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公开(公告)号：US5495812A
公开(公告)日：1996-03-05
申请号：US140181
申请日：1993-11-04
Applicant: Walter Schulze
Inventor： Walter Schulze
CPC classification number: F23G5/448 , F23G5/00 , F23G7/003 , F42B33/067 , F23G2201/101 , F23G2202/10 , F23G2202/105 , F23G2209/16 , F23G2900/54001
Abstract: An installation is provided for the deflagration of explosives. The installation includes a splinter and explosive-proof tunnel housing having open ends and receiving a deflagration reactor positioned inside the tunnel housing and having an entry passageway and entry zone, a deflagration zone and an exit zone and exit passageway. A conveyor device extends from outside the reactor and into and through and out of the reactor and includes a plurality of carriers movable along the conveyor device for receiving and transporting explosives into and through the entry zone and into the reactor zone for ignition and burning of the explosives in the reactor zone. Each of the carriers includes a device for closing in substantially air-tight manner the entry passage and the exit passage as the carrier moves through the reactor. Devices cooperate with the device for closing the entry passageway and the exit passageway for allowing a controllable residual airflow through the reactor.
Abstract translation: PCT No.PCT / EP92 / 00973。 371日期：1993年11月4日 102（e）日期1993年11月4日PCT提交1992年5月5日PCT公布。 出版物WO92 / 20969 日期：1992年11月26日。爆炸物爆燃安装。 该安装包括具有开口端的分裂和防爆隧道壳体，并且接收位于隧道壳体内部的具有进入通道和进入区，爆燃区以及出口区和出口通道的爆燃反应堆。 输送装置从反应器外部延伸并通过和流出反应器，并且包括可沿输送装置移动的多个载体，用于接收和运输爆炸物进入入口区域并进入反应器区域以点燃和燃烧 炸药在反应堆区。 每个载体包括当载体移动通过反应器时基本上气密地封闭入口通道和出口通道的装置。 装置与装置配合以关闭入口通道和出口通道，以允许可控制的剩余气流通过反应器。
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公开(公告)号：US5246599A
公开(公告)日：1993-09-21
申请号：US734197
申请日：1991-07-22
Applicant: Max Aicher
Inventor： Max Aicher
IPC: C02F11/12 , C02F11/10 , C02F11/18 , C02F103/00 , C10B53/00 , F23G5/027 , F26B17/20 , F26B23/02 , B01D35/18
CPC classification number: C10B53/00 , C02F11/10 , F23G5/027 , F26B17/205 , F26B23/028 , F23G2201/101 , F23G2201/303 , F23G2201/304 , F23G2204/103 , F23G2206/10 , F23G2209/12 , F23G2900/52001 , F23L2900/07005 , Y02E20/344 , Y02W10/40
Abstract: In a treatment or processing or sewage sludge in the sense of recycling, where the sewage sludge is to begin with dried (T), subsequently converted (K) under anaerobic conditions at approximately 250.degree. to 350.degree. C. and finally is sintered at at least 1250.degree. C. in successive steps, it is proposed to perform all process steps including the conveyance of the commodity to be processed between the individual processing steps successively in continuous passage in a closed system. Only the vapors are removed in this system in the drying stage (T) and the conversion gases in the conversion stage (K) and they are condensed; the heat quantity contained in the flue gas generated during the sintering process (S) is utilized for heating to begin with the conversion stage (K) and after that the drying stage (T). Because the flue gases are used for heating the processing steps in the sequence of the naturally occurring temperature gradient, the processing of the sewage sludge is achieved so as to be nearly self-sufficient as far as the energy requirement is concerned, meaning the energy required for the processing is largely supplied by the calorific value of the organic ingredients contained in the sewage sludge itself. Because the sewage sludge is processed in a closed system, nefarious effects upon the environment are avoided.
