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    • 4. 发明申请
    • GAS NOZZLE AND REACTOR WITH THE SAME
    • 气体喷嘴和反应器
    • WO2008154995A1
    • 2008-12-24
    • PCT/EP2008/004006
    • 2008-05-20
    • OUTOTEC OYJMISSALLA, MichaelPARTHASARATHY, MukundWERTHER, JoachimSCHMIDBAUER, Erwin
    • MISSALLA, MichaelPARTHASARATHY, MukundWERTHER, JoachimSCHMIDBAUER, Erwin
    • B01J8/18B01J8/24
    • B01J8/1818B01J8/1827F27B15/10
    • This invention relates to a gas nozzle (1, 1', 1 ") for introducing a gas or gas mix ture in a reactor or the like, comprising a nozzle tube (2) for passing through a gas, at least one nozzle opening (11) arranged near an end of the nozzle tube (2) for discharging the gas from the nozzle tube (2) to the surroundings, and a pot-like hood (4). The hood (4) closes the nozzle tube (2) with a hood cover (7) at the end at which the at least one nozzle opening (11) is provided. The hood (4) includes a hood apron (9) connected with the hood cover (7), which enclosing the nozzle tube (2) by forming an annular gap (10) extends away from the end at which the at least one nozzle opening (11) is provided. The hood apron (9) preferably has a length (L) of at least about 100 mm. Furthermore, this invention relates to a reactor with such gas nozzle (1, 1', 1 ").
    • 本发明涉及一种用于在反应器等中引入气体或气体混合物的气体喷嘴(1,1',1“),其包括用于通过气体的喷嘴管(2),至少一个喷嘴开口 11),其布置在喷嘴管(2)的端部附近,用于将喷嘴管(2)的气体排放到周围,以及盆形罩(4),罩(4)封闭喷嘴管 在所述至少一个喷嘴开口(11)的端部处具有罩罩(7),所述罩(4)包括与所述罩盖(7)连接的罩围裙(9),所述罩盖围绕所述喷嘴管 (2)通过形成环形间隙(10)远离设置有所述至少一个喷嘴开口(11)的端部延伸,所述罩围裙(9)优选地具有至少约100mm的长度(L)。 此外,本发明涉及一种具有这种气体喷嘴(1,1',1“)的反应器。
    • 5. 发明申请
    • PROCESS AND PLANT FOR REFINING RAW MATERIALS CONTAINING ORGANIC CONSTITUENTS
    • WO2009100841A3
    • 2009-08-20
    • PCT/EP2009/000730
    • 2009-02-04
    • OUTOTEC OYJSCHMIDBAUER, Erwin
    • SCHMIDBAUER, Erwin
    • C10B49/16C10G1/00C10G1/02
    • In accordance with the invention, refining raw materials containing organic constituents, such as raw materials containing oil and/or bitumen, in particular oil or tar sand or oil shale, is effected with the following steps: supplying the raw materials to an expulsion stage and expelling a hydrocarbonaceous, in particular oil-containing vapor at a temperature of e.g. about 300 to 1000°C, supplying the hydrocarbonaceous vapor expelled in the expulsion stage and/or in a gasification stage downstream of the expulsion stage to a processing stage, in which the same is further processed e.g. by cracking, coking and/or hydrotreating, separating the products obtained in the processing stage and withdrawing the same, introducing the solids left in the expulsion stage and/or in the gasification stage including the non-evaporated fractions of heavy hydrocarbons into a combustion stage, burning the heavy hydrocarbons left in the solids in the combustion stage at a temperature of e.g. about 600 to 1500°C, preferably e.g. about 1050 to 1200°C, recirculating hot solids from the combustion stage into the expulsion stage and/or the gasification stage, wherein the oxidizing atmosphere of the combustion stage is separated from the atmosphere of the expulsion stage and/or the gasification stage by means of a blocking device, and supplying water into the expulsion stage and/or the gasification stage.