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    • 21. 发明授权
    • Method and apparatus for indirectly drying and preheating fine material
    • 间接干燥和预热精细材料的方法和装置
    • US4422846A
    • 1983-12-27
    • US394838
    • 1982-07-02
    • Heinrich WeberKurt LorenzHorst Dungs
    • Heinrich WeberKurt LorenzHorst Dungs
    • F26B17/32F26B1/00F26B3/24F26B23/00F27B7/10
    • F26B23/001F26B1/00F26B3/24Y02P70/405
    • A method and apparatus is disclosed for indirectly drying and preheating fine material, in particular, moisture containing coal or the like, comprises, providing a rotary drum which is mounted for rotation and has a plurality of heating tubes extending therethrough, supplying heated cooling gas from a dry coke cooling system to the heating tubes, supplying the moist material to the drum, adjacent the bottom thereof, removing the material from the drum after it has been predried and preheated, and returning or recycling a portion of the predried and preheated material to the rotary drum. The method and apparatus utilizes the heated cooling gas used to cool dry coke in a dry coke cooling plant from high temperatures to below 200.degree. C. It has been found that such heated cooling gas for a selected amount of dry coke is useful either in a series of more than one rotary drum or, to process moist material in a single rotary drum and also generate steam as a byproduct.
    • 公开了一种用于间接干燥和预热细材料,特别是包含煤等的水分的方法和装置,包括:提供旋转滚筒,该滚筒安装成旋转并具有多个从其延伸的加热管,将加热的冷却气体从 干燥的焦炭冷却系统到加热管,将湿物料供应到滚筒,邻近其底部,在预干燥和预热之后从滚筒中除去材料,并将预干燥和预热的材料的一部分返回或再循环到 旋转鼓。 该方法和装置利用加热的冷却气体将干燥焦炭冷却设备中的干焦从高温冷却至低于200℃。已经发现,用于所选量的干焦的这种加热的冷却气体可用于 一系列多个旋转鼓,或在单个旋转鼓中处理湿物质,并产生蒸汽作为副产物。
    • 22. 发明授权
    • Apparatus for producing abrasion resistant coke from brown coal briquets
    • 用于生产棕煤煤的耐磨焦炭的设备
    • US4259158A
    • 1981-03-31
    • US61917
    • 1979-07-30
    • Heinrich WeberKurt LorenzHorst DungsRoman KurtzHans-Joachim Kersting
    • Heinrich WeberKurt LorenzHorst DungsRoman KurtzHans-Joachim Kersting
    • C10B49/06C10B53/08C10B1/04
    • C10B53/08
    • A method of producing abrasion resistant coke from brown coal briquets in a shaft furnace comprises charging the coke briquets into the top of the furnace and removing coke from the bottom of the furnace while directing inert hot combustion gases into the furnace and through the briquets at a plurality of vertically spaced levels throughout the height of the shaft furnace. Gases are directed at temperatures to effect and successively lower stages of the furnace the preheating, predrying, carbonization, and cooling of the charge. In accordance with a feature of the invention, gases are collected in each of the preheating and predrying stages by the use of a tubular suction arm which extends substantially across the width of the furnace and includes a performated bottom and sidewalls which extend partly below the bottom and are provided with a saw-tooth configuration so as to withdraw the gases through the space below the bottom and through the perforations of the bottom and to effect entrainment of dust from the charge in so doing. The shaft furnace construction for carrying out the method includes means for circulating the hot gases into each of the stages and the closed tubular suction arm which extends substantially across the whole width of the furnace in each of the preheating and predrying stages includes a bottom perforated wall and side walls which extend downwardly beyond the bottom and arranged so as to draw off a percentage of the gases from the associated stage and in so doing prevent the outflow dust along with the gases. The construction is such that about 10% of the gases is evacuated below the perforated bottom and then up through the bottom and withdrawn through the suction arm.
