Method for continuously co-firing pulverized coal and a coal-water slurry
    42.
    发明授权
    Method for continuously co-firing pulverized coal and a coal-water slurry 失效
    连续共烧煤粉和水煤浆的方法

    公开(公告)号:US5380342A

    公开(公告)日:1995-01-10

    申请号:US85629

    申请日:1993-07-02

    CPC classification number: F23K1/02 F23C1/00 F23D1/005

    Abstract: A process is provided for burning a coal water slurry comprising providing clean coal fines of less than 100 mesh at about 50 weight % and water at about 50 weight % by co-firing the coal water slurry in a continuous stream with a separate stream of pulverized coal wherein about 80% of the total BTU output of the furnace is provided from the pulverized coal and approximately 20% of the BTU output is provided from the coal water slurry. First, a quarl in the furnace is preheated using natural gas, for example. The furnace is next fired with a fuel source of 60% pulverized coal and 40% natural gas. A coal water slurry with fines of minus 100 or smaller is subsequently gradually introduced into the furnace as the gas input is gradually decreased.

    Abstract translation: 提供了一种用于燃烧煤水浆料的方法,其包括以约50重量%提供小于100目的清洁煤细粉和约50重量%的水,通过将煤水浆料在连续流中与单独的粉碎物流共烧 其中炉的总BTU输出的约80%由粉煤提供,大约20%的BTU输出由煤水浆提供。 首先,例如,使用天然气预热炉内的。。。 炉子下一次用燃料源60%粉煤和40%天然气燃烧。 当气体输入逐渐减小时,随着小于等于或小于零的细粉的煤水浆料随后逐渐引入炉中。

    Process for producing a coal-water slurry
    44.
    发明授权
    Process for producing a coal-water slurry 失效
    生产水煤浆的工艺

    公开(公告)号:US4786289A

    公开(公告)日:1988-11-22

    申请号:US158070

    申请日:1988-02-12

    CPC classification number: C10L1/326 F23K1/02

    Abstract: A process for producing a coal-water slurry of low viscosity and high coal concentration with a low specific energy and a good efficiency is provided, which process comprises wet-grinding coal by means of a wet vertical ring-roll mill in the presence or absence of a surfactant and recycling a part of the coal ground by the mill, as it is, without classifying it, to the mill through a splitter.

    Abstract translation: 提供了具有低比能量和高效率的低粘度和高煤浓度的水煤浆的方法,该方法包括在存在或不存在下通过湿式立式环辊研磨机对煤进行湿磨 的表面活性剂,并且通过研磨机将磨碎的煤的一部分原样再循环,通过分离器将其分类到研磨机。

    Coal slurry system
    45.
    发明授权
    Coal slurry system 失效
    煤浆系统

    公开(公告)号:US4602483A

    公开(公告)日:1986-07-29

    申请号:US710302

    申请日:1985-03-08

    CPC classification number: F01K9/003 F23K1/02 F23K3/02

    Abstract: A slurry of liquified gas such as carbon dioxide and finely pulverized coal particles is provided in a mixing chamber and discharged from the chamber into a pipeline for conveyance to a power plant. During discharge from the mixing chamber pressurized gas at a sufficiently high pressure is injected above the slurry mix to maintain adequate pressure during discharge and prevent cavitation at the inlet port of pumping means employed in the pipeline. The slurry is depressurized at the downstream end of the pipeline by movement through pressure reduction means so that it is decompressed non-adiabatically and the coal and gas particles are separated. The gas remains at a low temperature and is passed in heat exchange relationship with cooling water from the power plant cooling tower to lower the temperature of same and consequently increase the efficiency of the power plant. In another embodiment the gas comprises carbon dioxide and a portion of the cool carbon dioxide is discharged directly into the basin of the cooling tower to reduce the water temperature and provide beneficial cooling water chemistry control.

    Abstract translation: 在混合室中设置二氧化碳和细粉煤颗粒等液化气体的浆液,并从室排出到输送到发电厂的管道中。 在从混合室排放期间,在浆料混合物上方注入足够高压力的压缩气体以在排放期间保持足够的压力并防止在管道中使用的泵送装置的入口处的空化。 通过运动通过减压装置在管道的下游端将浆料减压,使得其非绝热地减压,并分离煤和气体颗粒。 气体保持在低温,并与来自发电厂冷却塔的冷却水进行热交换,降低其温度,从而提高发电厂的效率。 在另一个实施方案中,气体包括二氧化碳,一部分冷二氧化碳直接排放到冷却塔的盆中以降低水温并提供有益的冷却水化学控制。

    Process for the production of a coal-water suspension which is suitable
for use in coal gasification under elevated pressure
    46.
    发明授权
    Process for the production of a coal-water suspension which is suitable for use in coal gasification under elevated pressure 失效
    生产适用于高压煤炭气化的煤 - 水悬浮液的方法

    公开(公告)号:US4526588A

    公开(公告)日:1985-07-02

    申请号:US490547

    申请日:1983-05-06

    CPC classification number: C10L5/00 C10L1/326 F23K1/02 Y10S48/01

    Abstract: A coal-water suspension containing 50 to 75 percent by weight coal, based on the weight of the suspension, the bulk of the coal having a particle size of 50 to 500 .mu.m, the proportion of the particles having a diameter greater than 0.5 mm in the coal being less than 15 percent by weight and the particle size distribution curve of the coal in the Rosin-Rammler particle size distribution grid according to DIN 4190 having a slope of .gtoreq.1; a process for the production of such water-coal suspension which is suitable for use in coal gasification under elevated pressure by mixing lump coal with water directly, the water being added in a concentration just sufficient to form a water-coal dust suspension suitable for the gasification reaction and grinding the resultant suspension in a disc attrition mill, a toothed disc attrition mill or a toothed colloid mill.

