Inventor
Robert B. James, Jr.
Inventor
Northbrook, IL, US
Overview
Patents· 52 as inventor
Public. Assignee & technology derived from the patent record. Each patent links to its LexDana page.
C10Gprimary
C10GCracking hydrocarbon oils23%
C07CAcyclic or carbocyclic compounds15%
A62DChemical means for extinguishing fires or for combating or protecting against harmful chemical agents10%
G21CNuclear reactors8%
Y02EReduction of greenhouse gas [ghg] emissions, related to energy generation, transmission or distribution8%
Y02PClimate change mitigation technologies in the production or processing of goods5%
B01JChemical or physical processes, e.g. catalysis or colloid chemistry4%
C01BNon-metallic elements4%
C10MLubricating compositions4%
B01DSeparation3%
PatentTitleYear
10,214,464Steady state high temperature reactor20199,809,662'Polypropylene production processes'20179,689,615'Steady state high temperature reactor'20179,239,385'Method of producing isotopes in power nuclear reactors'20169,202,598'Fail-free fuel bundle assembly'20158,953,731'Method of producing isotopes in power nuclear reactors'20158,842,801'Rod assembly for nuclear reactors'20148,603,399'Integrated oxygenate conversion and product cracking'20138,414,798'Processes and systems for producing syngas from methane'20138,128,887'Metal-based coatings for inhibiting metal catalyzed coke formation in hydrocarbon conversion processes'20128,009,791'Fuel supports for nuclear reactors'20117,935,324'Integrated warm gas desulfurization and gas shift for cleanup of gaseous streams'20117,781,637'Segmented waste rods for handling nuclear waste and methods of using and fabricating the same'20107,687,671'Integrated oxygenate conversion and product cracking'20107,638,040'Process for upgrading contaminated hydrocarbons'20097,577,230'Fuel support and method for modifying coolant flow in a nuclear reactor'20097,526,058'Rod assembly for nuclear reactors'20097,505,547'Assembly and method for mounting a fuel assembly having a predefined orientation within a nuclear reactor'20097,128,883'Process and apparatus for ethylbenzene production and transalkylation to xylene'20066,958,425'Aromatics transalkylation to ethylbenzene and xylenes'20056,855,854'Process and apparatus for ethylbenzene production and transalkylation to xylene'20056,060,631'Process for the conversion of plastic to produce a synthetic crude oil'20005,969,201'Process for the conversion of plastic to produce a synthetic crude oil'19995,904,838'Process for the simultaneous conversion of waste lubricating oil and pyrolysis oil derived from organic waste to produce a synthetic crude oil'19995,723,706'Process for the treatment of halogenated organic feedstocks'19985,552,037'Process for the treatment of two halogenated hydrocarbon streams'19965,401,894'Process for the treatment of halogenated organic feedstocks'19955,316,663'Process for the treatment of halogenated hydrocarbons'19945,302,282'Integrated process for the production of high quality lube oil blending stock'19945,244,565'Integrated process for the production of distillate hydrocarbon'19935,176,816'Process to produce a hydrogenated distillable hydrocarbonaceous product'19935,102,531'Process for treating a temperature sensitive hydrocarbonaceous stream containing a non-distillable component to product a distillable hydrocarbonaceous product'19925,068,484'Process for the hydroconversion of a feedstock comprising organic compounds having a tendency to readily form polymer compounds'19915,064,450'Gas absorber method and apparatus'19915,057,125'Process for the treatment of vent gas containing organic halide compounds'19915,028,313'Process for treating a temperature-sensitive hydrocarbonaceous stream containing a non-distillable component to produce a distillable hydrocarbonaceous product'19915,013,424'Process for the simultaneous hydrogenation of a first feedstock comprising hydrocarbonaceous compounds and having a non-distillable component and a second feedstock comprising halogenated organic compounds'19915,004,533'Process for treating an organic stream containing a non-distillable component to produce an organic vapor and a solid'19914,929,781'Process for the simultaneous hydroconversion of a first feedstock comprising unsaturated, halogenated organic compounds and a second feedstock comprising saturated, halogenated organic compounds'19904,927,520'Process for treating a hydrocarbonaceous stream containing a non-distillable component to produce a hydrogenated distillable hydrocarbonaceous product'19904,923,590'Process for treating a temperature-sensitive hydrocarbonaceous stream containing a non-distillable component to produce a hydrogenated distillable hydrocarbonaceous product'19904,902,842'Process for the simultaneous hydroconversion of a first feedstock comprising unsaturated, halogenated organic compounds and a second feedstock comprising saturated, halogenated organic compounds'19904,899,001'Process for the simultaneous hydroconversion of a first feedstock comprising unsaturated, halogenated organic compounds and a second feedstock comprising saturated, halogenated organic compounds'19904,895,995'Process for the simultaneous hydroconversion of a first feedstock comprising unsaturated, halogenated organic compounds and a second feedstock comprising saturated, halogenated organic compounds'19904,882,037'Process for treating a temperature-sensitive hydrocarbonaceous stream containing a non-distillable component to produce a selected hydrogenated distillable light hydrocarbonaceous product'19894,840,721'Process for treating a temperature-sensitive hydrocarbonaceous stream containing a non-distillable component to produce a hydrogenated distillable hydrocarbonaceous product'19894,818,368'Process for treating a temperature-sensitive hydrocarbanaceous stream containing a non-distillable component to produce a hydrogenated distillable hydrocarbonaceous product'19894,806,233'Method of separating a hot hydrocarbonaceous stream'19894,594,144'Process for making high octane gasoline'19864,482,369'Process for producing a hydrogen-rich gas stream from the effluent of a catalytic hydrocarbon conversion reaction zone'19844,431,522'Catalytic reforming process'19844,397,383'Escalator safety insert'1983Career & activity timeline
Assembled from patent assignee/location history and declaration credentials.
1983Based in Willowdale, CA· patent location history
1984–1998Patents assigned to UOP INC (27)· patent assignee history
1984–2019Based in Northbrook, IL, US· patent location history
1989Based in Des Plaines, IL, US· patent location history
1999–2019Patents assigned to UOP LLC (15)· patent assignee history
2009–2016Patents assigned to GEN ELECTRIC (4)· patent assignee history
2009–2016Based in Wilmington, NC, US· patent location history
2014–2016Patents assigned to JAMES ROBERT BRYANT (4)· patent assignee history
2014–2016Patents assigned to RUSSELL II WILLIAM EARL (4)· patent assignee history
Inventor activity
Assignee and location history derived from the patent record.
Assignees
| Assignee | Patents | Span |
|---|---|---|
| UOP INC | 27 | 1984–1998 |
| UOP LLC | 15 | 1999–2019 |
| GEN ELECTRIC | 4 | 2009–2016 |
| JAMES ROBERT BRYANTself | 4 | 2014–2016 |
| RUSSELL II WILLIAM EARL | 4 | 2014–2016 |
Locations
| Location | Patents | Span |
|---|---|---|
| Northbrook, Illinois, US | 41 | 1984–2019 |
| Wilmington, NC, US | 9 | 2009–2016 |
| Des Plaines, Illinois, US | 1 | 1989 |
| Willowdale, CA | 1 | 1983 |