    • 在竖炉中从褐煤块生产耐磨焦炭的方法包括将焦炭块装入炉的顶部并从炉底排出焦炭,同时将惰性热燃烧气体引入炉中并通过一块 多个垂直间隔的水平位于竖炉的高度。 气体被引导到温度的作用并连续降低炉的预热,预干燥,碳化和冷却的阶段。 根据本发明的特征,通过使用基本上跨过炉子的宽度延伸的管状抽吸臂将气体收集在每个预热和预干燥阶段中,并且包括表面的底部和侧壁,其部分地在底部下方延伸 并且设置有锯齿构造,以便通过底部下方的空间并通过底部的穿孔抽出气体,并且这样进行夹带灰尘。 用于执行该方法的竖炉结构包括用于将热气体循环到每个级中的装置,并且在每个预热和预干燥阶段中基本跨过炉的整个宽度延伸的封闭管状抽吸臂包括底部穿孔壁 以及侧壁,其向下延伸超出底部并且被布置成从相关联的阶段排出一定百分比的气体,并且因此防止流出灰尘与气体一起流出。 该结构使得约10%的气体在穿孔底部下抽真空,然后通过底部抽出,并通过抽吸臂抽出。
    • 23. 发明授权
    • Method and apparatus for producing abrasion resistant coke from brown
coal briquets
    • 从褐煤砖生产耐磨焦炭的方法和设备
    • US4231844A
    • 1980-11-04
    • US18870
    • 1979-03-09
    • Heinrich WeberKurt LorenzHorst DungsRoman KurtzHans-Joachim Kersting
    • Heinrich WeberKurt LorenzHorst DungsRoman KurtzHans-Joachim Kersting
    • C10B49/06C10B53/08C10B3/00
    • C10B53/08
    • A method of producing abrasion resistant coke from brown coal briquets in a shaft furnace comprises charging the coke briquets into the top of the furnace and removing coke from the bottom of the furnace while directing inert hot combustion gases into the furnace and through the briquets at a plurality of vertically spaced levels throughout the height of the shaft furnace. Gases are directed at temperatures to effect and successively lower stages of the furnace the preheating, predrying, carbonization, and cooling of the charge. Gases are collected in each of the preheating and predrying stages by the use of a tubular suction arm which extends substantially across the width of the furnace and includes a performated bottom and sidewalls which extend partly below the bottom and are provided with a saw-tooth configuration so as to withdraw the gases through the space below the bottom and through the perforations of the bottom and to effect entrainment of dust from the charge in so doing. The shaft furnace includes means for circulating the hot gases into each of the stages. Hot inert combustion gases are introduced into the circulating gases to avoid condensation of liquids.
    • 一种在竖炉中由棕色煤砖生产耐磨焦炭的方法包括将焦炭块装入炉子顶部,并从炉底排出焦炭,同时将惰性热燃烧气体引入炉内,并在一 多个垂直间隔的水平位于竖炉的高度。 气体被引导到温度的作用并连续降低炉的预热,预干燥,碳化和冷却的阶段。 通过使用基本上跨过炉子的宽度延伸的管状抽吸臂将气体收集在每个预热阶段和预干燥阶段中,该管状抽吸臂包括在底部部分延伸并且具有锯齿构造的表面底部和侧壁 以便将气体通过底部下方的空间并通过底部的穿孔抽出,并且在这样做时引起来自电荷的灰尘的夹带。 竖炉包括用于将热气体循环到每个级中的装置。 将热惰性燃烧气体引入循环气体中以避免液体冷凝。
    • 25. 发明授权
    • Method for producing non-abrasive coke forms from brown-coal briquets
    • 从褐煤砖生产非磨料焦炭形式的方法
    • US4134794A
    • 1979-01-16
    • US837448
    • 1977-09-28
    • Kurt LorenzHorst DungsPeter Speich
    • Kurt LorenzHorst DungsPeter Speich
    • C10B53/08C10B17/00C10B21/02C10B21/12
    • C10B53/08
    • The coke forms are produced in four stages, each constituted by a respective oven chamber, and in which the briquets are, respectively, preheated, dehydrated or dried, carbonized and cooled. Hot gas circuits are provided, in which the hot gas is composed substantially of burnt lean gas of the carbonization, and, for each stage, the hot gases are recirculated in a separate respective circuit. In the preheating, dehydrating and carbonization stages, the hot gases are heated and produced, or supplemented, in a respective separate combustion chamber with the recirculating hot gas in the carbonization stage being supplemented with cooled lean gas from this stage. The recirculating hot gases are dedusted separately in a dust settling chamber in which their flow velocity is reduced to approximately 0.2 to 2.0 m/sec, with the dust being collected. Steam may be added to the recirculating hot gas of the preheating stage, drying stage, or both, and the pressure in the hot gas circuits is maintained at a level slightly higher than atmospheric pressure. The oven chambers are arranged as a vertical oven block plant and the oven chambers are interconnected with each other by transition zones which are conically narrowed to approximately one half of the cross section of the chamber and then widened up to the full cross section. The hot gas inlets are provided in the transition zones at the lower ends of the oven chambers, and the hot gas outlets are provided in the transition zones at the upper ends of the chambers. The dust settling chambers are provided immediately adjacent the hot gas outlets, and the carbonization chamber is surrounded by its combustion chamber to form an operating unit. SPCROSS-REFERENCE TO RELATED APPLICATIONSThis is a continuation of application Ser. No. 660,153, filed Feb. 23, 1976, now abandoned.