Abstract translation: 在循环利用的污水处理或污水处理中，污水从干燥（T）开始，随后在250〜350℃的厌氧条件下转化（K），最后在 至少1250℃，建议执行所有的处理步骤，包括在闭合系统中连续通过的各个处理步骤之间输送待处理的商品。 在该系统中，在干燥阶段（T）和转化阶段（K）中的转化气体中仅蒸发蒸气，并将其冷凝; 在烧结过程（S）中产生的烟气中所含的热量用于加热，从转化阶段（K）开始，之后是干燥阶段（T）。 由于烟道气按照天然存在的温度梯度的顺序加热处理步骤，所以能够满足污水污泥的处理要达到能源需求几乎自给自足，意味着所需的能量 因为处理主要是由污水污泥本身含有的有机成分的热值提供的。 由于污水污泥在封闭系统中进行处理，因此避免了对环境的恶劣影响。
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公开(公告)号：US20080053347A1
公开(公告)日：2008-03-06
申请号：US11862355
申请日：2007-09-27
Applicant: William Walker , Karen Bertram
Inventor： William Walker , Karen Bertram
CPC classification number: F23G5/0276 , F23G5/04 , F23G5/12 , F23G5/16 , F23G5/444 , F23G5/446 , F23G5/46 , F23G2201/101 , F23G2201/80 , F23G2203/8013 , F23G2205/14 , F23G2206/203 , Y02E20/12
Abstract: A pyrolyzer has a heated inner housing that includes first and second conveyors. Preferred conveyors have independent or at least potentially independent flows of material to be pyrolyzed. All suitable conveyors are contemplated, including especially screw conveyors, or combination of screw and paddle conveyors. Both first and second conveyors can be disposed within a common lumen, with a partial divider between them. An alternative divider is also contemplated that more or less divides the inner housing into two lumens. Thus, the lumens can be entirely distinct, or can have cross-flow of gases and/or material being pyrolyzed. Heat transfer fins can be advantageously attached, extend from, or be otherwise coupled to the inner housing to assist in transfer of heat into the lumen(s) of the inner housing.
Abstract translation: 热解器具有加热的内壳，其包括第一和第二输送机。 优选的输送机具有待热解的材料的独立或至少潜在独立的流动。 可以考虑所有合适的输送机，包括特别是螺旋输送机，或螺旋桨和桨式输送机的组合。 第一和第二输送机都可以设置在共同的管腔内，在它们之间具有部分分隔。 也可以设想一种可选择的分隔器，或多或少地将内壳分成两个流明。 因此，流明可以是完全不同的，或者可以具有被热解的气体和/或材料的交叉流。 传热翅片可以有利地附接，延伸或耦合到内壳体，以帮助将热量传递到内壳体的内腔中。
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公开(公告)号：US20060124040A1
公开(公告)日：2006-06-15
申请号：US10517023
申请日：2002-06-26
Applicant: William Walker
Inventor： William Walker
CPC classification number: F23G5/0276 , F23G5/04 , F23G5/12 , F23G5/16 , F23G5/444 , F23G5/446 , F23G5/46 , F23G2201/101 , F23G2201/80 , F23G2203/8013 , F23G2205/14 , F23G2206/203 , Y02E20/12
Abstract: An apparatus for treating waste material that comprises four major cooperating subsystems, namely a pyrolytic converter (24), a two-stage thermal oxidizer (26), a steam generator (28) and a steam turbine (30) driven by steam generated by the steam generator. In operation, the pyrolytic converter is uniquely heated without any flame impinging on the reactor component and the waste material to be pyrolyzed is transported through the reaction chamber of the pyrolytic converter by a pair of longitudinally extending, side-by-side material transporting mechanisms (42, 43).
Abstract translation: 一种用于处理废物的设备，包括四个主要协作子系统，即热解转换器（24），二级热氧化器（26），蒸汽发生器（28）和由蒸汽发生器（28）驱动的蒸汽驱动的蒸汽， 蒸汽发生器。 在操作中，热解转炉被独特加热而没有任何火焰撞击在反应器部件上，待热解的废料通过一对纵向延伸的并排材料输送机构（例如， 42，43）。
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公开(公告)号：US06746497B1
公开(公告)日：2004-06-08
申请号：US09784448
申请日：2001-02-27
Applicant: Masamoto Kaneko
Inventor： Masamoto Kaneko
IPC: C10J300
CPC classification number: F23G5/0276 , F23G5/165 , F23G5/50 , F23G2201/101 , F23G2201/303 , F23G2202/101 , F23G2207/101 , F23G2207/30 , F23G2209/281
Abstract: A waste is dry-distilled in a gasification furnace and generated combustible gas is combusted in a combustion furnace. A temperature in the combustion furnace is set to be substantially constant at a first preset temperature or more. When the temperature in the combustion furnace is greater than the first preset temperature by combustion of other fuels, the combustible gas is introduced. When the temperature in the combustion furnace reaches a second preset temperature or more by the combustion of only the combustible gas, the combustion of the other fuels is finished. When the temperature in the combustion furnace falls below a third preset temperature the combustion of the other fuels is resumed. When the temperature in the gasification furnace falls below a fourth preset temperature, the combustion of the other fuels is finished.
