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    • 3. 发明授权
    • Process for the combustion of waste material with production of thermal
energy
    • 用于生产热能的废料燃烧过程
    • US5797336A
    • 1998-08-25
    • US702550
    • 1996-10-24
    • Patrick MullerHans Ruegg
    • Patrick MullerHans Ruegg
    • B09B3/00F23G5/00F23G5/16F23G5/30F27D17/00F23J11/00
    • F23G5/006F23G5/16F23G5/30F23C2206/103F23G2201/30F23G2201/303F23G2202/103F23G2203/501
    • Waste is burnt in a furnace chamber (1). The oxygen-containing flue gases resulting in this process are introduced into a fluidized bed in an afterburning chamber (5) and reburnt. Solids discharged with the flue gases from the afterburning chamber (5) are separated from the flue gases in a dust separator (9) and recycled to the afterburning chamber (5), so that a circulating fluidized bed is formed, which produces a very homogeneous temperature distribution in the afterburning chamber (5) and at the same time permits highly efficient cooling of the flue gases. A secondary oxygen feed for the afterburning is dispensed with, which enables a decrease in size both of the afterburning chamber (5) and also of the downstream heat-recovery and gas cleaning devices and improvement in efficiency resulting therefrom.
    • PCT No.PCT / CH96 / 00006 Sec。 371日期1996年10月24日第 102(e)1996年10月24日PCT 1996年1月8日PCT PCT。 出版物WO96 / 21825 日期1996年7月18日在炉室(1)中燃烧废物。 导致该方法的含氧烟道气被引入到后燃烧室(5)中的流化床中并重新反应。 与来自再燃烧室(5)的烟气排出的固体与灰尘分离器(9)中的烟道气分离并再循环至后燃烧室(5),从而形成循环流化床,产生非常均匀的 在再燃烧室(5)中的温度分布并且同时允许烟道气体的高效冷却。 省略了用于后燃烧的二次氧气进料,这使得后燃烧室(5)以及下游热回收和气体净化装置的尺寸都能够减小,从而提高了由此产生的效率。
    • 5. 发明授权
    • Process for the thermal treatment of waste material
    • 废料热处理工艺
    • US5915311A
    • 1999-06-29
    • US702551
    • 1996-10-24
    • Patrick MullerHans Ruegg
    • Patrick MullerHans Ruegg
    • B09B3/00C10B27/00F23G5/027F23G5/16F23G5/30F27D17/00F23J11/00
    • F23G5/30F23G5/027
    • The waste material is degasified under the action of heat in a pyrolysis chamber (2). The volatile degasifying products are subjected to afterburning with supply of oxygen in an afterburning chamber (4a or 4b or 4c) designed as a fluidized-bed reactor. The solids discharged from the afterburning chamber (4a or 4b or 4c) are separated off from the flue gas stream in a dust separator (8) and, preferably cooled in an external fluid-bed cooler, are recycled to the afterburning chamber (4a or 4b or 4c). The temperatures of above 2500.degree. C., which are produced in the afterburning of the carbonization gases having a high heating value (minimum 8000 kJ/m.sup.3 (S.T.P.), can be controlled.
    • PCT No.PCT / CH96 / 00007 Sec。 371日期1996年10月24日第 102(e)1996年10月24日PCT 1996年1月8日PCT PCT。 出版物WO96 / 21824 日期1996年7月18日在热解室(2)中,废料在热作用下脱气。 在设计为流化床反应器的辅助燃烧室(4a或4b或4c)中,挥发性脱气产物经过二氧化碳供给。 从再燃烧室(4a或4b或4c)排出的固体在灰尘分离器(8)中从烟道气流中分离出来,优选在外部流体床冷却器中冷却,再循环到后燃烧室(4a或 4b或4c)。 可以控制在具有高热值(最小8000kJ / m3(S.T.P.))的碳化气体的再燃烧中产生的高于2500℃的温度。
    • 6. 发明授权
    • Process for cooling and cleaning flue gases
    • 冷却和清洁烟道气的过程
    • US5878677A
    • 1999-03-09
    • US702552
    • 1996-10-24
    • Patrick MullerHans Ruegg
    • Patrick MullerHans Ruegg
    • F23J15/00B01D53/50B01D53/68B01J8/26F23J11/00
    • B01D53/12B01D53/508B01D53/685B01J8/26
    • To cool and clean flue gases from a furnace of a waste incineration plant, the flue gases are fed to a fluidized-bed reactor (6) as fluidizing gases in a first stage (1), into which solid sorbents are simultaneously introduced to remove gaseous pollutants. Solids discharged from the fluidized-bed reactor (6), together with the unused sorbents, are preferably recirculated via a fluid-bed cooler (15). Whereas in the first stage (1), at temperatures above 600.degree. C., optimum conditions, in particular for removing SO.sub.2, are created, the flue gases are further cooled and treated in a second stage (2a, 2b, 2c). In a second circulating fluidized bed, at temperatures below 600.degree. C., excellent conditions are created for HCl removal. In addition to the optimum gas cleaning, efficient cooling is also achieved, corrosion problems on heat-transfer surfaces also being solved.
