Predicate |
Object |
assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_3a9a1d3b8056585cfcfb11600d9b9efa |
classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2257-702 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J2240-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-0446 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2256-16 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J2230-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-0495 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2256-24 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-048 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J2205-60 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J2205-40 |
classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B3-506 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-0655 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-047 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-002 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-062 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-064 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B3-56 |
classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-047 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F25J1-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F25J3-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01B3-50 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01B3-56 |
filingDate |
2002-12-17^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate |
2010-01-12^^<http://www.w3.org/2001/XMLSchema#date> |
inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_88dd160f1b7b97779fa646f66abd57ba |
publicationDate |
2010-01-12^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber |
US-7644595-B2 |
titleOfInvention |
Combined recovery of hydrogen and hydrocarbon liquids from hydrogen-containing gases |
abstract |
A pressure differential of a feed gas ( 110 ) between a compressor ( 120 ) and expander ( 160 ) is employed to cool the feed gas to condense and remove at least a portion of one component to produce a partially depleted feed gas from which another component may then be removed. In especially preferred aspects, the feed gas comprises C 2 -C 5 hydrocarbons and hydrogen, wherein the hydrocarbons are condensed in the cooler and hydrogen is removed using a pressure swing adsorption unit ( 180 ). |
isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2011203313-A1 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2018058753-A1 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-104896875-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2012167620-A1 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-104896875-B http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-10605522-B2 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2017222138-A1 |
priorityDate |
2001-12-18^^<http://www.w3.org/2001/XMLSchema#date> |
type |
http://data.epo.org/linked-data/def/patent/Publication |