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1. 发明授权

US4632766A Method of treatment of waste water obtained in a gasification plant during washing of raw gas 失效
标题翻译：处理原料气洗涤过程中气化厂废水的处理方法
公开(公告)号：US4632766A
公开(公告)日：1986-12-30
申请号：US620554
申请日：1984-06-14
申请人： Bernhard Firnhaber , Adolf Linke , Rolf Wetzel
发明人： Bernhard Firnhaber , Adolf Linke , Rolf Wetzel
IPC分类号： C02F1/74 , C02F1/72 , C02F1/78 , C02F9/00
CPC分类号： C02F9/00 , C02F1/72 , C02F1/78 , C02F2103/18
摘要： In a method of treating waste water obtained in a direct washing with water of raw gas in a plant for a gasification of gas, the waste water is first settled in a settling tank and a resultant concentrated slime-containing water is subjected to a multi-stage oxidation with air or oxygen only at the temperatures of between 20.degree. C., and 80.degree. C., and the slime-containing water obtained after the oxidation is conveyed to a filtration system or a slime-depositing container.
摘要翻译：在用于气体气化的设备中用原水气体直接洗涤获得的废水的处理方法中，首先将废水沉降在沉淀槽中，并将得到的含浓灰泥的水进行多级处理，空气或氧气仅在20℃至80℃的温度下进行阶段氧化，将氧化后获得的含粘稠水输送至过滤系统或粘泥沉积容器。

2. 发明授权

US5066476A Method of producing hydrogen-rich gas 失效
标题翻译：生产富氢气体的方法
公开(公告)号：US5066476A
公开(公告)日：1991-11-19
申请号：US550105
申请日：1990-07-06
申请人： Rolf Wetzel , Bernhard Firnhaber
发明人： Rolf Wetzel , Bernhard Firnhaber
IPC分类号： C01B3/50 , C10J3/46
CPC分类号： C10J3/466 , C01B3/50 , C10J3/86 , C10K1/004 , C10K1/005 , C10K1/02 , C10K1/08 , C10K3/04 , C01B2203/047 , C01B2203/0475 , C01B2203/0485 , C10J2300/1846 , C10J2300/1884 , Y02P20/129
摘要： A gas with a hydrogen content of at least 85 volume percent of partial oxidation crude gas is produced in a method including cooling of the gas after waste heat boiler of a gasifier by adding converted circulating gas in a quenching zone. The resulting gas mixture after corresponding gas treatment is subjected to a CO-conversion and then separated into a circulating gas partial stream and a product gas partial stream. The circulating gas partial stream is supplied back after a corresponding compression to the quenching zone, while the product gas partial stream after a so-called acid gas washing is subjected to a further gas treatment in correspondence with a desired use.
摘要翻译：在包括通过在淬火区域中加入转化的循环气体的气化器的废热锅炉之后的气体冷却的方法中，产生氢含量为至少85体积％的部分氧化粗气体的气体。对相应气体处理后的所得气体混合物进行CO转化，然后分离成循环气体部分气流和产物气体部分气流。在对淬火区进行相应的压缩之后，将循环气体部分流供给回来，同时对所谓的酸性气体洗涤后的产物气体部分流进行进一步的气体处理。

3. 发明授权

US4994093A Method of producing methanol synthesis gas 失效
标题翻译：生产甲醇合成气的方法
公开(公告)号：US4994093A
公开(公告)日：1991-02-19
申请号：US550133
申请日：1990-07-06
申请人： Rolf Wetzel , Bernhard Firnhaber
发明人： Rolf Wetzel , Bernhard Firnhaber
IPC分类号： C01B3/50 , C07C29/151 , C10J20060101 , C10J3/46
CPC分类号： C07C29/1518 , C01B3/50 , C10J3/46 , C10J3/86 , C10K1/002 , C10K1/003 , C10K1/004 , C10K1/005 , C10K1/02 , C10K1/04 , C10K1/101 , C10K3/04 , C01B2203/0465 , C01B2203/0475 , C01B2203/0485 , C10J2300/1223 , C10J2300/1621 , C10J2300/1665 , C10J2300/1846 , C10J2300/1884 , Y02P20/129
摘要： In accordance with a method of producing of methanol synthesis gas from a partial oxidation crude gas, the gas is cooled after a waste heat boiler of a gasifier by adding a converted circulating gas in a quenching zone. The resulting gas mixture is dedusted and then separated into a product gas partial stream and a circulating gas partial stream. The product gas partial stream is supplied after corresponding gas treatment to the synthesis reactor while the circulating gas partial stream is subjected to a CO-conversion and supplied back to the quenching zone.
摘要翻译：根据从部分氧化粗气体生产甲醇合成气的方法，通过在淬火区域中加入转化的循环气体，在气化器的废热锅炉之后冷却气体。将所得气体混合物除尘，然后分离成产物气体部分流和循环气体部分流。在对合成反应器进行相应的气体处理之后，将产物气体部分流供给到循环气体部分流进行CO转化并供给到淬火区域。