    • PCT No.PCT / CH96 / 00008 Sec。 371日期1996年10月24日第 102(e)1996年10月24日PCT 1996年1月8日PCT PCT。 WO96 / 21504 PCT出版物 日期1996年7月18日为了从废物焚烧厂的炉子中冷却和清洁烟道气,烟道气被送入流化床反应器(6),作为第一阶段(1)中的流化气体,固体吸附剂 同时引入去除气态污染物。 从流化床反应器(6)排出的固体与未使用的吸附剂一起优选通过流化床冷却器(15)再循环。 而在第一阶段(1)中,在高于600℃的温度下,产生了最佳条件,特别是用于除去SO 2的烟道气体,在第二级(2a,2b,2c)中被进一步冷却和处理。 在第二循环流化床中,在低于600℃的温度下,产生了HCl去除的良好条件。 除了最佳的气体清洗之外,还实现了有效的冷却,也解决了传热表面的腐蚀问题。
    • 7. 发明授权
    • Process and apparatus for the thermal production of energy from waste
material, particulary refuse
    • 用于废物热能生产的工艺和设备,特别是垃圾
    • US5749309A
    • 1998-05-12
    • US439126
    • 1995-05-11
    • Stefan ForsbergHans Ruegg
    • Stefan ForsbergHans Ruegg
    • F23G5/00B09B3/00C10B7/04C10B53/00C10J3/00F23G5/027
    • F23G5/0276C10B53/00C10B7/04F23G2205/10F23G2205/16F23L2900/07005Y02E20/344Y02E50/30Y02P20/129
    • Waste material is conveyed in an uncomminuted state on a grate (5) through a combustion chamber (12) of a stationary furnace (10) and at the same time mixed by a thrust and shearing action of the grate (5). A gaseous oxidizing agent is introduced, for example via gas lances, into the combustion chamber (12) from above the layer of waste material (11) lying on the grate (5). The oxidizing agent cooperates with the combustible volatile substances escaping from the waste to form flames. The layer of waste is heated by the thermal radiation of the flames such that degasification occurs. The combustible gases thus freed are partially burnt. The waste material freed from the volatile substances, that is to say refuse coke, and the unburnt volatile substances, that is to say combustible gases, can be used as fuels outside the plant or within the plant. The oxidizing agent does not come into contact with the thermally stressed parts of the plant. It is thus possible to use oxidizing agents having a high oxygen content of up to 100%. This results in an enormous reduction of flue gases by up to 80%.
    • 废料通过固定炉(10)的燃烧室(12)在炉排(5)上以非破坏状态输送,同时通过炉排(5)的推力和剪切作用混合。 气态氧化剂例如通过气体喷枪从位于炉排(5)上的废料层(11)的上方引入燃烧室(12)。 氧化剂与从废物中逸出的可燃性挥发性物质配合形成火焰。 废物层被火焰的热辐射加热,从而发生脱气。 因此释放的可燃气体部分燃烧。 从挥发性物质(即垃圾焦炭)中排出的废物和未燃烧的挥发性物质,即可燃性气体,可用作植物外或植物内的燃料。 氧化剂不会与植物的热应力部分接触。 因此,可以使用氧含量高达100%的氧化剂。 这样可以大大减少烟气达80%。
    • 8. 发明授权
    • Process and installation for the recovery of ammonia during the
separation of nitrogen oxide from waste gases
    • 在废气中分离出氮氧化物时氨氮的回收过程和安装
    • US5069886A
    • 1991-12-03
    • US590436
    • 1990-09-26
    • Ruedi FreyHans Ruegg
    • Ruedi FreyHans Ruegg
    • B01D53/58B01D53/94C01C1/02C01C1/12C02F1/20
    • B01D53/58C01C1/12
    • Process and apparatus wherein nitrogen oxides NO.sub.x contained in waste gases produced by combustion of fossil fuels in a firing plant are removed by reacting the waste gases with ammonia NH.sub.3 to reduce the nitrogen oxides to elementary nitrogen N.sub.2 ; subjecting the waste gases after being so reacted to wet waste gas cleaning whereby the washing water removes the unreacted ammonia (slip) from the waste gas to produce slip enriched washing water; raising the pH value of the slip enriched washing water to a value of more than 10, introducing air into the pH raised slip enriched washing water to remove the slip from the water and produce an air-slip mixture and recycling the slip into the furnace to react with waste gases to lower the amount of ammonia discharged into the atmosphere.
