公开(公告)号：US2271017A

公开(公告)日：1942-01-27

申请号：US20709538

申请日：1938-05-10

申请人： APPLIED CHEMICALS INC

发明人： RENE LEPRESTRE ,  LEPRESTRE MARGARET C ,  DOUGLAS HADDEN H ,  TOBIN RALPH C ,  JOSEPH DANNENBERG

CPC分类号： C10G47/00 ,  C10G47/32

公开(公告)号：US2089616A

公开(公告)日：1937-08-10

申请号：US64713132

申请日：1932-12-14

申请人： ERNEST A OCON

发明人： MCKEE RALPH H

CPC分类号： C10G47/32

公开(公告)号：US1966455A

公开(公告)日：1934-07-17

申请号：US43039930

申请日：1930-02-21

申请人： UNIVERSAL OIL PROD CO

发明人： MORRELL JACQUE C

IPC分类号： C10G67/10

CPC分类号： C10G47/32 ,  C10G67/10

公开(公告)号：US1956573A

公开(公告)日：1934-05-01

申请号：US45596430

申请日：1930-05-26

申请人： STANDARD OIL DEV CO

发明人： HASLAM ROBERT T

IPC分类号： C10G47/32

CPC分类号： C10G47/32

公开(公告)号：US1956567A

公开(公告)日：1934-05-01

申请号：US45891930

申请日：1930-05-31

申请人： STANDARD OIL DEV CO

发明人： CARLETON ELLIS

CPC分类号： C10G47/32

公开(公告)号：US1937946A

公开(公告)日：1933-12-05

申请号：US42795430

申请日：1930-02-12

申请人： UNIVERSAL OIL PROD CO

发明人： GUSTAV EGLOFF

IPC分类号： C10G67/08

CPC分类号： C10G47/32 ,  C10G67/08

公开(公告)号：US1928784A

公开(公告)日：1933-10-03

申请号：US57924031

申请日：1931-12-05

申请人： INTERNAT OIL GAS CORP

发明人： HARRIS LEONARD B

CPC分类号： C10G47/32 ,  C01B3/40

公开(公告)号：US1046683A

公开(公告)日：1912-12-10

申请号：US1908444674

申请日：1908-07-21

申请人： TURNER CHARLES WORTH

发明人： TURNER CHARLES WORTH

IPC分类号： C07C11/00

CPC分类号： C10G47/32 ,  C07C11/00

公开(公告)号：US20230407192A1

公开(公告)日：2023-12-21

申请号：US18333846

申请日：2023-06-13

申请人： COOLBROOK OY

发明人： Alexander KARPOV ,  Denis SEMENOV ,  Vahid SUDZHADINOV

IPC分类号： C10G47/32 ,  C10G47/36

CPC分类号： C10G47/32 ,  C10G47/36 ,  C10G2300/708 ,  C10G2300/807 ,  C10G2300/4006 ,  C10G2400/20

摘要： A method for reducing coke formation during thermal or thermochemical conversion of hydrocarbon feedstocks in a gaseous diluent using a rotary reactor provided. The method comprises supplying an amount of additional gaseous diluent into high-temperature region(s) (10) of the reactor, where conditions are established for thermal or thermochemical conversion to occur. In these regions, said additional gaseous diluent is supplied into a reaction space through perforations and/or pores (11) made in stationary blades (2, 4) or in other surfaces (7, 7A) enclosing a process fluid flow. A rotary apparatus configured to implement the method is further provided.

公开(公告)号：US20230348800A1

公开(公告)日：2023-11-02

申请号：US18136031

申请日：2023-04-18

申请人： GTI Energy

发明人： Terry MARKER ,  Martin B. LINCK ,  Jim WANGEROW ,  Pedro ORTIZ-TORAL

IPC分类号： C10G50/00 ,  C10L3/08 ,  C07C1/12 ,  C07C1/04 ,  C07C5/13 ,  C07C9/04 ,  B01D3/14 ,  C10G47/32 ,  B01D3/06

CPC分类号： C10G50/00 ,  C10L3/08 ,  C07C1/12 ,  C07C1/04 ,  C07C5/13 ,  C07C9/04 ,  B01D3/143 ,  C10G47/32 ,  B01D3/06 ,  C10G2400/08 ,  C10G2300/1025 ,  C01B32/50

摘要： Processes for converting methane and/or other hydrocarbons to synthesis gas (i.e., a gaseous mixture comprising H2 and CO) are disclosed, in which at least a portion of the hydrocarbon(s) is reacted with CO2. At least a second portion of the methane may be reacted with H2O (steam), thereby improving overall thermodynamics of the process, in terms of reducing endothermicity (ΔH) and the required energy input, compared to “pure” dry reforming in which no H2O is present. Such dry reforming (reaction with CO2 only) or CO2-steam reforming (reaction with both CO2 and steam) processes are advantageously integrated with Fischer-Tropsch synthesis to yield liquid hydrocarbon fuels. Further integration may involve the use of a downstream finishing stage involving hydroisomerization to remove FT wax. Yet other integration options involve the use of combined CO2-steam reforming and FT synthesis stages (optionally with finishing) for producing liquid fuels from gas streams generated in a number of possible processes, including the hydropyrolysis of biomass.