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    • 1. 发明授权
    • Process for the solvent extraction of solid carbon-containing materials,
principally coal
    • 溶剂萃取固体含碳材料的方法,主要是煤
    • US4224136A
    • 1980-09-23
    • US958483
    • 1978-11-07
    • Heinz M. zu KockerJurgen Tietze
    • Heinz M. zu KockerJurgen Tietze
    • C10L9/04C10G1/04C10G1/06
    • C10G1/042
    • A solid carbonaceous material principally coal is subjected to a solvent extraction by[a] introducing a hydrogen donor-solvent and the carbonaceous particulate material into a generally vertically directed extraction zone at an elevated pressure;[b] imparting a continuous generally upwards directed flow to said solvent, the solvent being at a temperature above the softening temperature of the said particles and the pressure being higher than the vapor pressure of the solvent at said temperature, the flow velocity of the solvent being sufficient to cause fluidization of said particles;[c] withdrawing the solvent together with the formed extract continuously at the top of the extraction zone while preventing the entrainment of solid particles;[d] effecting the separation of the extract and solvent outside said extraction zone;[e] removing the remaining solid particles together with residual extract-free or extract-lean solvent from the extraction zone separate from the withdrawal at [c]; and[f] separating the solvent removed at [e] from the solid particles.
    • 通过[a]在高压下将氢供体 - 溶剂和碳质颗粒材料引入一般垂直取向的萃取区,将固体碳质材料主要进行溶剂萃取; [b]向所述溶剂施加连续的大致向上的流动,溶剂处于高于所述颗粒的软化温度的温度,并且压力高于溶剂在所述温度下的蒸气压,溶剂的流速 足以引起所述颗粒的流化; [c]在提取区的顶部连续地将所形成的提取物与所形成的提取物一起取出,同时防止固体颗粒的夹带; [d]在所述提取区域之外实现提取物和溶剂的分离; [e]将残留的固体颗粒与残留的无萃取物或贫提取物的溶剂从[c]分离出来的提取区除去; 和[f]将在[e]处除去的溶剂与固体颗粒分离。
    • 3. 发明授权
    • Heating system for regenerative coke ovens
    • 再生焦炉加热系统
    • US5259932A
    • 1993-11-09
    • US776278
    • 1991-11-22
    • Manfred BlaseUlrich KochanskiDietrich WagenerGunther MeyerHeinz DurselenDieter StalhermJoachim HoitzLudwig OffermannJurgen Tietze
    • Manfred BlaseUlrich KochanskiDietrich WagenerGunther MeyerHeinz DurselenDieter StalhermJoachim HoitzLudwig OffermannJurgen Tietze
    • C10B21/10C10B21/20C10B21/22C10B5/16C10B21/18
    • C10B21/22Y02P20/129
    • According to the invention the heating system for regenerative coke oven batteries that can be heated with rich gas and/or lean gas or mixed gas is provided comprising vertical flues cooperating in pairs, each vertical flue being connected to a regenerator for preheating the air and, in the case of lean gas operation, for preheating the lean gas or mixed gas. High and low combustion stages, as well as structure defining an internal flue gas return at levels above a flue base are provided. Discharge openings are provided at at least three levels for supplying each flue. A base discharge opening is provided at the flue base directly connected to regenerators. Hollow communicating channels are defined for connecting the regenerators to discharge openings located above the flue base. The hollow communicating channels are preferably formed in each communicating wall connected to a discharge opening leading only to one adjacent flue. The regenerators for preheating air are subdivided in a longitudinal direction of the oven with one part being connected to the base openings at the flue base and another part being connected to the hollow communicating channels. A regulating system is provided for setting the amount of air for the two parts separately. Pressure blocks are provided for setting the air distribution at the discharge openings provided above the flue base. The circulating flow openings are arranged at the foot of each flue in a hollow communicating wall between adjacent flues to provide ascending and descending flow.