    • 焦炭形式分四个阶段生产,每个阶段分别由相应的烘箱室构成,其中将砖块分别预热,脱水或干燥,碳化和冷却。 提供了热气体回路,其中热气体基本上由碳化的燃烧的贫气组成,并且对于每个阶段,热气体在单独的相应回路中再循环。 在预热,脱水和碳化阶段,热气体在相应的单独的燃烧室中被加热和生产或补充,碳化阶段中的再循环热气体从该阶段补充冷却的贫气。 再循环的热气体在灰尘沉降室中单独除尘,其中它们的流速降低到约0.2至2.0m / sec,灰尘被收集。 可以将蒸汽加入到预热段,干燥阶段或两者的再循环热气体中,并且将热气回路中的压力保持在略高于大气压的水平。 烤箱室被布置成垂直的烤箱装置,并且烤箱室通过过渡区彼此互连,过渡区被锥形变窄到室的横截面的大约一半,然后被加宽到整个横截面。 热气体入口设置在烘箱室的下端的过渡区域中,热气体出口设置在室的上端的过渡区域中。 灰尘沉降室紧邻热气出口设置,碳化室由其燃烧室包围以形成操作单元。
    • 26. 发明授权
    • Process for removing dust from dry cooled coke
    • 从干燥冷却焦炭中除去灰尘的方法
    • US4792382A
    • 1988-12-20
    • US936183
    • 1986-12-01
    • Kurt LorenzHorst DungsKlaus MrongowiusJost-Wilfried Gehrhardt
    • Kurt LorenzHorst DungsKlaus MrongowiusJost-Wilfried Gehrhardt
    • C10B39/00C10B39/02
    • C10B39/02C10B39/00
    • The invention concerns a process for removing dust from coke cooled by a dry method after the coke has left the cooling zone of a cooling chamber, and a device for carrying out the process. A dust-free flushing gas is injected below the cooling zone, preferably parallel to the direction in which the coke moves when it has been cooled to below 200.degree. C., to draw the gas off above the discharge lock together with the stirred-up coke dust, and to recirculate the gas after the dust is removed from it. As an alternative, compressed air is blown through the coke after it has left the lock and while it is being transported through a vibrating machine. The coke is cooled in a dry cooling unit to below 200.degree. C. and preferably 130.degree. to 180.degree. C. The coke is then cooled outside the dry cooling unit by means of air at about 50.degree. to 90.degree. C. and preferably 70.degree. to 80.degree. C. Either simultaneously with or immediately after the cooling step with air, the coke is moistened, for example by sprinkling or spraying, to a residual moisture of 2% to 4% by weight and preferably 2% to 3% by weight.
