公开(公告)号：US20120067607A1

公开(公告)日：2012-03-22

申请号：US13235964

申请日：2011-09-19

申请人： Heinrich Weber ,  Juergen Blickle

发明人： Heinrich Weber ,  Juergen Blickle

IPC分类号： B25F5/00

CPC分类号： B24B23/04 ,  B23Q5/04 ,  B24B27/08 ,  B24B47/16 ,  B25F5/00 ,  B27B19/006 ,  F16H21/52 ,  F16H35/18

摘要： The invention discloses a portable tool having a housing with a gearhead, having a motor shaft which can be rotationally driven by a motor and which can be coupled via an eccentric coupling drive to a tool spindle for the drive thereof, wherein the tool spindle can be driven in a rotational oscillatory manner about the longitudinal axis thereof and is configured for accommodating a tool, wherein a motion-reversal drive is provided which is configured for converting an oscillating drive movement produced by the eccentric coupling drive into an oscillating output movement which has a direction of oscillation opposed to said drive movement. The motion-reversal drive is configured as an epicyclic gearing.

摘要翻译： 本发明公开了一种具有齿轮箱的壳体的便携式工具，其具有可由电动机旋转驱动的电动机轴，并且可以通过偏心联接驱动联接到用于其驱动的工具主轴，其中工具主轴可以 以其旋转振荡方式围绕其纵向轴线驱动并且被配置为容纳工具，其中提供了运动反转驱动器，其被构造成将由偏心联接驱动器产生的振荡驱动运动转换成振荡输出运动，该振荡输出运动具有 与所述驱动运动相反的振荡方向。 运动反转驱动器配置为行星齿轮传动装置。

公开(公告)号：US5335546A

公开(公告)日：1994-08-09

申请号：US761788

申请日：1991-09-19

申请人： Bernhard Karbach ,  Reinhard Prause ,  Heinrich Weber

发明人： Bernhard Karbach ,  Reinhard Prause ,  Heinrich Weber

IPC分类号： G01N29/04 ,  G01N29/26

CPC分类号： G01N29/26

摘要： In a process for ultrasonic testing of elongated, prism-shaped sections (22) with at least one planar outer surface (54) extending along the longitudinal axis (26) of the section, with the objective of detecting material defects or verifying geometric data, the section (22) to be tested is exposed to ultrasonic beams from several ultrasonic probes (28 to 34) installed in a probe carrier (44). The section (22) is moved along its longitudinal axis (26) in relation to the probe carrier (44). The latter is installed in the rotor (20) of a rotary testing machine which rotates around the longitudinal axis (26) of the section (22). The probes (28 to 34) are installed in the probe carrier (44) so that each can be displaced individually, either transversely or, preferably, at right angles to the longitudinal axis (26) if the section (22) and the direction of the probes and/or so that their angular position can be adjusted individually by swivelling them around a swivel axis ( 58) running parallel to the longitudinal axis (26) of the section (22). The individual probes (28 to 34) are adjusted so that the central beams (46) emitted by each probe (28 to 34 ) impinge upon the planar outer surface (54) adjacent to one another, thus forming adjacent scanning zones in the volume of the section (22) to be tested. The probes (28 to 34) are triggered individually by an arrangement for determining the angle between the rotor (20) and the section (22); testing is only performed when the angle between the central beam (46 and the planar outer surface (54) lies within a predetermined range.

公开(公告)号：US4422857A

公开(公告)日：1983-12-27

申请号：US398593

申请日：1982-07-15

申请人： Heinrich Weber ,  Horst Dungs ,  Kurt Tippmer

发明人： Heinrich Weber ,  Horst Dungs ,  Kurt Tippmer

IPC分类号： C10J3/02 ,  C10J3/30 ,  C10J3/06 ,  C10J3/16

CPC分类号： C10J3/02 ,  C10J3/30 ,  C10J3/721 ,  C10J3/78 ,  C10J2300/0943 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0969 ,  C10J2300/0976

摘要： A method for the gasification of coke is disclosed in which coke produced in a coking chamber and having a temperature of 900.degree. C. to 1100.degree. C. is forced into a coke bucket, after coking in the coking chamber, and fed by means of hot coke conveyors without substantial temperature changes to a gasifier. The coke is gasified in the gasifier while adding at least one of oxygen and air, and steam and carbon dioxide.

