Predicate |
Object |
assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_9c2b8ddf635d74accbd24d3a867392ea http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_952c09bc4f0d744d5747bfaa2b3492aa http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_a2a99738c564d0d4da77d442ec8f7500 http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_2cc6c67f1d6f405081587f35c21c1055 |
classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00826 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-00026 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00049 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00761 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2229-186 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00822 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00873 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00835 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00783 |
classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F28D9-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F28F3-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F28D9-0062 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C1-042 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F28F3-025 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-0093 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C1-0435 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-023 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J23-8913 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-334 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-1019 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-008 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J29-7669 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J23-75 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J29-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-0006 |
classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F28D9-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-89 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J19-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G2-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C27-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J35-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J35-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J35-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C1-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-75 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J29-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F28F3-00 |
filingDate |
2014-03-19-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate |
2015-12-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_11aa39378761e1283fdf4af783d899dc http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_53cd9ce75971dfab2d7255c2dd1ac895 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_820aeb75ed35617020c28a5ae0e7267d |
publicationDate |
2015-12-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber |
US-9206091-B2 |
titleOfInvention |
Processes and systems for synthesis gas conversion using a hybrid fischer-tropsch catalyst in a compact heat exchange reactor |
abstract |
Disclosed are a process and a system for synthesis gas conversion. The process includes contacting a synthesis gas feed of hydrogen and carbon monoxide having a H 2 /CO ratio from 0.5 to 3.0 with a hybrid catalyst of particles having a particle size from 50 to 500 μm and having at least one zeolite and a Fischer-Tropsch component wherein the ratio of zeolite to Fischer-Tropsch component is from 0.1:1 to 30:1 and the hybrid catalyst includes from 0.5 to 40 wt % Fischer-Tropsch component. The process is conducted in a compact heat exchange reactor having a set of reaction passages disposed between a synthesis gas feed header and a products header and a set of coolant passages disposed between a coolant inlet header and a coolant outlet header. The set of coolant passages conducts a coolant therethrough, and the set of reaction passages contains the hybrid catalyst therein and conducts synthesis gas and reaction products therethrough. The process is conducted at a temperature from 200 to 2800° C., a pressure from 5 to 40 atmospheres, a recycle ratio from 1 to 3, and a gaseous hourly space velocity less than 20,000 volumes of gas per volume of catalyst per hour. The effluent produced includes a hydrocarbon product containing at least 50 wt % C 5+ hydrocarbons and less than 5 wt % C 21+ hydrocarbons at a C 5+ productivity from 0.05 to 2 g C5+ /g cat /h. |
priorityDate |
2013-05-14-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type |
http://data.epo.org/linked-data/def/patent/Publication |