    • 本发明涉及一种在焦炭离开冷却室的冷却区之后通过干法冷却的焦炭除去灰尘的方法和用于进行该方法的装置。 当冷却至低于200℃时,无尘冲洗气体被注入到冷却区的下方,优选平行于焦炭移动的方向,以将气体与排出口一起排出 焦炭粉尘,并且在灰尘从其中除去之后再循环气体。 作为替代方案,压缩空气在其离开锁定之后并且通过振动机被输送时通过焦炭吹送。 将焦炭在干燥冷却装置中冷却至低于200℃,优选130℃至180℃。然后将焦炭通过空气在约50-90℃下冷却至干燥冷却装置外,优选70℃ 在与空气同时或立即冷却步骤之后,将焦炭例如通过喷洒或喷雾润湿至2%至4%重量比,优选2%至3%的残余水分,通过 重量。
    • 27. 发明授权
    • Apparatus with two-stage heating for carbonizing cold-compacted
briquettes
    • 具有两段加热用于碳化冷压实压块的装置
    • US4544451A
    • 1985-10-01
    • US580794
    • 1984-02-16
    • Heinrich WeberKurt LorenzHorst Dungs
    • Heinrich WeberKurt LorenzHorst Dungs
    • C10B53/08C10L5/16C10L5/20C10B1/04C10B3/02
    • C10L5/16C10B53/08C10L5/20Y02P20/129
    • Briquettes made from bituminous or sub-bituminous coal or peat are produced by grinding the coal, mixing it with a binder and compacting the mixture. They are then carbonized in a continuous process in a shaft oven. The coal may be predried and the finished briquettes may be preheated, with a subsequent drying and hardening. The carbonization is effected in two stages in an indirectly heated shaft oven, with the evolved gas being taken off about at the mid-height of the oven shaft, processed, and used for heating in the second, high-temperature stage. The flue gases from this high-temperature stage are used for heating in the first stage and for preheating. The second or high-temperature stage is followed by a cooling stage where the gases evolved in the second stage, and mainly comprising hydrogen are used and circulated. The evolved gas in excess is continuously removed from the cooling circuit.
    • 由沥青或次烟煤或泥炭制成的团块通过研磨煤,与粘合剂混合并压实混合物来生产。 然后将它们在轴烘箱中以连续的方法碳化。 煤可以预干燥,并且可以预热完成的团块,随后进行干燥和硬化。 在间接加热的竖炉中分两步进行碳化,放出的气体在烘箱轴的中间高度处被取出,进行处理,并用于第二高温阶段的加热。 来自该高温阶段的烟气用于第一阶段的加热和预热。 第二或高温阶段之后是冷却阶段,其中在第二阶段中放出的气体和主要包含氢的气体被使用和循环。 过量的放出气体从冷却回路连续地移出。
    • 28. 发明授权
    • Method for dry cooling coke and coke cooler to implement the method
    • 干法冷却焦炭和焦炭冷却器实施方法
    • US4370202A
    • 1983-01-25
    • US208316
    • 1980-11-19
    • Heinrich WeberKurt LorenzHorst Dungs
    • Heinrich WeberKurt LorenzHorst Dungs
    • C10B39/02C10B39/00
    • C10B39/02Y02P20/129
    • A coke cooler and method of operating the cooler is disclosed for dry cooling hot glowing coke through the recovery of the sensible heat of the hot glowing coke. The apparatus includes a vertically elongated vessel having walls partially formed with integral heat exchange tubes for the passage of a liquid coolant and a shroud having an internal prechamber mounted in the upper end of the vessel for receiving a charge of the hot glowing coke. The shroud cooperates with the vessel to provide a annular passage for fluid flow therebetween of a gas which directly contacts the hot glowing coke for direct cooling while liquid coolant is passed through the tubes for indirectly cooling the coke.