Abstract translation: 在气化炉中将废物进行干馏，并在燃烧炉中产生可燃气体。 在第一预设温度或更高温度下将燃烧炉中的温度设定为基本恒定。 当燃烧炉中的温度通过其他燃料的燃烧而大于第一预设温度时，引入可燃气体。 当燃烧炉中的温度仅通过可燃气体的燃烧而达到第二预定温度以上时，其他燃料的燃烧结束。 当燃烧炉中的温度低于第三预设温度时，其它燃料的燃烧恢复。 当气化炉中的温度低于第四预设温度时，其他燃料的燃烧结束。
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Patent Agency Ranking
公开(公告)号：US20040060487A1
公开(公告)日：2004-04-01
申请号：US10670287
申请日：2003-09-26
Inventor： Toshio Maesato
IPC: F23G005/04
CPC classification number: C10B47/46 , C10B53/00 , F23G5/04 , F23G5/16 , F23G5/20 , F23G2201/101 , F23G2203/208 , F23J15/06 , Y02E50/14 , Y02E50/30
Abstract: A furnace has a dual structure for carbonizing material. The furnace has a group of inner chambers and an outer chamber. Each of the inner chambers has a lid which can open and close to input the material for carbonizing. The outer chamber moves so that the group of inner chambers is housed in the outer chamber. Due to this, a combustion space is formed between the group of inner chambers and the outer chamber so as to heat each of the inner chambers to dry the material by distillation.
Abstract translation: 炉具有用于碳化材料的双重结构。 炉具有一组内室和外室。 每个内室具有可以打开和关闭以输入用于碳化的材料的盖。 外室移动，使得一组内室容纳在外室中。 由此，在内室组和外室之间形成燃烧空间，以便加热每个内室以通过蒸馏干燥材料。
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47.发明授权
公开(公告)号：US3639111A
公开(公告)日：1972-02-01
申请号：US3639111D
申请日：1969-01-30
Applicant: UNIV CALIFORNIA
Inventor： BRINK DAVID L , THOMAS JEROME F
CPC classification number: F23G5/027 , B01D53/523 , C10B53/00 , C10J3/00 , C10J3/26 , C10J3/721 , C10J3/723 , C10J3/74 , C10J3/84 , C10J2300/092 , C10J2300/093 , C10J2300/0946 , C10J2300/0956 , C10J2300/0959 , C10J2300/0996 , C10J2300/1253 , C10J2300/1869 , C10J2300/1884 , C10J2300/1892 , F23G7/04 , F23G2201/101 , F23G2201/301 , F23G2201/303 , F23G2206/203 , Y02E20/12
Abstract: Organic material, such as kraft black liquor, organic fuels, garbage and organic wastes, is destructively distilled and pyrolyzed at an elevated temperature and for a time sufficient to break down the material to noncombustible solids and to a stable gaseous clean burning fuel. The temperature is maintained to preclude recombination of intermediate products formed during the pyrolysis and which would otherwise pollute the atmosphere. A controlled amount of oxygen is continuously introduced during the cracking to provide energy by exothermic oxidative reactions but the oxygen is insufficient to effect stoichiometric or in other words complete combustion.
Abstract translation: 诸如牛皮纸黑液，有机燃料，垃圾和有机废物的有机材料在高温下被破坏性地蒸馏和热解，并且足以将材料分解成不可燃固体和稳定的气体清洁燃烧燃料的时间。 保持温度以排除在热解期间形成的中间产物的重组，否则会污染大气。 在裂化期间连续引入受控量的氧以通过放热氧化反应提供能量，但氧不足以实现化学计量或换句话说完全燃烧。
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公开(公告)号：US20160245508A1
公开(公告)日：2016-08-25
申请号：US15025835
申请日：2014-10-02
Applicant: ENI S.P.A.
Inventor： Felicia MASSETTI , Maria Ilaria PISTELLI , Medardo PINTI
CPC classification number: F23G7/001 , C02F11/06 , C02F11/10 , C10J3/005 , C10J3/60 , C10J2200/158 , C10J2300/1246 , F23G5/006 , F23G5/027 , F23G5/0273 , F23G5/04 , F23G5/20 , F23G5/46 , F23G2201/101 , F23G2201/302 , F23G2201/303 , F23G2201/40 , F23G2203/211 , F23G2206/10 , F23G2209/12 , F23G2900/50001 , F23G2900/50201 , F23G2900/50204 , F23G2900/52001 , F23G2900/52002 , F23G2900/54402 , Y02W10/40
Abstract: The present invention relates to reaction equipment for the treatment of organic and/or inorganic waste of refineries or petrochemical plants comprising: •—a drying and pyrolysis device (4) which rotates around its longitudinal, tilted rotation axis (A), •—a gasification device (6) which rotates around its longitudinal, horizontal rotation axis (B), •—a combustion device (14) comprising a burner (13) having a longitudinal horizontal axis (C), •—at least one settling chamber (15) for the collection of intermediate solid residues and the accumulation of intermediate gaseous reaction products, •—at least one outlet duct of the gaseous end-products (16), at least one outlet duct of the solid end-products (7), and at least one inlet duct of the feedstock (2) •—said combustion device (14), drying and pyrolysis device (4), gasification device (6) are physically separated and positioned on three different levels, •—the longitudinal rotation axis (A) of the drying and pyrolysis device (4) is tilted with respect to both the longitudinal rotation axis (B) of the gasification device (6) and also with respect to the longitudinal axis (C) of the combustion device (14), •—the longitudinal rotation axis (B) of the gasification device (6) is parallel to the longitudinal axis (C) of the combustion device (14), •—the combustion device (14) is in fluid communication with the drying and pyrolysis device (4), •—the drying and pyrolysis device (4) comprises, in its interior, a first indirect heat exchange device (3) in which the combustion fumes coming from the combustion device (14) flow, •—at least one settling chamber (15) in fluid communication with said drying and pyrolysis device (4) and with said gasification device (6) and with said combustion device (14), •—conveying means (5) are positioned in the settling chamber (15) and put the drying and pyrolysis device (4) in fluid communication with the gasification device, •—it comprises a second heat exchange device (12) in fluid communication with the first indirect heat exchange device (3) and the combustion device (14), •—it comprises means for the suction of the intermediate gaseous reaction products, said means being positioned in the settling chamber (15).