摘要翻译： 公开了一种焦化气化方法，其中在焦化室中产生的温度为900℃至1100℃的焦炭在焦化室中焦化后被迫进入焦炭桶，并通过 热焦炭输送机没有对气化炉的实质温度变化。 焦炭在气化器中气化，同时加入氧气和空气中的至少一种，以及蒸汽和二氧化碳。

公开(公告)号：US4379692A

公开(公告)日：1983-04-12

申请号：US289235

申请日：1981-08-03

申请人： Heinrich Weber ,  Kurt Lorenz ,  Horst Dungs

发明人： Heinrich Weber ,  Kurt Lorenz ,  Horst Dungs

IPC分类号： C10B53/06 ,  B01J6/00 ,  C04B7/44 ,  C10B57/10 ,  F26B3/26 ,  F26B17/00 ,  F26B17/16 ,  F26B3/00 ,  F26B17/12

CPC分类号： F26B3/26

摘要： A preheating moist fine material, such as pit coal and lignate, peat, wood, oil shale, or even ores or limestone for cement production, and an apparatus for carrying out the method are disclosed. Moist fine material is mixed above a heater with predried and preheated material until the mixture is made fluid. The fluid mixture slides down between and piles up to a level above the heater. A part of the predried and preheated fine material is removed from below the heater in an amount corresponding to another part thereof and is conveyed to above the heater with the moist fine material.

摘要翻译： 公开了一种预热湿润精细材料，例如煤矿和木质素，泥炭，木材，油页岩，甚至用于水泥生产的矿石或石灰石，以及用于实施该方法的装置。 潮湿的细料在预热和预热的材料上混合在加热器上方，直到混合物成为流体。 流体混合物向下滑动并堆积到加热器上方的水平面上。 预干燥和预热的细材料的一部分从加热器的下方以与其另一部分相对应的量被除去，并用湿的精细材料输送到加热器的上方。

公开(公告)号：US4352720A

公开(公告)日：1982-10-05

申请号：US201262

申请日：1980-10-27

申请人： Heinrich Weber ,  Kurt Lorenz ,  Horst Dungs ,  Klaus Urbye

发明人： Heinrich Weber ,  Kurt Lorenz ,  Horst Dungs ,  Klaus Urbye

IPC分类号： C10B53/08 ,  C10B1/04

CPC分类号： C10B53/08 ,  Y02P20/129

摘要： 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.

摘要翻译： 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。

公开(公告)号：US4302430A

公开(公告)日：1981-11-24

申请号：US144038

申请日：1980-04-28

申请人： Heinrich Weber ,  Dieter Laufhutte

发明人： Heinrich Weber ,  Dieter Laufhutte

IPC分类号： B01D3/00 ,  C02F1/20 ,  C10K1/12 ,  C01C1/10

CPC分类号： C10K1/12

摘要： A process for releasing ammonia which is bound in coal water using a pre-desulfurization plant having ammonia and hydrogen sulfide scrubbers through which crude coking plant gas is passed comprises circulating the crude coke oven gases through the hydrogen sulfide scrubber and the ammonia scrubber in succession, directing the coal water first through the ammonia scrubber while the crude coking plant gases are being also circulated therethrough after passing it first through the hydrogen sulfide scrubber. An alkali solution is also circulated through the ammonia scrubber to enrich the solution with acid components and to liberate ammonia bound in the coal water directing the coal water which has been enriched from the ammonia scrubber into the hydrogen sulfide scrubber. The process is characterized by the fact that the alkali solution which has first served for the hydrogen sulfide scrubber is added to the ammonia hydrogen sulfide scrubber. 80 to 90% of the total alkali solution is charged to the hydrogen sulfide after-washery and then on the hydrogen sulfide pre-washery and the rest is charged to an ammonia expulsion apparatus.

