公开(公告)号：US4554053A

公开(公告)日：1985-11-19

申请号：US553476

申请日：1983-11-18

Applicant: John Rizzon ,  Gunter Adomat ,  Peter Diemer

Inventor： John Rizzon ,  Gunter Adomat ,  Peter Diemer

IPC: C10B57/06 ,  C10B55/00

CPC classification number: C10B57/06

Abstract: In a method of removing heavy tar produced in a coke oven during the cooling of a coke-oven gas from the coke-oven gas, the heavy tar pieces are crushed in a pulverizer to obtain particles of the size of less than 1 mm. The heavy tar particles are then rarefied by the addition to them of a mixture of tar and water. The resulting mixture is maintained under the temperature of 55.degree.-75.degree. C. and then transported to a charge coal which is then charged into the coke-oven.

Abstract translation: 在从焦炉气体冷却焦炉煤气的同时，在焦炉中除去重焦油的方法中，将重焦油片在粉碎机中粉碎，得到尺寸小于1mm的颗粒。 然后，通过加入焦油和水的混合物，重质焦油颗粒被稀释。 将所得混合物保持在55-75℃的温度下，然后运送至装料煤，然后将其装入焦炉中。

公开(公告)号：US5771822A

公开(公告)日：1998-06-30

申请号：US561649

申请日：1995-11-22

Applicant: John Rizzon

Inventor： John Rizzon

IPC: B09B3/00 ,  C03B3/00 ,  C03B5/00 ,  C03B5/12 ,  F23G5/00 ,  F23G5/08 ,  F23J1/00 ,  F23J15/00

CPC classification number: F23J15/003 ,  B09B3/0066 ,  C03B3/00 ,  C03B5/005 ,  C03B5/12 ,  F23G5/006 ,  F23G5/085 ,  F23G2201/301 ,  F23G2201/302 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/602 ,  F23G2201/70 ,  F23G2201/80 ,  F23G2202/102 ,  F23G2202/103 ,  F23G2202/20 ,  F23G2203/212 ,  F23G2205/14 ,  F23G2205/18 ,  F23G2209/12 ,  F23G2209/28 ,  F23G2900/50002 ,  F23J2219/10 ,  F23J2219/80 ,  F23L2900/07005 ,  Y02E20/344 ,  Y02P40/55

Abstract: The present invention describes a process for the disposal of residual substances from waste incineration plants as well as activated coke and/or activated carbon. For this purpose the residual substance as well as activated coke and/or activated carbon is introduced into the annular shaft (3) of the primary chamber (2) of the furnace (1). In the primary chamber (2) a temperature of 1250.degree. C. to 1500.degree. C. is set. The molten material flowing off leaves the primary chamber (2) together with the flue gases through the central outlet (4). The molten material is passed through the secondary chamber (5) and is discharged as slag. The present invention furthermore describes an apparatus for such process, where in the furnace roof (10) of the primary chamber (2) of the furnace (1) one or several burners (7) are disposed and at one or several points (22) of the furnace roof (10) secondary air is introduced into the primary chamber (2) and at one or several points (23) of the furnace roof (10) tertiary air is introduced into the primary chamber (2).

Abstract translation: 本发明描述了用于处理来自废物焚化厂以及活性焦炭和/或活性炭的残余物质的方法。 为此，残留物质以及活性焦炭和/或活性炭被引入到炉（1）的主室（2）的环形轴（3）中。 在初级室（2）中，设定1250℃至1500℃的温度。 流出的熔融材料通过中心出口（4）与烟道气一起离开主室（2）。 熔融材料通过次级室（5）并作为渣排出。 本发明还描述了一种用于这种方法的装置，其中在炉（1）的主室（2）的炉顶（10）中设置一个或多个燃烧器（7）并且在一个或多个点（22）处， 炉顶（10）的二次空气被引入主室（2）中并且在炉顶（10）的一个或多个点（23）处，三次空气被引入主室（2）。

公开(公告)号：US4905614A

公开(公告)日：1990-03-06

申请号：US238522

申请日：1988-08-31

Applicant: Wolfgang Grigel ,  Jakob Hinterkeuser ,  Heinz-Dieter Waldhecker ,  John Rizzon ,  Kariheinz Passler

Inventor： Wolfgang Grigel ,  Jakob Hinterkeuser ,  Heinz-Dieter Waldhecker ,  John Rizzon ,  Kariheinz Passler

IPC: B09B3/00 ,  C02F11/06 ,  F23G5/04 ,  F23G5/32 ,  F23G5/46 ,  F23J15/02 ,  F23J15/06 ,  F23L15/04

CPC classification number: F23G5/46 ,  F23G5/04 ,  F23G5/32 ,  F23J15/025 ,  F23J15/06 ,  F23L15/04 ,  F23G2202/20 ,  F23G2206/10 ,  F23G2209/102 ,  F23G2209/12 ,  F23G2209/14 ,  F23G2209/30 ,  F23G2900/7011 ,  F23J2215/20 ,  F23J2215/30 ,  F23J2217/105 ,  F23J2219/60 ,  F23J2219/70 ,  Y02E20/348 ,  Y02W10/40

Abstract: Waste materials, potentially following their comminution and potentially following their dying or, respectively, preheating, are burned in a cyclone kiln (buring cyclone or, melting cyclone) at extremely high temperatures above 1500.degree. C. with formation of a molten slag low in noxious substances and a hot exhaust gas in which latter the valuable substances and/or noxious substances contained in the waste materials volatilize, whereby dusts enriched with valuable substances on the one hand and, on the other hand, dusts enriched with noxious substances are respectively separately separated out of the exhaust gas by partial condensation.

Abstract translation: 可能在粉碎后潜在的废物和潜在的死亡或分别预热的废料在高于1500℃的极高温度下在旋风窑（固化旋风分离器或熔融旋流器）中燃烧，形成熔点低的有害物质 物质和热废气，其中废物中包含的有价值物质和/或有害物质挥发，一方面富含有价值物质的粉尘和另一方面是富含有害物质的粉尘分别分开 通过部分冷凝排出废气。