APPARATUS FOR THE TREATMENT OF SOLIDS AND/OR GASES
    1.
    发明申请
    APPARATUS FOR THE TREATMENT OF SOLIDS AND/OR GASES 有权
    用于处理固体和/或气体的装置

    公开(公告)号:US20120269688A1

    公开(公告)日:2012-10-25

    申请号:US13503073

    申请日:2010-10-20

    IPC分类号: B01J8/18

    摘要: An apparatus for the treatment of at least one of solids and gases includes a fluidized-bed reactor configured to fluidize the solids using fluidizing gas and to at least one of thermally and chemically treat the solids. A centrifugal separator is configured to separate the fluidizing gas and the solids from each other. A transfer duct connects the fluidized-bed reactor and centrifugal separator to each other. The transfer duct has a trapezoidal cross-section in a vertical direction and in a horizontal direction. The transfer duct branches off from the fluidized bed reactor with a cross-section having a horizontal dimension that is greater than a vertical dimension. The cross-section of the transfer duct expands downwards in the vertical direction from the fluidized-bed reactor to the centrifugal separator. The cross-section of the transfer duct tapers in the horizontal direction from the fluidized-bed reactor towards the centrifugal separator.

    摘要翻译: 用于处理固体和气体中的至少一种的装置包括流化床反应器,其构造成使用流化气体使固体流化并且至少一种热固化和化学处理固体。 离心分离器构造成将流化气体和固体彼此分离。 输送管将流化床反应器和离心分离器彼此连接。 输送管道在垂直方向和水平方向上具有梯形截面。 输送管道从流化床反应器分支,横截面的水平尺寸大于垂直尺寸。 输送管道的横截面在垂直方向上从流化床反应器向下膨胀到离心分离器。 输送管道的横截面从流化床反应器向离心分离器在水平方向逐渐变细。

    PROCESS FOR PLANT FOR REFINING RAW MATERIALS CONTAINING ORGANIC CONSTITUENTS
    5.
    发明申请
    PROCESS FOR PLANT FOR REFINING RAW MATERIALS CONTAINING ORGANIC CONSTITUENTS 有权
    用于精炼含有机原料的工厂的工艺

    公开(公告)号:US20100313475A1

    公开(公告)日:2010-12-16

    申请号:US12867451

    申请日:2009-02-04

    IPC分类号: C10L3/00 C10G9/04

    摘要: A process for refining raw materials containing oil and/or bitumen includes supplying the raw materials to a reactor. The reactor is operated under a pressure of from 0.001 to 1 bar and at a reactor temperature of from 300 to 1000° C. so as to volatize fuel gases and obtain solids and non-evaporated fractions of heavy hydrocarbons. The solids and non-evaporated fractions of heavy hydrocarbons are introduced into a furnace. The non-evaporated fractions of heavy hydrocarbons are burned in the furnace at a furnace temperature of from 600 to 1500° C. so as to obtain hot solids in the furnace. The hot solids are recirculated from the furnace into the reactor. An oxidizing atmosphere of the furnace is separated from an atmosphere of the reactor by a sealing device.

    摘要翻译: 用于精炼含有油和/或沥青的原料的方法包括将原料供应到反应器中。 反应器在0.001至1巴的压力和300至1000℃的反应器温度下运行,以便挥发燃料气体并获得重质烃的固体和非蒸发馏分。 将重质烃的固体和非蒸发馏分引入炉中。 重质烃的非蒸发馏分在炉中在600至1500℃的炉温下燃烧,以便在炉中获得热固体。 热固体从炉再循环到反应器中。 通过密封装置将炉的氧化气氛与反应器的气氛分离。

    PROCESS AND PLANT FOR PRODUCING METAL OXIDE FROM METAL SALTS
    8.
    发明申请
    PROCESS AND PLANT FOR PRODUCING METAL OXIDE FROM METAL SALTS 有权
    从金属盐生产金属氧化物的工艺和设备

    公开(公告)号:US20120052000A1

    公开(公告)日:2012-03-01

    申请号:US13146196

    申请日:2009-12-18

    IPC分类号: C01F7/02 B01J8/08 C01B13/14

    CPC分类号: C01F7/444 C01B13/18 C01F7/445

    摘要: A process for producing metal oxide from a metal salt includes supplying a first part of the metal salt to a hydrate drier so as to indirectly heat the first part of the metal salt in the hydrate drier using a heat transfer medium from a first stage of a multi-stage indirect cooler so as to dry the first part of the metal salt in the hydrate drier and so as to control a waste gas temperature of the process. A second part of the metal salt is guided as a partial stream past the hydrate drier. The metal salt is preheated in a first preheating stage and precalcined in a second preheating stage. The metal salt and a fluidizing gas having a temperature of 150° C. or less are supplied to a fluidized bed reactor so as to calcine the metal salt to form a metal oxide product. The metal oxide product is cooled in at least one suspension heat exchanger and then in the multi-stage indirect cooler.

    摘要翻译: 从金属盐生产金属氧化物的方法包括将金属盐的第一部分供应到水合物干燥器中,以便使用传热介质间接加热水合物干燥器中的金属盐的第一部分, 多级间接冷却器,以干燥水合物干燥器中的金属盐的第一部分,以便控制该方法的废气温度。 金属盐的第二部分作为部分流引导通过水合物干燥器。 金属盐在第一预热阶段进行预热,并在第二预热阶段进行预煅烧。 将金属盐和温度为150℃以下的流化气体供给流化床反应器,以煅烧金属盐形成金属氧化物产物。 金属氧化物产物在至少一个悬浮热交换器中冷却,然后在多级间接冷却器中冷却。

    Process and plant or refining raw materials containing organic constituents
    10.
    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。