摘要翻译： 使用具有氨和硫化氢洗涤器的预脱硫装置在煤水中结合的氨的方法，通过粗制焦化装置气体通过该脱硫装置包括循环粗炼焦气体通过硫化氢洗涤器和氨洗涤器， 首先通过氨洗涤器引导煤水，同时粗炼焦设备气体首先通过硫化氢洗涤器之后也循环通过。 碱性溶液也循环通过氨洗涤器以富含酸组分的溶液，并释放在煤水中结合的氨，将已经从氨洗涤器中富集的煤水引入硫化氢洗涤器。 该方法的特征在于首先将用于硫化氢洗涤器的碱溶液加入氨硫化氢洗涤器中。 将总碱性溶液的80-90％装入硫化氢洗涤后，然后在硫化氢预洗涤器上，将其余的装入氨排出装置中。

公开(公告)号：US4248603A

公开(公告)日：1981-02-03

申请号：US76379

申请日：1979-09-17

申请人： Heinrich Weber ,  Horst Dungs ,  Fritz Ferdinand ,  Yves Brasseur ,  Henri Birscheidt

发明人： Heinrich Weber ,  Horst Dungs ,  Fritz Ferdinand ,  Yves Brasseur ,  Henri Birscheidt

IPC分类号： C10B53/08 ,  C10L5/08 ,  C10L5/26 ,  C10L5/28

CPC分类号： C10L5/26

摘要： A method for producing hot briquettes, for example, for use in blast furnaces, and using a briquetting material of non-caking components, such as low temperature coke from bituminous coal and/or lignite, coke dust and/or oil coke and caking fat coal at temperatures between 430.degree. C. and 540.degree. C., comprising, delivering the briquetting material to a briquetting press to form briquette blanks, tempering and degassing the blanks by delivering the blanks into individual chambers in a closed system of several chambers having gas communication with each other so that there is partly changing amounts of gas generated in the individual chambers and the briquette blanks are formed into tempered briquettes, and applying an overpressure to the chambers to conduct the gases away from the chamber with one and the same overpressure. The equipment for the execution of the method comprises a hardening system in the form of a single cube-shaped tank having one corner which is inclined downwardly and which is divided into several substantially parallel narrow chambers by walls which are disposed parallel to the inclined outer surface and which has a channel above an upper lateral edge for charging hot briquettes into the individual chambers and also for conducting away gases formed during tempering in a path diagonally opposite to the charging channel. An emptying channel is located under the lower lateral edge of the tank.

摘要翻译： 一种用于生产例如用于高炉的热压块的方法，以及使用非结块部件的压块材料，例如来自烟煤和/或褐煤的低温焦炭，焦炭粉和/或油焦和结块脂肪 煤，其温度在430℃至540℃之间，包括将压块材料输送到压块压块以形成团块坯料，通过在具有气体的几个室的封闭系统中将坯料输送到各个室中回火和脱气坯料 彼此连通，使得在各个室中产生的气体的部分变化量，并且将团块坯料形成为回火团块，并向腔室施加超压，以将气体以相同的超压力导出。 用于执行该方法的设备包括具有单个立方体形状的罐形式的硬化系统，其具有向下倾斜的一个角部，并且其被平行于倾斜的外表面设置的壁分隔成几个基本上平行的窄室 并且其具有在上侧边缘上方的通道，用于将热压块装入各个室中，并且还用于导出在与充电通道对角相对的路径中回火期间形成的气体。 一个排空通道位于罐的下侧边缘下方。

公开(公告)号：US4230594A

公开(公告)日：1980-10-28

申请号：US922311

申请日：1978-07-06

申请人： Heinrich Weber ,  Kurt Tippmer

发明人： Heinrich Weber ,  Kurt Tippmer

IPC分类号： C10K1/20 ,  C10K3/06 ,  C22B5/00

CPC分类号： C10K1/20 ,  Y02P20/129

摘要： A method of producing reducing gases from oxide ores, particularly iron ores, which contain mainly carbon monoxide and hydrogen and which are employed in the reduction process with a two to three fold excess with regard to the stoichiometric requirement of the ore to be reduced, comprising, mixing a hot moist fresh reducing gas and a preheated recycled gas, both of which are used in reducing iron ores and mainly contain carbon monoxide and hydrogen, directing the mixed gases in counterflow heat exchange with iron sponge in a desulfurizer to treat the sponge, thereafter, directing the treated sponge into an oxidizer and circulating preheated air thereover to lightly oxidize the iron sponge, and subsequently, directing the lightly oxidized iron sponge into a reducing shaft along with the mixed gases which are taken out of the desulfurizer.