    Abstract translation: 含有50〜75重量%煤的煤 - 水悬浮液,基于悬浮液的重量,大部分煤的粒径为50〜500μm,直径大于0.5mm的粒子的比例 在小于15重量%的煤中,根据DIN 4190的Rosin-Rammler粒度分布网格中的煤的粒度分布曲线具有> / = 1的斜率; 一种用于生产这种水煤悬浮液的方法,其适用于在高压下通过将块煤与水直接混合而用于煤气化,所加入的水的浓度恰好足以形成适用于水煤灰的水煤灰悬浮液 气化反应并将所得悬浮液研磨在圆盘磨耗机,齿盘磨碎机或带齿胶体磨中。

    Pollution-free low temperature slurry combustion process utilizing the
super-critical state
    48.
    发明授权
    Pollution-free low temperature slurry combustion process utilizing the super-critical state 失效
    无污染的低温浆料燃烧过程利用超临界状态

    公开(公告)号:US4380960A

    公开(公告)日:1983-04-26

    申请号:US261143

    申请日:1981-05-06

    Abstract: A continuous process for the combustion of solid fuels under conditions such that flue gas is essentially free of particulates and oxides of sulfur and nitrogen. Fuel is charged as an aqueous slurry and additional water condensed from the flue gas may be recycled to the pressurized combustion zone. Combustion is promoted both by water vapor and alkali added with the fuel slurry, while the alkali serves also to neutralize and remove sulfur in completely oxidized, or sulfate, form. Heat of combustion raises the temperature of the reactants above the critical temperature of water, forming a hot fluid from which useful heat is transferred. Under the pressure of the system, heat recovery results in condensation of water, retaining and slurry product ash and providing recycle water, which helps to control reaction temperature as well as to promote the combustion.

    Abstract translation: 在使烟道气基本上不含硫和氮氧化物的条件下固体燃料燃烧的连续方法。 燃料作为含水浆料加料,并且从废气中冷凝的另外的水可以再循环到加压燃烧区。 通过添加有燃料浆料的水蒸气和碱来促进燃烧,而碱还用于中和和完全氧化或硫酸盐形式的硫。 燃烧的热量使反应物的温度升高到临界温度以上,形成热的流体,从中传递有用的热量。 在系统的压力下,热回收导致水,保留和浆料产物灰分的冷凝,并提供循环水,这有助于控制反应温度以及促进燃烧。

    Fuel producing system for solid/liquid mixtures
    49.
    发明授权
    Fuel producing system for solid/liquid mixtures 失效
    固体/液体混合物的燃料生产系统

    公开(公告)号:US4259022A

    公开(公告)日:1981-03-31

    申请号:US101858

    申请日:1979-12-10

    Applicant: Roy E. Folland

    Inventor: Roy E. Folland

    Abstract: A fuel producing system for a solid/liquid mixture. The system comprises a mixing reservoir having a first inlet for receiving a combustible liquid fuel, and a second inlet for receiving a solid fuel pulverized to a mixable state with said liquid fuel. Mixing means is provided in the mixing reservoir to mix both fuels. Quantitative control means is also provided in the reservoir to measure predetermined amounts of the liquid and solid fuels delivered therein. A holding reservoir receives the solid/liquid fuel mixture from an output conduit of the mixing reservoir. Pump means is provided in the output conduit. First control means is further provided to shut off the flow of the fuel mixture to the holding reservoir to permit the mixing of further fuel mixture in the mixing reservoir. A second control means initiates the flow of the fuel mixture to the holding tank when the mixture fluid therein is extracted to a predetermined low level.

    Abstract translation: 用于固体/液体混合物的燃料生产系统。 该系统包括具有用于接收可燃液体燃料的第一入口和用于接收与所述液体燃料粉碎至可混合状态的固体燃料的第二入口的混合容器。 在混合容器中设置混合装置以混合两种燃料。 定量控制装置还设置在储存器中以测量其中输送的液体和固体燃料的预定量。 保持容器从混合容器的输出管道接收固体/液体燃料混合物。 泵装置设置在输出管道中。 进一步提供第一控制装置以便将燃料混合物的流动截止到保持容器以允许在混合容器中混合进一步的燃料混合物。 当其中的混合流体被提取到预定的低水平时,第二控制装置启动燃料混合物到储存箱的流动。

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