4. 发明授权

US4971777A Process for the removal of acid components and nitrogen oxides from the waste gases of industrial furnaces 失效
标题翻译：从工业炉废气中除去酸性成分和氮氧化物的方法
公开(公告)号：US4971777A
公开(公告)日：1990-11-20
申请号：US271094
申请日：1988-11-14
申请人： Bernhard Firnhaber , Karl Schmid , Cort Starck , Hans-Werner Gosch , Richard Wenderoth , Rolf Wetzel , Wolfgang Schulte
发明人： Bernhard Firnhaber , Karl Schmid , Cort Starck , Hans-Werner Gosch , Richard Wenderoth , Rolf Wetzel , Wolfgang Schulte
IPC分类号： B01D53/56 , B01D53/60 , B01D53/68 , B01D53/77
CPC分类号： B01D53/56 , B01D53/60 , B01D53/68
摘要： The process removes acid components including sulfur oxides and nitrogen oxides from the exhaust gases of industrial furnaces and includes oxidizing the nitrogen oxide contained in the exhaust gases with the oxygen contained in the exhaust gases at a exhaust gases temperature between 300.degree. and 900.degree. C. before entry of the gases into a first absorption stage, with an addition to the exhaust gases of an organic compound, preferably methanol, as a radical former. After oxidation of nitrogen oxides the exhaust gases undergo a two-stage absorption using aqueous ammonium salt solutions as absorption liquid, whose pH-value is continuously adjusted to less than 5 by addition of aqueous ammonia solution. The mol ratio of NO.sub.2 to SO.sub.2 in the exhaust gases introduced to the second absorption stage is maintained between 0.01 and 0.5 by diverting a portion of the exhaust gases prior to the first absorption stage to the second absorption stage. The salt solutions obtained thereby are neutralized together and evaporated, whereby the salts so produced, after pelletization or granulation represent a useful fertilizer.
摘要翻译：该方法从工业炉排气中除去含硫氧化物和氮氧化物的酸组分，包括在排气温度在300-900℃之间用废气中所含的氧氧化废气中所含的氮氧化物。在气体进入第一吸收阶段之前，加入有机化合物（优选甲醇）的废气作为基团前体。在氧化氮氧化物之后，废气通过使用含水铵盐溶液作为吸收液进行二阶段吸收，其pH值通过加入氨水溶液连续地调节到小于5。通过将第一吸收阶段之前的一部分排气转移到第二吸收阶段，引入第二吸收阶段的废气中的NO 2与SO 2的摩尔比保持在0.01至0.5之间。将由此得到的盐溶液中和在一起并蒸发，由此在造粒或造粒后生成的盐代表有用的肥料。

