material reacted with HF in steps (1) and (2).
isCitedBy http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-20130115287-A
priorityDate 1996-04-10-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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