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    Coal decomposition method and equipment in cycle heating gas style
    51.
    发明授权
    Coal decomposition method and equipment in cycle heating gas style 有权
    煤分解方法和设备在循环加热气体样式

    公开(公告)号：US09260665B2

    公开(公告)日：2016-02-16

    申请号：US13578631

    申请日：2010-11-23

    申请人： Shucheng Zhu

    发明人： Shucheng Zhu

    IPC分类号： C10L5/00 ,  C10B49/04 ,  C10B57/00 ,  C10B47/00 ,  C10B37/00 ,  C10B53/04 ,  C10B1/10

    CPC分类号： C10B49/04 ,  C10B1/10 ,  C10B37/00 ,  C10B47/00 ,  C10B53/04 ,  C10B57/00

    摘要： The invention discloses a coal decomposition method and equipment in cycle heating gas style. The coal decomposition equipment can avoid introducing impurity, ensure a pure decomposed gas and keep continuous heating without extrinsic heat source, which includes an airtight kiln body with coal inlet and coal outlet; a facility for impelling and decomposing coal set in the kiln body; a coal decomposed gas collecting pipe set in one end of the airtight kiln body, and a high temperature gas input pipe set in the other end of the airtight kiln body; wherein the coal decomposed gas collecting pipe is connected with a post-processing facility and communicates with the high temperature gas input pipe through a circle pipe, and the circle pipe and/or the high temperature gas input pipe comprises a heating device.

    摘要翻译： 本发明公开了一种循环加热气体煤分解方法和设备。 煤分解装置可以避免引入杂质，确保纯分解气体，保持连续加热，无需外加热源，包括煤气入口和煤气出口的密闭窑体; 用于推动和分解窑体中的煤的设施; 设置在气密窑体的一端的煤分解气体收集管和设置在气密窑体的另一端的高温气体输入管; 其中，煤分解气体收集管与后处理设备连接，并通过圆管与高温气体输入管连通，圆管和/或高温气体输入管包括加热装置。

    SYSTEM AND PROCESS FOR CONVERTING WHOLE TIRES AND OTHER SOLID CARBON MATERIALS INTO RECLAIMABLE AND REUSABLE COMPONENTS
    55.
    发明申请
    SYSTEM AND PROCESS FOR CONVERTING WHOLE TIRES AND OTHER SOLID CARBON MATERIALS INTO RECLAIMABLE AND REUSABLE COMPONENTS 审中-公开
    将全轮胎和其他固体碳材料转化为可回收和可重复使用的组件的系统和方法

    公开(公告)号：US20130189182A1

    公开(公告)日：2013-07-25

    申请号：US13738173

    申请日：2013-01-10

    申请人： Fredrick Taylor

    发明人： Fredrick Taylor

    IPC分类号： C10B53/07

    CPC分类号： C10B53/07 ,  C01B32/05 ,  C09C1/48 ,  C10B1/10 ,  C10B47/00 ,  C10B47/18 ,  C10B47/30 ,  C10B53/00 ,  C10G1/00 ,  C10G1/02 ,  C10G1/10 ,  C10J2300/0946 ,  C22B7/001 ,  Y02P10/214 ,  Y02P20/143

    摘要： A system and method of converting tires or other solid carbon based material is disclosed, including providing a chamber, feeding the solid carbon based material into the chamber, rotating the chamber, heating and reducing the material in the chamber, collecting solid residue from the chamber, collecting vapor from the chamber, and converting vapor collected from the chamber to a liquid. In an embodiment, the material includes a whole tire. The tire is heated in the chamber causing the tire to collapse and liquefy, exposing the metal in the tire which aids in grinding the carbon material in the tire as it tumbles, collecting solid residue, for example tire carbons, and collecting vapor, for example vaporized oil, and benzene and methane gas from the chamber and converting the oil. The chamber may be heated to a temperature from about 350° F. to about 1100° F. using gases reclaimed from the material.

    摘要翻译： 公开了一种转换轮胎或其他固体碳基材料的系统和方法，包括提供腔室，将固体碳基材料进料到腔室中，旋转腔室，加热和还原腔室中的材料，从腔室收集固体残留物 从腔室收集蒸气，并将从腔室收集的蒸气转化为液体。 在一个实施例中，材料包括整个轮胎。 轮胎在腔室中被加热，导致轮胎塌陷和液化，使轮胎中的金属暴露，这有助于轮胎中的碳材料在其滚动时被研磨，收集固体残余物例如轮胎碳，并收集蒸汽，例如 蒸发的油，以及来自室的苯和甲烷气体并转化油。 可以使用从材料回收的气体将室加热至约350°F至约1100°F的温度。

    Method for the production of coke
    57.
    发明授权
    Method for the production of coke 失效
    生产焦炭的方法

    公开(公告)号：US4734165A

    公开(公告)日：1988-03-29

    申请号：US860218

    申请日：1986-05-06

    申请人： Hartmut Bauer ,  Dietrich Wagener ,  Egmar Wunderlich

    发明人： Hartmut Bauer ,  Dietrich Wagener ,  Egmar Wunderlich

    IPC分类号： C10B7/14 ,  C10B47/00 ,  C10B49/00 ,  C10B51/00

    CPC分类号： C10B7/14 ,  C10B47/00 ,  C10B49/00 ,  C10B51/00

    摘要： Coke is produced from coal by coking the coal, and optionally by drying and/or preheating the coal prior to coking, and further optionally by dry cooling the coke subsequent to coking. At least the coking step is achieved in a pressure tight container which may be a transportable or tippable container. The coking step is performed in the container by conducting a gas through the container in direct or indirect heat exchange relationship with the coal and forming coke. The coking step includes a phase of lump coke formation achieved by heating the coal in a temperature range of between approximately 250.degree. and 600.degree. C. by indirect heat exchange only.