5. 发明授权

US5470361A Process for working up municipal plastic waste materials by gasification 失效
标题翻译：通过气化处理市政塑料废料的工艺
公开(公告)号：US5470361A
公开(公告)日：1995-11-28
申请号：US331364
申请日：1994-10-27
申请人： Adolf Linke , Werner Pohl , Karl Schmid , Rolf Wetzel
发明人： Adolf Linke , Werner Pohl , Karl Schmid , Rolf Wetzel
IPC分类号： C10J3/46 , C10J3/66 , C10J3/06 , C10K1/02 , C10K1/06
CPC分类号： C10J3/00 , C10J3/66 , C10J3/721 , C10K1/003 , C10K1/004 , C10K1/02 , C10K1/101 , C10K1/143 , C10J2300/0906 , C10J2300/0946 , C10J2300/0959 , C10J2300/169 , C10J2300/1884 , Y02E50/32
摘要： In the process for gasification of municipal waste plastic waste material pieces of about a 20 mm piece size are compressed and heated at a pressure of from 40 to 80 bar until at a temperature of from 230.degree. to 300.degree. C. to produce an HCl-containing gas and a plastic waste material containing less than 3000 mg of HCl per kg and the HCl-containing gas produced is washed with water to produce a hydrochloric acid solution. The plastic waste material is then heated further until at a temperature of from 400.degree. to 500.degree. C. to form a plastic melt having a viscosity of less than 300 cSt, advantageously less than 50 cSt. This plastic melt is gasified at a pressure of 4 bar with oxygen in a flame reaction to form a crude gas containing a preponderant proportion of CO in relation to CO.sub.2 in a gasification chamber having a central temperature of about 1600.degree. C. The crude gas is withdrawn from the gasification reactor at a temperature of 1300.degree. to 1600.degree. C., quenched with a water spray to cool it until at a temperature of 700.degree. to 900.degree. C. and then further cooled by indirect heat transfer in a heat exchanger producing steam until at a temperature of from 220.degree. to 300.degree. C. The cooled crude gas is dedusted until a dust content of less than 20 mg/Nm.sup.3 of crude gas is reached and the dedusted gas is washed and desulfurized to form the product gas.
摘要翻译：在城市废塑料废气的气化过程中，将大约20毫米片尺寸的废料在40至80巴的压力下压缩和加热至230℃至300℃的温度，以产生HCl- 含有气体和每千克含有少于3000毫克HCl的塑料废料，所生成的含HCl气体用水洗涤以产生盐酸溶液。然后将塑料废料进一步加热至400℃至500℃的温度，以形成粘度小于300cSt，有利地小于50cSt的塑料熔体。该塑料熔体在4巴的压力下与氧气在火焰反应中气化，形成一种粗气体，其在中心温度为约1600℃的气化室中含有相对于CO 2的CO优选比例。粗气体为在1300℃至1600℃的温度下从气化反应器中取出，用水喷雾骤冷至700℃至900℃的温度，然后通过间接传热在热交换器中进一步冷却，产生蒸汽直至温度为220〜300℃。将冷却的粗气除尘至达到小于20mg / Nm3的原油的粉尘含量，并将除尘气体洗涤并脱硫形成产物气体。

6. 发明授权

US4316741A Blast furnace process employing exchange fuel gas 失效
标题翻译：使用交换燃气的高炉工艺
公开(公告)号：US4316741A
公开(公告)日：1982-02-23
申请号：US141297
申请日：1980-04-18
申请人： Rolf Wetzel
发明人： Rolf Wetzel
IPC分类号： C21B5/00
CPC分类号： C21B5/001
摘要： A blast furnace process and plant are provided employing a gas mixture comprising coke oven gas and gasified fine grained to dusty fuels. The mixture is produced in a mixing chamber wherein the raw gas from the gasifier is chilled with purified cool coke oven gas. The gas mixture is separated from dust and desulfurized in a cyclone charged with burn lime dust. Then the gas mixture is fed to the blast furnace proper and enters at temperatures from about 750.degree. C. to 1000.degree. C.
摘要翻译：使用包括焦炉煤气和气化细粒度的灰尘燃料的气体混合物提供高炉方法和设备。混合物在混合室中产生，其中来自气化器的原料气体用纯化的冷焦炉气体冷却。气体混合物与粉尘分离，并在带有烧石灰粉尘的旋风分离器中脱硫。然后将气体混合物送入高炉，并在约750℃至1000℃的温度下进入。

7. 发明授权

US4936871A Method of cooling partial oxidation gas 失效
标题翻译：冷却部分氧化气体的方法
公开(公告)号：US4936871A
公开(公告)日：1990-06-26
申请号：US322073
申请日：1989-03-10
申请人： Gerhard Wilmer , Rolf Wetzel
发明人： Gerhard Wilmer , Rolf Wetzel
IPC分类号： C10J3/84 , C10K1/04
CPC分类号： C10K1/04 , C10J3/84 , C10K1/08 , C10J2300/1603
摘要： Decribed is a method of cooling partial oxidation gas exiting at a temperature between 1,000.degree. and 1,700.degree. C. from a conically converging outlet portion of a reactor vessel into a subsequent tubular cooling zone. To prevent deposition of sticky molten impurities entrained in the gas stream on the walls in the transition region between the reactor vessel and the cooling zone, the outlet portion of the reactor vessel is provided with a ring-shaped slot for injecting at an angle between 0.degree. to 90.degree. a frustoconical stream of cooling fluid. Another ring-shaped slot is provided in the cooling zone to inject at an angle between 70.degree. to 90.degree. another frustoconical stream of cooling fluid into the cooling zone.
摘要翻译：说明的是将部分氧化气体在1000℃至1700℃的温度下从反应器容器的锥形出口部分冷却到随后的管状冷却区域中的方法。为了防止夹带在气流中的粘性熔融杂质沉积在反应器容器和冷却区之间的过渡区域中的壁上，反应器容器的出口部分设置有环形槽，用于以0° DEG至90°的截头圆锥形冷却液流。在冷却区中设置另一个环形槽，以70度至90度之间的角度将另一个截头圆锥形的冷却流体流注入冷却区。