    • 公开了一种用于干燥冷热焦炭的焦炭冷却器和操作冷却器的方法,其通过回收热发热焦炭的显热。 该装置包括垂直细长的容器,其具有部分地形成有用于液体冷却剂通过的整体热交换管的壁和具有安装在容器的上端中的内部前置室的护罩,用于接收热发热焦炭的装料。 护罩与容器配合以提供环形通道,用于在其间直接接触热发光焦炭的气体之间流体流动,用于直接冷却,同时液体冷却剂通过用于间接冷却焦炭的管。
    • 29. 发明授权
    • Process for the production of molded metallurgical coke from coal
briquettes
    • 从煤球生产成型冶金焦的方法
    • US4305788A
    • 1981-12-15
    • US135112
    • 1980-03-28
    • Heinrich WeberKurt LorenzHorst DungsKlaus Urbye
    • Heinrich WeberKurt LorenzHorst DungsKlaus Urbye
    • C10B53/08C10B47/18
    • C10B53/08Y02P20/129
    • The process for the production of molded metallurgical coke from dried coal or fine coal mixtures with a low swelling index particularly highly volatile fine coal comprises mixing normal washed fine coal or fine coal mixtures of a grain size of from 0 to 10 mm and a swelling index of not more than 5 with a binder, pressing the mixture into briquettes, oxidizing the briquettes in a continuous material flow stream, and coking the oxidized briquettes continuously in an oven chamber by supplying indirectly and exhausting the coke oven gases with a temperature of 300.degree. to 1200.degree. C. The device for carrying out the process includes a vertically extending reactor housing having an oxidation chamber adjacent the top thereof with an indirectly heated vertical coking chamber directly below the oxidation chamber and with a cooling chamber directly below the coking chamber and including means for circulating heating gases into the coking chamber and then upwardly through the coking chamber and out adjacent the top of the coking chamber and into the oxidation chamber.
    • 从干燥煤或具有低膨胀率特别是高挥发性细煤的细煤混合物生产成型冶金焦的方法包括混合正常洗涤的细煤或0至10mm的粒度的细煤混合物和溶胀指数 不超过5的粘合剂,将混合物压成团块,以连续的材料流动流将煤块氧化,并在室温炉中连续地将氧化的团块进行间歇加热并排出温度为300°C的焦化炉气体 用于进行该方法的装置包括垂直延伸的反应器壳体,其具有邻近其顶部的氧化室,其具有在氧化室正下方的间接加热的垂直焦化室,以及直接在焦化室下方的冷却室,并且包括 将加热气体循环进入焦化室,然后向上通过焦化室的装置 离开焦化室的顶部并进入氧化室。
    • 30. 发明授权
    • Method of producing abrasion-proof coke forms from bituminous coal,
brown coal or peat briquets
    • 从烟煤,褐煤或泥炭块生产耐磨焦炭的方法
    • US4259157A
    • 1981-03-31
    • US30939
    • 1979-04-17
    • Kurt LorenzHorst DungsHans B. KoenigsRoman Kurtz
    • Kurt LorenzHorst DungsHans B. KoenigsRoman Kurtz
    • C10B3/00C10B53/08C10B57/10C10B39/00C10B47/20C10L5/28
    • C10B53/08C10B3/00C10B57/10
    • Abrasion-proof coke forms are produced from bituminous coal, brown coal, or peat in the form of briquets, by preheating the briquets, dehydrating or predrying them, carbonizing them and then cooling them in at least three separate stages in which the briquets are dehydrated indirectly by subjecting them to indirect temperature conditions, producing a temperature gradient in the briquets. The briquets are automatically fed into a shaft tower which includes an upper drying shaft portion made up of a plurality of stacked radiators which include tube elements for the passing of a heating fluid, such as steam, therethrough and which define vertical shaft passages through which the briquet forms are passed downwardly and into a carbonizing shaft which has separate gas channels for directing heating gases therethrough and to a heating flue and which subsequently includes a lower cooling zone through which the briquets pass and then into a discharge channel where they are delivered for classification.
    • 耐火焦炭形式是由煤焦煤,褐煤或泥炭以砖块的形式生产的,通过预热砖块,将其脱水或预干燥,将其碳化,然后至少在三个不同的阶段将其冷却,其中砖块脱水 间接通过使它们处于间接温度条件下,在砖块中产生温度梯度。 该砖被自动地供入到塔架中,该塔架包括由多个堆叠式散热器构成的上部干燥轴部分,该多个堆叠式散热器包括用于使诸如蒸汽的加热流体通过的管状元件,并且限定垂直的轴通道, 砖块形式向下通入碳化轴,其具有用于将加热气体引导通过的气体通道和加热烟道,并且随后包括下部冷却区域,通过该下部冷却区域,煤块通过该冷却区域,然后进入排出通道,在那里它们被分配 。