    摘要翻译： 焦炭通过焦化煤而产生，并且任选地在焦化之前干燥和/或预热煤，并且进一步任选地通过在焦化之后干燥冷却焦炭。 至少焦化步骤在压力容器中实现，压力容器可以是可运输的或可翻转的容器。 通过与煤和成形焦直接或间接的热交换关系通过容器进行气体在容器中进行焦化步骤。 焦化步骤包括通过仅通过间接热交换在约250℃至600℃的温度范围内加热煤获得的块状焦炭形成阶段。

    Process and apparatus for producing nonaqueous coke slurry and pipeline transport thereof
    58.
    发明授权
    Process and apparatus for producing nonaqueous coke slurry and pipeline transport thereof 失效
    用于生产非水焦炭浆料的方法和设备及其管道输送

    公开(公告)号：US4208251A

    公开(公告)日：1980-06-17

    申请号：US916514

    申请日：1978-06-19

    申请人： Ross H. Rasmussen

    发明人： Ross H. Rasmussen

    IPC分类号： C10B7/10 ,  C10B47/00 ,  C10L1/32 ,  C10L5/00 ,  F17D1/08 ,  C10B47/18 ,  F17D1/00

    CPC分类号： C10L5/00 ,  C10B47/00 ,  C10B7/10 ,  C10L1/322 ,  F17D1/088 ,  Y10T137/0391

    摘要： A process comprising heating coal in a substantially air-free environment to liberate volatile materials and produce coke, condensing at least some of the volatile materials so liberated to liquefied products and dispersing the coke therein to form a coke slurry, feeding the coke slurry to a slurry pipeline, and pumping the coke slurry through the pipeline to a destination.Apparatus comprising a tube furnace having an external heating means for indirectly heating powdered coal therein in a substantially air-free environment to a temperature adequate to liberate volatile materials and produce coke, means to feed powdered coal to the furnace under pressure and force the volatile materials and coke produced in the furnace through the furnace to a condensing means in which at least some of the volatile materials are condensed with the coke dispersed therein to form a coke slurry, and means to convey the coke slurry from the condensing means to a pipeline for transport to a destination.

    摘要翻译： 一种方法，包括在基本无空气的环境中加热煤以释放挥发性物质并产生焦炭，将至少一些挥发性物质冷凝，从而释放出液化产物并将焦炭分散在其中以形成焦炭浆料，将焦炭浆料送入 泥浆管道，并将焦炭浆料通过管道泵送到目的地。 一种装置，它包括具有外部加热装置的管式炉，该外部加热装置用于在基本上无空气的环境中将其中的粉煤间接加热至足以释放挥发性物质并产生焦炭的温度，在压力下将粉煤送入炉中并迫使挥发性物质 和在炉中通过炉产生的焦炭到冷凝装置，其中至少一些挥发性物质与分散在其中的焦炭冷凝以形成焦炭浆料，以及将焦炭浆料从冷凝装置输送到管道的装置 运送到目的地。

    Method for controlling combustion in coke oven battery
    59.
    发明授权
    Method for controlling combustion in coke oven battery 失效
    焦炉电池燃烧控制方法

    公开(公告)号：US4045292A

    公开(公告)日：1977-08-30

    申请号：US701150

    申请日：1976-06-30

    申请人： Taro Matsushita ,  Masahiro Hiraki ,  Takeo Fujimura ,  Shinji Hasebe

    发明人： Taro Matsushita ,  Masahiro Hiraki ,  Takeo Fujimura ,  Shinji Hasebe

    IPC分类号： C10B21/10 ,  C10B21/20 ,  C10B47/00

    CPC分类号： C10B21/20 ,  C10B47/00

    摘要： In the operation of a conventional coke oven battery, a target flue temperature for each oven group is set on the basis of details of coal charge consisting of the weight, the particle size, the moisture content, the volatile matter content and the timing of charging of the coal charge, so as to achieve a target net coking time and a target soaking time given by a coke production schedule. Then, the temperature is measured for individual flues at certain intervals of time and deviations of thus measured flue temperatures from said target flue temperature are calculated by computer, to set a flow rate and a calorific value of the fuel gas for each oven group. A stack draft is set and controlled by computer so that an optimum combustion may take place in response to changes in the flow rate and the calorific value of the fuel gas. Said target flue temperature is furthermore bias-corrected with the use of a mean measured flue temperature, measured net coking times, measured soaking times and the details of coal charge corresponding thereto.

    摘要翻译： 在常规焦炉电池的操作中，基于由重量，颗粒尺寸，含水量，挥发物含量和充电时间组成的煤电荷的细节，设定每个烘箱组的目标烟道温度 的煤炭收费，以实现由焦炭生产计划给出的目标净焦化时间和目标浸泡时间。 然后，以一定的时间间隔测量单个烟道的温度，并通过计算机计算由所述目标烟道温度测量的烟道温度的偏差，以设定每个烤箱组的燃料气体的流量和发热量。 堆垛吃水由计算机设置和控制，使得响应于燃料气体的流量和热值的变化可以发生最佳燃烧。 所述目标烟道温度进一步通过使用平均测量烟道温度，测量的净焦化时间，测量的均热时间和对应于其的煤炭细节的细节进行偏差校正。