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公开(公告)号：US09366477B2
公开(公告)日：2016-06-14
申请号：US14363524
申请日：2012-12-10
Applicant: TSP GMBH
Inventor： Markus Bux , Steffen Ritterbusch , Tilo Conrad
CPC classification number: F26B3/28 , C02F11/16 , F23G5/04 , F23G7/001 , F23G2201/101 , F23G2206/203 , F26B3/286 , F26B9/10 , F26B9/103 , F26B23/00 , F26B23/001 , F26B23/002 , F26B2200/18 , Y02B40/74 , Y02E20/12 , Y02P70/405 , Y02W10/37
Abstract: The invention relates to a process for drying sludge having the following steps: a) applying a sludge having a dry matter content of 15% to 30% to a floor of a drying hall (10), or sludge already present, b) predrying the sludge in the drying hall (10), wherein the sludge is mixed, c) introducing at least a part of the predried sludge into a heated thermal dryer (12), wherein the sludge introduced in each case into the thermal dryer (12) is replaced in the drying hall (10), by carrying out the step a), by a sludge having a dry matter content of 15% to 30% which then likewise passes through step b), d) drying the sludge in the thermal dryer (12) to a dry matter content of 80% to 95%, wherein air (14) taking up moisture from the sludge flows over or through the sludge, wherein the air (14) is brought to a temperature in a range from 70° C. to 160° C., or wherein, by heating the sludge, water vapor is liberated from the sludge, wherein the sludge, after achieving the dry matter content of 80% to 95%, is discharged from the thermal dryer (12), wherein the sludge discharged from the thermal dryer in each case is replaced by predried sludge by carrying out step c), which predried sludge then likewise passes through step d), e) passing the air (14) heated in step d), or the water vapor through a first region of a heat exchanger (17), through which ambient air (16) passes in a second region, wherein the air (14) heated in step d) or the water vapor releases heat to the ambient air (16), with condensation of the moisture present in the heated air or in the water vapor, wherein the heated air (14) or the water vapor is cooled to a temperature in the range from 10° C. to 60° C., and the ambient air (16) is heated to a temperature at most 40 K above the ambient temperature and the former temperature is at most 50° C., and f) promoting the predrying according to step b) by introducing the ambient air (18) heated in step e) into the drying hall (10), in such a manner that the ambient air (16) flows onto or over the surface of the sludge applied to the floor of the drying hall (10).
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公开(公告)号：US07621225B2
公开(公告)日：2009-11-24
申请号：US10517023
申请日：2002-06-26
Applicant: William C. Walker , Karen Bertram, legal representative
Inventor： William C. Walker
IPC: F23G5/12
CPC classification number: F23G5/0276 , F23G5/04 , F23G5/12 , F23G5/16 , F23G5/444 , F23G5/446 , F23G5/46 , F23G2201/101 , F23G2201/80 , F23G2203/8013 , F23G2205/14 , F23G2206/203 , Y02E20/12
Abstract: An apparatus for treating waste material that comprises four major cooperating subsystems, namely a pyrolytic converter (24), a two-stage thermal oxidizer (26), a steam generator (28) and a steam turbine (30) driven by steam generated by the steam generator. In operation, the pyrolytic converter is uniquely heated without any flame impinging on the reactor component and the waste material to be pyrolyzed is transported through the reaction chamber of the pyrolytic converter by a pair of longitudinally extending, side-by-side material transporting mechanisms (42, 43).
Abstract translation: 一种用于处理废物的设备，包括四个主要协作子系统，即热解转换器（24），二级热氧化器（26），蒸汽发生器（28）和由蒸汽发生器（28）驱动的蒸汽驱动的蒸汽， 蒸汽发生器。 在操作中，热解转炉被独特加热而没有任何火焰撞击在反应器部件上，待热解的废料通过一对纵向延伸的并排材料输送机构（例如， 42，43）。
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