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    • 3. 发明申请
    • HEATING AND TREATMENT OF PARTICULATE MATERIAL
    • 颗粒材料的加热和处理
    • WO1991001799A1
    • 1991-02-21
    • PCT/AU1990000330
    • 1990-08-03
    • CRA SERVICES LIMITEDBATTERHAM, Robin, JohnGRANT, Roderick, MacphersonHAPP, James, VincentTHIELE, Glenn, Ashley
    • CRA SERVICES LIMITED
    • B01J06/00
    • B01J8/1836B01J2208/00088B01J2208/00371B01J2208/00495C04B5/06C04B7/432Y02P40/121C04B7/4484
    • The specification discloses a process for heating solid particulate materials. The process comprises entraining the solid particulate materials in a gas to form a stream of gas containing entrained particles and contacting this stream with a stream of hot gases. The contact between the two streams is performed in such a manner that at least a portion of the solid particulate material is heated rapidly and the heated and unheated particles enter flow patterns in which contact between the particles and with interior surfaces of a contact chamber is minimized. A heating and treatment chamber for applying the process to the treatment of solid particulate materials is disclosed. The specification also discloses a molten bath reactor combined with the chamber for heating and treating solid particulate materials. Hot off gases from the molten bath reactor can be passed through the chamber and treated particulate material from the chamber can be inserted in the molten bath reactor or partially recycled through the chamber.
    • 该说明书公开了一种用于加热固体颗粒材料的方法。 该方法包括将固体颗粒材料夹带在气体中以形成含有夹带颗粒的气流并将该流与热气流接触。 两个流之间的接触以这样的方式进行,使得固体颗粒材料的至少一部分被快速加热并且加热和未加热的颗粒进入其中颗粒之间的接触和接触室的内表面之间的接触最小化的流动模式 。 公开了一种用于将该方法应用于处理固体颗粒材料的加热和处理室。 本说明书还公开了一种与室结合的用于加热和处理固体颗粒材料的熔池反应器。 来自熔浴反应器的热气体可以通过室,并且来自室的经处理的颗粒材料可以插入熔池反应器中或部分地通过室再循环。
    • 6. 发明申请
    • ENERGY CONSERVING PROCESS FOR CALCINING CLAY
    • 能源保存过程计算粘土
    • WO1990005586A1
    • 1990-05-31
    • PCT/US1989002999
    • 1989-07-13
    • GEORGIA KAOLIN COMPANY, INC.
    • GEORGIA KAOLIN COMPANY, INC.BAIRD, David, Paul
    • B01J06/00
    • C09C1/42C01P2004/50C04B33/32F27B9/185F27D17/004Y02P40/63Y02P40/65
    • A dry pulverized clay powder (1) is fed to a calciner (20) to be calcined therein. The clay powder feed (1) is passed through the calciner (20) in direct heat exchange contact with a hot gas (5) passing therethrough to heat the clay powder sufficiently to calcine substantially all the clay powder while passing through the calciner (20). The calcined clay product (3) is removed from the calciner (20) and preferably passed in heat exchange relationship with a cooling medium (71) whereby the calcined clay product (3) is cooled and the cooling medium is heated. The hot off-gas (7) discharged from the calciner (20) is passed through an electrostatic precipitator (30) to remove at least a substantial portion of calcined clay product dust (11) entrained in the exhaust gas from the calciner. The clean gas (13) leaving the electrostatic precipitator (30) is passed in heat exchange relationship with a cooling fluid (51) to further cool the gas, and preferably to evaporate at least a portion of the cooling portion to produce a heating vapor (53). The hot calcined clay dust (11) separated from the hot gas in the electrostatic precipitator (30) is recovered. Preferably, the recovered hot calcined clay dust (11) is mixed with the clay feed material (1) being supplied to the calciner (20) without substantially cooling the hot calcined clay powder collected in the electrostatic precipitator (30).
    • 将干燥的粉碎粘土粉末(1)加入到煅烧器(20)中以在其中煅烧。 粘土粉末进料(1)通过煅烧炉(20)与通过其中的热气体(5)直接热交换接触,以充分加热粘土粉末,以在通过煅烧炉(20)的同时煅烧基本上所有的粘土粉末, 。 煅烧的粘土产物(3)从煅烧炉(20)中除去,优选与冷却介质(71)热交换,从而将煅烧的粘土产物(3)冷却并冷却介质。 从煅烧炉(20)排出的热废气(7)通过静电除尘器(30)以除去夹带在来自煅烧炉的废气中的至少大部分煅烧粘土产品粉尘(11)。 离开静电除尘器(30)的清洁气体(13)与冷却流体(51)以热交换关系通过,以进一步冷却气体,并且优选蒸发冷却部分的至少一部分以产生加热蒸气( 53)。 回收与静电除尘器(30)中的热气分离的热煅烧粘土粉尘(11)。 优选地,将回收的热煅烧粘土粉尘(11)与供给到煅烧炉(20)的粘土进料(1)混合,而基本上不会将收集在静电除尘器(30)中的热煅烧粘土粉末基本上冷却。