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    • 1. 发明授权
    • Eliminating ash bridging in ceramic filters
    • 消除陶瓷过滤器中的灰渣桥接
    • US5531798A
    • 1996-07-02
    • US249216
    • 1994-05-26
    • Folke EngstromJuhani Isaksson
    • Folke EngstromJuhani Isaksson
    • B01D46/00B01D46/24B01D46/42B01D46/46C10J3/84B01D46/04
    • B01D46/2407B01D46/002B01D46/0068B01D46/46C10J3/482C10J3/56C10J3/84C10K1/024B01D2273/20C10J2300/093
    • In the filtering of high temperature (e.g. greater than 400.degree. C.) and high pressure (e.g. greater than 5 bar) gas--such as produced by pressurized fluidized bed combustion or gasification of coal--there is often a buildup of particles on the supporting elements for the filters, and on surrounding structures. This buildup of particles can damage the filter elements, or greatly reduce their effectiveness. This problem is avoided by periodically automatically cleaning the supporting and/or surrounding surfaces of the filters, as by directing high pressure gas streams at the supporting and/or surrounding surfaces. The filters may also be backflushed with compressed gas, as is conventional, at the same time as, or at different times than, when the supporting and/or surrounding structures are cleaned. Conduits with nozzles may be mounted directly on the supporting and/or surrounding surfaces and connected by a pipe with an automatically controlled valve to a source of high pressure fluid.
    • 在过滤高温(例如大于400℃)和高压(例如大于5巴)的气体(例如通过加压流化床燃烧或煤气化产生)中,通常在支撑物上堆积颗粒 过滤器的元件和周围的结构。 这种颗粒的积聚可能会损坏过滤元件,或大大降低其效果。 通过周期性地自动清洁过滤器的支撑和/或周围表面来避免这个问题,如通过在支撑和/或周围表面处引导高压气体流。 过滤器也可以用压缩气体反冲洗,如常规的那样,在支撑和/或周围结构被清洁的同时或不同的时间。 带有喷嘴的管道可以直接安装在支撑和/或周围表面上,并通过具有自动控制阀的管道连接到高压流体源。
    • 2. 发明授权
    • Combustion of fuel containing alkalines
    • 燃烧含有碱的燃料
    • US4771712A
    • 1988-09-20
    • US65757
    • 1987-06-24
    • Folke EngstromErkki KiiskilaPekka Tormikoski
    • Folke EngstromErkki KiiskilaPekka Tormikoski
    • C10L9/10C10L10/04F23C10/10F23C10/22F23J20060101F23J7/00F23D1/00
    • F23C10/10C10L9/10F23J7/00F23C2206/101
    • A method of burning solid fuel having low melting point alkaline compositions, such as alkali metal salts, particularly lignite and salty brown coal. The fuel is introduced into the reaction chamber of a circulating fluidized bed reactor, and is mixed prior to introduction to the reaction chamber with a reactant material capable of reacting with the low melting point alkaline compositions of the fuel to produce high melting point alkali metal compounds during combustion. The temperature in the reaction chamber is kept below the melting point of the formed alkali metal compounds. The reactant material comprises silica oxide or a metal oxide, or hydroxide, of the group consisting of aluminum, calcium, magnesium, iron, titanium, and mixtures of two or more thereof. Kaolin is particularly effective, especially when the molar ratio of Al/(Na and K) is at least 1.0.
    • 一种燃烧具有低熔点碱性组合物的固体燃料的方法,例如碱金属盐,特别是褐煤和咸棕色煤。 将燃料引入循环流化床反应器的反应室中,并在与反应物料引入反应室之前混合,反应物料能够与燃料的低熔点碱性组合物反应以产生高熔点碱金属化合物 在燃烧过程中。 反应室中的温度保持低于形成的碱金属化合物的熔点。 反应物料包括氧化铝或金属氧化物或氢氧化物,它们由铝,钙,镁,铁,钛及其两种或多种的混合物组成。 高岭土特别有效,特别是当Al /(Na和K)的摩尔比至少为1.0时。
    • 4. 发明授权
    • Circulating fluidized bed reactor temperature control
    • 循环流化床反应器温度控制
    • US4672918A
    • 1987-06-16
    • US734716
    • 1985-05-16
    • Folke EngstromJuha Sarkki
    • Folke EngstromJuha Sarkki
    • B01J8/00B01J8/24B01J8/38F22B31/00F23C10/08F22B1/00
    • B01J8/1809B01J8/005B01J8/388F22B31/0084F23C10/08B01J2208/00044F23C2206/101
    • A simple yet effective method and apparatus control the temperature within a fluidized bed reactor within a desired range (e.g. about 800.degree.-950.degree. C.). Particulate solids in the off-gases from the combustion chamber of the reactor are separated out, and pass through one or more of a plurality of return conduits back to the combustion chamber. The temperature of the returning solids is controlled by positively cooling them, utilizing heat exchangers, within one or more of the conduits, and by controlling which of the conduits the solids flow through. Valves at the top of the conduits can control the flow of solids into the conduits. Alternatively U-shaped passageways at the bottom of the conduits between them and the combustion chamber can have fluidizing air injected therein, the injected air controlling the flow of solids out of the conduits into the combustion chamber.
    • 简单而有效的方法和装置将流化床反应器内的温度控制在所需范围内(例如约800-950℃)。 来自反应器的燃烧室的废气中的颗粒状固体被分离出来,并且通过多个返回导管中的一个或多个回到燃烧室。 回流固体的温度通过在一个或多个导管内利用热交换器进行正冷却来控制,并且通过控制固体流过哪个管道来控制。 导管顶部的阀门可以控制固体进入管道的流量。 或者在它们与燃烧室之间的导管底部的U形通道可以在其中注入流化空气,喷射的空气控制固体流出管道进入燃烧室。
    • 7. 发明授权
    • Fluidized bed reactor method and apparatus
    • 流化床反应器方法和装置
    • US5093085A
    • 1992-03-03
    • US161141
    • 1988-02-26
    • Folke EngstromReijo Kuivalaninen
    • Folke EngstromReijo Kuivalaninen
    • F23C10/24
    • F23C10/24B01J2208/00761
    • Fluidized bed reactor method and apparatus for removal of coarse material from the reactor. The apparatus comprises a discharge device including a substantially vertical pipe portion connected at one end with an outlet opening in the reactor grid, and at another end to an aeration chamber containing a discharge opening located below the level of the grid outlet opening; and a device for supplying pressurized air in short blasts of 30 to 100 milliseconds, preferably at pressures of from 2.5 to 7.0 bar, into the aeration chamber in the direction of the discharge opening to remove the coarse material from the reactor. Low pressure fluidizing air may be supplied to the vertical pipe portion as well as the aeration chamber to return small particles in the discharge device to the fluidization zone of the reactor.
    • 用于从反应器中除去粗物质的流化床反应器方法和装置。 该装置包括排放装置,该排放装置包括在一端与反应器格栅中的出口开口连接的基本上垂直的管部分,另一端包括位于格栅出口开口下方的排放口的通气室; 以及用于以30至100毫秒,优选2.5至7.0巴的压力将短气体的加压空气沿喷射口的方向供应到曝气室中以从反应器中除去粗物质的装置。 可以将低压流化空气供应到垂直管部分以及曝气室,以将排放装置中的小颗粒返回到反应器的流化区。