8. 发明授权

US4797198A Process for the working up of salvage oil 失效
标题翻译：补救油的处理过程
公开(公告)号：US4797198A
公开(公告)日：1989-01-10
申请号：US007358
申请日：1987-01-27
申请人： Rolf Wetzel , Hubert Coenen , Winfried Kreuch
发明人： Rolf Wetzel , Hubert Coenen , Winfried Kreuch
IPC分类号： C10G53/04 , C10G67/04 , C10M175/02 , C10G33/00
CPC分类号： C10M175/02
摘要： A process is disclosed for the working up of salvage oil, in which the salvage oil is subjected to an extraction under supercritical conditions. The halogen compounds contained in the produced extract are removed by catalytic hydrogenation. The extraction residue is eliminated by deposition or thermal treatment (gasification). In the case of a thermal treatment of the extraction residue, other residues can be simultaneously converted, so that the process is performed without yield of environmentally burdensome residues or by-products. Ethane in particular and/or propane is employed as solvent for the supercritical extraction.
摘要翻译：公开了一种处理救助油的方法，其中救助油在超临界条件下进行萃取。通过催化氢化除去生产的提取物中所含的卤素化合物。通过沉积或热处理（气化）消除萃取残留物。在提取残留物的热处理的情况下，可以同时转化其它残余物，使得该方法在没有产生环境负担的残余物或副产物的情况下进行。特别是使用乙烷和/或丙烷作为超临界萃取的溶剂。

9. 发明授权

US4045214A Method for producing steel 失效
标题翻译：生产钢的方法
公开(公告)号：US4045214A
公开(公告)日：1977-08-30
申请号：US540957
申请日：1975-01-14
申请人： Rolf Wetzel , Dietrich Radke
发明人： Rolf Wetzel , Dietrich Radke
IPC分类号： C21B13/14 , C21C1/08
CPC分类号： C21B13/143 , Y02P10/136 , Y02P10/265 , Y02P10/283
摘要： A method for producing steel from fine-grained iron ores includes the step of preheating and partially reducing the fine-grained iron ores in a countercurrent heat exchanger. The preheated and partially reduced fine-grained iron ores are then reduced in a fluidized bed reactor to form sponge iron. The reduction in the fluidized bed reactor is effected with exhaust gases which consist substantially of carbon monoxide and which emanate from a melting vessel in which sponge iron is melted. The fine-grained sponge iron produced in the fluidized bed reactor is separated from the reduction gases which form during the reduction in the fluidized bed reactor. The separated fine-grained sponge iron is pneumatically transported into a carbon containing melt in the melting vessel. The transported sponge iron is melted and subjected to a final reduction in the metal melt with the carbon in the metal melt and with further carbonaceous material which is pneumatically introduced into the metal melt. The melt is refined with pure oxygen. The oxygen, carbonaceous material and sponge iron are introduced into the metal melt through at least one nozzle which is disposed below the level of the metal melt surface.
摘要翻译：从细粒铁矿石生产钢的方法包括在逆流热交换器中预热和部分还原细粒铁矿石的步骤。然后将预热和部分还原的细粒铁矿石在流化床反应器中还原以形成海绵铁。流化床反应器的还原是由主要由一氧化碳组成并从海绵铁熔化的熔化容器中排出的废气来实现的。在流化床反应器中生产的细粒海绵铁与在流化床反应器还原期间形成的还原气体分离。分离的细粒海绵铁在熔融容器中气动输送到含碳的熔体中。将输送的海绵铁熔化，并使金属熔体与金属熔体中的碳和进一步的气态导入金属熔体中的碳质材料最终还原。熔体用纯氧精炼。氧气，含碳材料和海绵铁通过设置在金属熔体表面的下方的至少一个喷嘴引入到金属熔体中。

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