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公开(公告)号:US2419565A
公开(公告)日:1947-04-29
申请号:US46901642
申请日:1942-12-14
Applicant: PHILLIPS PETROLEUM CO
Inventor: KREJCI JOSEPH C
IPC: C09C1/50
CPC classification number: C09C1/50
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公开(公告)号:US2375798A
公开(公告)日:1945-05-15
申请号:US44533842
申请日:1942-06-01
Applicant: PHILLIPS PETROLEUM CO
Inventor: KREJCI JOSEPH C
IPC: C09C1/50
CPC classification number: C09C1/50
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公开(公告)号:US3410660A
公开(公告)日:1968-11-12
申请号:US48640565
申请日:1965-09-10
Applicant: PHILLIPS PETROLEUM CO
Inventor: HENDERSON EULAS W , KREJCI JOSEPH C
IPC: C09C1/50
CPC classification number: C09C1/50 , C01P2006/12 , C01P2006/19
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公开(公告)号:US3018309A
公开(公告)日:1962-01-23
申请号:US84138059
申请日:1959-09-21
Applicant: PHILLIPS PETROLEUM CO
Inventor: KREJCI JOSEPH C
IPC: C10G9/36
CPC classification number: C10G9/36 , C10G2400/20 , Y10S585/925 , Y10S585/95 , Y10S585/955
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公开(公告)号:US2781247A
公开(公告)日:1957-02-12
申请号:US40692154
申请日:1954-01-29
Applicant: PHILLIPS PETROLEUM CO
Inventor: KREJCI JOSEPH C
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公开(公告)号:US2750434A
公开(公告)日:1956-06-12
申请号:US30695653
申请日:1953-06-11
Applicant: PHILLIPS PETROLEUM CO
Inventor: KREJCI JOSEPH C
IPC: C10G9/36
CPC classification number: C10G9/36 , C10G2400/20 , Y10S585/921 , Y10S585/922 , Y10S585/924 , Y10S585/925 , Y10S585/955
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公开(公告)号:US2600994A
公开(公告)日:1952-06-17
申请号:US56211544
申请日:1944-11-06
Applicant: PHILLIPS PETROLEUM CO
Inventor: KREJCI JOSEPH C
IPC: C09C1/50
CPC classification number: C09C1/50
Abstract: A process for making carbon black comprises forming an annular outer layer of combustion-supporting gas rotating about the axis of a cylindrical furnace chamber, flowing an annular cylinder of hydrocarbon gas inside this outer layer, and flowing a core of combustion-supporting gas inside the annular cylinder, and burning the gas mixture to form carbon black from the combustion at each face of the annular cylinder. Hydrocarbon gas, e.g. methane which may be preheated, enters with air through tangential burners 15 in the side of cylindrical reaction chamber 10 of the type described in Specification 621,031, having steel shell 13 enclosing insulating layer 12 and refractory, e.g. sillimanite or fused alumina, lining 11; the gas/air mixture is introduced in increasing amount until a carbon black-forming temperature is reached. Hydrocarbon gas, e.g. methane or vaporized gas oil, with or without air, which may have been heated to 2000 DEG F. in preheater 32 is then fed into the reactor 10 through annular passage 18 or alternatively through a plurality of inlets arranged in a ring about the centre of the reactor inlet wall. At the same time air which may also be preheated in 32 is passed into reactor 10 through porous refractory tube 16 which may be perforated and may alternatively p have an open downstream end. Once the reaction is proceeding, the hydrocarbon gas supplied to tangential burners 15 may be cut off. Temperatures may be taken through 20 and the carbon black in the effluent may be washed down by water from spray 14.
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公开(公告)号:US2377245A
公开(公告)日:1945-05-29
申请号:US51279843
申请日:1943-12-03
Applicant: PHILLIPS PETROLEUM CO
Inventor: KREJCI JOSEPH C
IPC: C07C2/78
CPC classification number: C07C2/78 , Y10S585/923 , Y10S585/924 , Y10S585/953 , C07C11/24
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公开(公告)号:US2375797A
公开(公告)日:1945-05-15
申请号:US43652442
申请日:1942-03-27
Applicant: PHILLIPS PETROLEUM CO
Inventor: KREJCI JOSEPH C
IPC: C09C1/50
CPC classification number: C09C1/50
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