    • 通过使废气与氨NH 3反应除去氮氧化物至基本氮N2,从而除去燃烧装置中的化石燃料燃烧产生的废气中含有的氮氧化物的NOx的方法和装置; 使废气在反应后进行废气净化,由此洗涤水从废气中除去未反应的氨(滑动),以产生富含滑爽的洗涤水; 将增稠的洗涤水的pH值提高到10以上,将空气引入富含pH的升高的富集洗涤水中以从水中除去滑移物,并产生空气混合物并将其回收到炉中 与废气反应以降低排入大气的氨的量。
    • 9. 发明申请
    • METHOD AND DEVICE FOR PRODUCING EXPLOSIONS
    • 用于生产爆炸物的方法和装置
    • US20110180020A1
    • 2011-07-28
    • US13061978
    • 2009-09-01
    • Hans Ruegg
    • Hans Ruegg
    • F22B37/48
    • G10K15/043F28G7/00F28G7/005G01V1/116
    • An apparatus and a method for producing explosions, including a pressure-resistance container having a main explosion chamber introduced therein, further including a supply line for supplying a flowable explosible material, and a drain opening for the directed drainage of gas pressure caused by the ignition of the explosible material. The drain opening is closed directly by a closure means, preferably a plunger, which is pressed against the drain opening using a gas spring and held closed substantially up to the time of ignition. Before the actual main explosion, the closure means is moved by the igniting and the pressure force of an auxiliary explosion, thereby exposing the drain opening.
    • 一种用于产生爆炸的装置和方法,包括其中引入有主爆炸室的耐压容器,还包括用于供应可流动的可爆炸材料的供应管线和用于由点火引起的气体压力的定向排水的排水开口 的爆炸物质。 排放口直接由封闭装置(最好是柱塞)封闭,该装置使用气弹簧压靠排水开口,并基本上直到点火时保持关闭。 在实际的主要爆炸之前,封闭装置通过点火和辅助爆炸的压力而移动,从而暴露出排放口。
    • 10. 发明授权
    • Method for incinerating refuse and for treating the resulting slag
    • 焚烧垃圾和处理所得炉渣的方法
    • US6095064A
    • 2000-08-01
    • US168994
    • 1998-10-09
    • John MillardHans Ruegg
    • John MillardHans Ruegg
    • F23G5/16F23G5/20F23J1/00F23J3/00
    • F23G5/20F23G5/16F23J1/00F23G2202/106F23G2900/50209
    • A method for the incineration of refuse in an incineration cylindrical rotary kiln and for treating the resulting slag from the incineration of the refuse. The method includes the steps of removing the slag or ash from the cylindrical rotary kiln in a dry state and immediately separating the slag or ash in a first screening stage into at least two fractions, including a first fraction or screen underflow having a particle size of less than 32 mm. The method includes the further steps of feeding the first fraction or screen underflow to a second classifying stage where the first fraction or screen underflow is separated into a fine function having a particle size of up to 2 mm and the further step of returning at least part of the fine fraction to an air-inlet side of the cylindrical rotary kiln for incineration of the fine fraction.
    • 一种用于在焚烧圆柱形回转窑中焚烧垃圾的方法,并用于处理来自垃圾焚烧的所得炉渣。 该方法包括以下步骤:将来自圆柱形回转窑的渣或灰分从干燥状态除去,并立即将第一筛选阶段中的渣或灰分离成至少两个馏分,包括第一馏分或下游筛, 小于32毫米。 该方法还包括进一步的步骤,将第一部分或筛网下溢给第二分级阶段,在第二分级阶段,将第一分级或筛子下溢分离成具有至多2mm的粒度的精细功能,以及再次返回至少部分 的细小部分加入到圆筒状回转窑的空气入口侧,用于焚烧精细馏分。