摘要翻译： 一种从主要含有一氧化碳和氢气的氧化物矿石，特别是铁矿石中生产还原气体的方法，其用于还原过程中，相对于要还原的矿石的化学计量要求为二至三倍，包括 混合热湿新鲜还原气体和预热循环气体，两者均用于还原铁矿石，主要含有一氧化碳和氢气，引导混合气体与脱硫剂中的铁海绵逆流热交换以处理海绵， 之后，将经处理的海绵引导到氧化器中并循环预热的空气以轻轻氧化铁海绵，随后将轻度氧化的铁海绵与从脱硫器中取出的混合气体一起引导到还原轴中。

公开(公告)号：US4213790A

公开(公告)日：1980-07-22

申请号：US927366

申请日：1978-07-24

申请人： Klaus Bauer ,  Wolf Goldmann ,  Horst Kretzer ,  Heinrich Weber ,  Rudiger Beyer ,  Wilfried Kreft ,  Frank Schaberg ,  Rudolf Weber ,  Herbert Schmelter ,  Horst Ritzmann ,  Erich Schnieder ,  Georg Schepers

发明人： Klaus Bauer ,  Wolf Goldmann ,  Horst Kretzer ,  Heinrich Weber ,  Rudiger Beyer ,  Wilfried Kreft ,  Frank Schaberg ,  Rudolf Weber ,  Herbert Schmelter ,  Horst Ritzmann ,  Erich Schnieder ,  Georg Schepers

IPC分类号： C04B7/44 ,  B01J8/24 ,  C04B7/45 ,  F27B1/02 ,  F27B15/00 ,  F27B15/12 ,  F27B15/14

CPC分类号： B01J8/1809 ,  C04B7/45 ,  B01J2208/00061 ,  B01J2208/00504 ,  B60Y2200/143

摘要： A process for producing cement wherein preheated, partially calcined powder-form raw material is finally calcined in a fluidized bed and is discharged to a cooler through which a cooling stream of air passes. A part of the cooling air passes into the fluidized bed from below and another part of the cooling air, together with the partially calcined material, passes into the fluidized bed from the side. The rates of material flow to and from the fluidized bed is regulated to maintain a substantially uniform intersticial ratio between the upper and lower regions of the fluidized bed.

摘要翻译： 一种生产水泥的方法，其中预热的部分煅烧的粉末形式的原料最终在流化床中煅烧，并被排放到冷却剂通过的冷却器中。 一部分冷却空气从下方进入流化床，另一部分冷却空气与部分煅烧的材料一起从侧面进入流化床。 调节流入和流出床的物料流速，以保持流化床的上部和下部区域之间的基本均匀的间隙比。

公开(公告)号：US4142941A

公开(公告)日：1979-03-06

申请号：US832365

申请日：1977-09-12

申请人： Heinrich Weber ,  Horst Dungs ,  Klaus Urbye ,  Franz Beckmann ,  Hugo Schmauch ,  Karl H. Flasche

发明人： Heinrich Weber ,  Horst Dungs ,  Klaus Urbye ,  Franz Beckmann ,  Hugo Schmauch ,  Karl H. Flasche

IPC分类号： C10B53/08 ,  C10B57/04 ,  C10B45/02 ,  C10L5/16

CPC分类号： C10B57/04 ,  C10B53/08

摘要： A method of producing blast furnace coke from bituminous coals, particularly coals having poor coking capacities in which the coal to be carbonized is ground, predried or preheated, mixed with binders, compressed or formed into briquets having small mechanical resistances and charged into oven chambers, is characterized by fine coals or fine coal mixtures having a swelling index in mixture according to DIN 51741, smaller than 7, and preferably, below 6, and comprising more than 50% of poorly or non-baking coal having a content of volatile matter in excess of 30% or less than 20% which coals or coal mixtures are ground up to attain asurface per unit mass, according to DIN 66145, of from 400 cm.sup.2 to 1200 cm.sup.2 per gram, and with from 3% to 8% by weight of organic binders, compressing the mixture to form it into a briquet at a temperature range of from 70.degree. C. to 300.degree. C. and charging the compressed briquet into the oven chambers without substantial intermediate cooling in order to carbonize it.