    • PCT No.PCT / EP90 / 00838 Sec。 371日期1991年11月22日 102(e)1991年11月22日PCT PCT 1990年5月23日PCT公布。 出版物WO90 / 14408 日本1990年11月29日。根据本发明,提供可用富气体和/或贫气或混合气体加热的再生焦炉电池的加热系统,其包括成对配合的垂直烟道,每个垂直烟道连接到 用于预热空气的再生器,并且在贫气操作的情况下,用于预热贫气或混合气体。 提供高和低燃烧阶段,以及限定在烟道底部上方的内部烟气返回的结构。 在至少三个级别提供排放开口以供应每个烟道。 在与再生器直接连接的烟道底座处设置基座排出口。 定义了空心连通通道,用于将再生器连接到位于烟道底部上方的排放口。 中空连通通道优选地形成在连接到仅引导到相邻烟道的排放口的每个连通壁中。 用于预热空气的再生器在炉的纵向方向上分为一部分,其连接到烟道底部的基部开口,另一部分连接到中空连通通道。 提供了用于分别设置两个部件的空气量的调节系统。 提供压力块,用于设置在烟道底部上方的排放口处的空气分布。 循环流动开口布置在每个烟道的脚下相邻烟道之间的中空连通壁中,以提供上升和下降的流动。
    • 4. 发明授权
    • Shaft-like dry cooler for coke
    • 用于焦炭的轴式干燥冷却器
    • US4371425A
    • 1983-02-01
    • US255231
    • 1981-04-17
    • Wilhelm DanguillierWolfgang GramsJurgen Tietze
    • Wilhelm DanguillierWolfgang GramsJurgen Tietze
    • C10B39/02
    • C10B39/02
    • Coke is dry cooled in a shaft-like cooler by gases conveyed through the coke. The cooler comprises a top antechamber below a charging opening, a cooling chamber under the antechamber and having a gas inlet and a coke outlet at the bottom end. Between the antechamber and the cooling chamber, there is a cylindrical wall having a gas inlet. The cooling chamber is divided by radial walls which abut a central masonry core and divide the chamber into three shaft-like chambers to insure uniform descending of the coke. A prop is placed at the center of each component shaft for deflecting the descending coke from a central region. Cooling gas is supplied through a pipe having a downwardly-directed opening below a central masonry core. Additional cooling gas is supplied by an annular chamber surrounding a cone at a coke outlet of the cooling chamber.
    • 焦炭通过输送通过焦炭的气体在轴状冷却器中进行干式冷却。 冷却器包括在充电开口下方的顶部前室,在前室下方的冷却室,并且在底端具有气体入口和焦炭出口。 在前厅和冷却室之间有一个具有气体入口的圆柱形壁。 冷却室由径向壁分隔,该径壁邻接中心砖石芯并将室分成三个轴状室,以确保焦炭均匀下降。 支柱放置在每个部件轴的中心,用于将下降的焦炭从中心区域偏转。 冷却气体通过在中央砖石芯下方具有向下开口的管道供应。 另外的冷却气体由围绕冷却室的焦炭出口处的锥体的环形室供应。
    • 6. 发明授权
    • Shaft cooler for the dry quenching of coke
    • 用于干熄焦的轴冷却器
    • US4708196A
    • 1987-11-24
    • US604653
    • 1984-03-23
    • Jurgen TietzeWilhelm DanguillierHeinz ThubeavilleSiegfried PohlFriedrich Muller
    • Jurgen TietzeWilhelm DanguillierHeinz ThubeavilleSiegfried PohlFriedrich Muller
    • C10B39/02C10B39/00
    • C10B39/02Y02P20/129
    • A shaft cooler for dry quenching of coke includes an inner masonry ring that is an independent structure suspended on the top edge of the outer masonry of the shaft cooler. The weight of the inner masonry ring is carried by stays which bear on the top edge of the outer masonry. The tubular stays are disposed in one embodiment inside the masonry ring and in another embodiment outside the masonry ring. The tubular stays are connected to ring mains for conducting a coolant medium. When the tubular stays are disposed outside the masonry ring, parallel tubes are interconnected along their entire length by webs to form a closed steel ring. Ring tubes are welded to the top and bottom ends to serve as a heat exchanger and are connected to the evaporator section of a waste-heat boiler of the shaft cooler. Flue-gas passages are formed at the bottom edge of the masonry ring by radially, spaced-apart webs.
    • PCT No.PCT / DE83 / 00128 Sec。 371日期1984年3月23日 102(e)1984年3月23日PCT提交1983年7月22日PCT公布。 公开号WO84 / 00557 日本1984年2月16日。用于焦炭干法淬火的轴冷却器包括内部砖石环,其是悬挂在轴冷却器的外部砖石顶部边缘上的独立结构。 内部砖石环的重量由承载在外部砖石顶部边缘的支撑物承载。 在一个实施例中,管状支柱设置在砌筑环内,在另一实施例中设置在砖石环外。 管状支架连接到环形电源,用于导电冷却剂介质。 当管状支柱设置在砌筑环的外侧时,平行的管子通过腹板沿其整个长度相互连接以形成封闭的钢环。 环管被焊接到顶端和底端以用作热交换器并且连接到轴冷却器的废热锅炉的蒸发器部分。 烟道通过径向隔开的纤维网形成在砖石环的底部边缘处。