PROCESS AND APPARATUS FOR DEDUSTING A VAPOR GAS MIXTURE
    4.
    发明申请
    PROCESS AND APPARATUS FOR DEDUSTING A VAPOR GAS MIXTURE 有权
    用于喷射气体混合物的方法和装置

    公开(公告)号:US20140290480A1

    公开(公告)日:2014-10-02

    申请号:US14351883

    申请日:2012-10-10

    IPC分类号: B03C3/00

    CPC分类号: B03C3/00

    摘要: A process for dedusting a dust laden vapor gas mixture (VGM) obtained by pyrolysis of a material containing hydrocarbons includes treating the dust laden VGM in a dry electrostatic precipitator at a temperature in a range from 380 to 480° C. so as to separate dust from the VGM. Then, the VGM is cooled to a temperature in a range from 310 to 360° C.

    摘要翻译: 通过对含有烃的材料进行热解而获得的含灰尘蒸汽气体混合物(VGM)的除尘方法包括在380-480℃的温度范围内,在干式静电除尘器中处理载有灰尘的VGM,以分离灰尘 来自VGM。 然后,将VGM冷却至310〜360℃的温度。

    Process and apparatus for dedusting a vapor gas mixture
    7.
    发明授权
    Process and apparatus for dedusting a vapor gas mixture 有权
    用于除尘蒸气混合物的方法和装置

    公开(公告)号:US09221062B2

    公开(公告)日:2015-12-29

    申请号:US14351883

    申请日:2012-10-10

    IPC分类号: B03C3/00

    CPC分类号: B03C3/00

    摘要: A process for dedusting a dust laden vapor gas mixture (VGM) obtained by pyrolysis of a material containing hydrocarbons includes treating the dust laden VGM in a dry electrostatic precipitator at a temperature in a range from 380 to 480° C. so as to separate dust from the VGM. Then, the VGM is cooled to a temperature in a range from 310 to 360° C.

    摘要翻译: 通过对含有烃的材料进行热解而获得的含灰尘蒸汽气体混合物(VGM)的除尘方法包括在380-480℃的温度范围内,在干式静电除尘器中处理载有灰尘的VGM,以分离灰尘 来自VGM。 然后,将VGM冷却至310〜360℃的温度。

    Process and plant or refining raw materials containing organic constituents
    8.
    发明授权
    Process and plant or refining raw materials containing organic constituents 有权
    包含有机成分的工艺和植物或精炼原料

    公开(公告)号:US08936657B2

    公开(公告)日:2015-01-20

    申请号:US12867451

    申请日:2009-02-04

    IPC分类号: C01B3/36 C10G1/02

    摘要: A process for refining raw materials containing at least one of oil and bitumen includes supplying the raw materials to a reactor and volatilizing fuel gas in the reactor at a temperature of from 300 to 1000° C. and a pressure of from 0.001 to 1 bar. Solids remaining in the reactor, including non-evaporated fractions of heavy hydrocarbons, are introduced into a furnace. A staged combustion of the non-evaporated fractions of heavy hydrocarbons is performed in a substoichiometric stage and in a superstoichiometric stage in the furnace at a furnace temperature of from 600 to 1500° C. as to obtain hot solids in the furnace. The hot solids are recirculated from the furnace into the reactor. A sealing device separates an oxidizing atmosphere of the furnace from an atmosphere of the reactor.

    摘要翻译: 用于精炼含有油和沥青中的至少一种的原料的方法包括将原料供应到反应器中并在300-1000℃的温度和0.001至1巴的压力下使反应器中的燃料气体挥发。 残留在反应器中的固体,包括重质烃的非蒸发馏分,被引入炉中。 未蒸发馏分的重质烃的分段燃烧是在600至1500℃的炉温下在化学计量阶段和炉中的超化学计量阶段进行的,以便在炉中获得热固体。 热固体从炉再循环到反应器中。 密封装置将炉的氧化气氛与反应器的气氛分离。

    PROCESS AND PLANT FOR REFINING OIL-CONTAINING SOLIDS
    9.
    发明申请
    PROCESS AND PLANT FOR REFINING OIL-CONTAINING SOLIDS 有权
    精炼含油固体的工艺和设备

    公开(公告)号:US20100187161A1

    公开(公告)日:2010-07-29

    申请号:US12668778

    申请日:2008-06-24

    IPC分类号: C10G1/02 F27B15/14

    摘要: For refining oil-containing solids, in particular oil sand or oil shale, there is proposed a process with the following steps: supplying the oil-containing solids to a reactor and expelling an oil-containing vapor at a temperature of 300 to 1000° C., supplying the oil-containing vapor expelled in the reactor to a cracker, in which the heavy oil components are broken down, separating the products obtained in the cracker and withdrawing the product streams, introducing the solids left in the reactor including the unevaporated fraction of heavy hydrocarbons into a furnace, burning the heavy hydrocarbons left in the solids in the furnace at a temperature of 600 to 1500° C., preferably 1050 to 1200° C., recirculating hot solids from the furnace into the reactor, wherein the oxidizing atmosphere of the furnace is separated from the atmosphere of the reactor by a blocking device.

    摘要翻译: 为了精炼含油固体,特别是油砂或油页岩,提出了一种具有以下步骤的方法:将含油固体供应到反应器中并在300至1000℃的温度下排出含油蒸汽 将在反应器中排出的含油蒸气供应到裂化器中,其中重油组分被分解,分离在裂化器中获得的产物并抽出产物流,将留在反应器中的固体引入,包括未蒸发的馏分 将重质烃放入炉中,在600至1500℃,优选1050至1200℃的温度下将留在炉中固体中的重质烃燃烧,将热固体从炉中再循环进入反应器,其中氧化 通过阻挡装置将炉的气氛与反应器的气氛分离。

    Anode for the electrolytic winning of metals and process
    10.
    发明授权
    Anode for the electrolytic winning of metals and process 失效
    阳极用于电解金属和工艺的获胜

    公开(公告)号:US5679240A

    公开(公告)日:1997-10-21

    申请号:US679683

    申请日:1996-07-11

    CPC分类号: C25C7/02

    摘要: The anode comprises a substantially horizontal carrying bar, which is disposed outside the electrolyte and serves to supply electric current. Two substantially parallel metal surfaces (anode grids) are electrically conductively connected to the carrying bar and with at least one-half of their surface extending into the electrolyte. The carrying bar comprises a copper conductor, to which at least one vertical copper rod is joined. There is a direct electrically conducting connection between the copper conductor and the copper rod. The copper rod is surrounded by a titanium sheath and is an interference fit in that sheath. The copper rod provided with the titanium sheath is disposed between the two anode grids and is electrically conductively connected to said grids.

    摘要翻译: 阳极包括基本上水平的承载杆,其设置在电解质的外部并用于提供电流。 两个基本上平行的金属表面(阳极栅极)导电地连接到承载杆,并且其表面的至少一半延伸到电解质中。 承载杆包括铜导体,至少一个垂直铜杆连接到该铜导体。 在铜导体和铜棒之间有一个直接的导电连接。 铜杆被钛护套包围,并且是在该护套中的过盈配合。 设置有钛护套的铜杆设置在两个阳极栅极之间,并且与导电连接到所述栅极。