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Brief description of the waste materials, industrial and / or household and installation for the treatment of industrial waste materials, and / or household

机译:工业和/或家庭废物的简要说明以及用于处理工业和/或家庭废物的设备

摘要

The waste is loaded into a number of containers with holes and the waste in the containers (20) is incinerated as they pass in convoy through a furnace (12). The products from this incineration undergo one or more further treatments. The containers with holes are shaped to roll themselves into the furnace under gravity Before incineration, the waste is dried in the containers in convoy in a dryer (11) heated by the residual heat from the means of heating the incinerator. Part of the gases from the incineration are recycled as fuel to obtain the necessary incineration temperature and/or feed an energy recovery unit (4). The incineration gases are evacuated in pipes (102, 103) whose temperature is controlled by heating or cooling the pipes to avoid the escape of polluting gases. The temperature in the pipes is maintained at between 272 and 357 deg C. Part of the pollutants in the gas are lost in contact with filters or active carbon absorbers in the flow in or after the incinerator. The filters are motor elements (21) containing active carbon and ensuring the rotation of the containers by a racking system. After incineration the solids in the containers and/or the active carbon are washed by passing through a liquid bath (13). After incineration the waste is treated by separating the carbonated solids from the metals, minerals or metal oxides by gravity in a separation bath (18); pumping the carbonated solids in the separation basin and filtering the carbonated solids in a band filter (19) to bring water to ion exchange resins (190). The carbonated solids or the active carbon after filtration of the incineration gas is crushed, mixed and floated on a basin of liquid (230) to agglomerate the carbon with a grease on the surface and collect ashes containing heavy metals at the bottom. Alternatively, the carbonated solids or the active carbon after filtration is contained in a dissolving vessel (211) of supercritical gas, applying temperature and pressure so the separation gas reaches the supercritical state and thus dissolves the caron present in the elements to be treated and leaves a deposit of polluting ash. The supercritical gas is then evacuated and expanded below supercritical conditions so the carbon is deposited as a solid. The gas used is carbon dioxide at a pressure above 73 bar and a temperature above 31 deg C.The ashes containing pollutants are treated by a supercritical liquid chosen to oxidize the metals or degrade the pollutants, in particular by mixing with water and pressurising to 221 bars and 374 deg C. Installation to carry out the above process, with the dryer, the furnace and the dechlorination basin placed in three tunnels, one under the other, interconnected by piston lifts carrying the containers from one tunnel to the next.
机译:废物被装入带有孔的多个容器中,并且当容器(20)在车队中通过炉子(12)时将其焚化。焚化产生的产品经过一种或多种进一步处理。带有孔的容器的形状使其在重力作用下滚动到炉中。在焚化之前,废物在干燥机(11)的车队中的容器中干燥,该干燥器由来自加热焚化炉的残余热量加热。焚化产生的部分气体作为燃料循环使用,以达到必要的焚化温度和/或供入能量回收装置(4)。焚化气体被排入管道(102、103)中,管道的温度通过加热或冷却管道来控制,以避免逸出污染气体。管道中的温度保持在272至357摄氏度之间。在焚烧炉内或之后的流中,气体中的部分污染物与过滤器或活性炭吸收器接触而损失掉。过滤器是装有活性炭并通过货架系统确保容器旋转的电机元件(21)。焚化后,容器中的固体和/或活性炭将通过液浴(13)进行洗涤。焚烧后,通过在分离槽(18)中通过重力将碳酸化的固体与金属,矿物或金属氧化物分离来处理废物。将碳酸化固体泵入分离池,并在带式过滤器(19)中过滤碳酸化固体,以将水带入离子交换树脂(190)。焚化气体过滤后的碳酸化固体或活性炭被粉碎,混合并漂浮在液体盆(230)上,使碳与表面的油脂团聚,并在底部收集含有重金属的灰烬。或者,将过滤后的碳酸盐固体或活性炭容纳在超临界气体的溶解容器(211)中,施加温度和压力以使分离气体达到超临界状态,从而溶解存在于待处理元素中的碳并离开积存的污染灰烬。然后将超临界气体抽空并在超临界条件下膨胀,使碳以固体形式沉积。所使用的气体为二氧化碳,压力高于73 bar,温度高于31℃。含污染物的灰分用超临界液体处理,该液体可氧化金属或降解污染物,特别是与水混合并加压至221在374℃和374摄氏度的压力下进行安装。将干燥机,熔炉和脱氯池放在三个通道中,一个在另一个通道下,并通过活塞升降机相互连接,将容器从一个通道运送到另一个通道。

著录项

  • 公开/公告号FR2822527B1

    专利类型

  • 公开/公告日2003-10-10

    原文格式PDF

  • 申请/专利权人 MAILLOT SARL;

    申请/专利号FR20010003772

  • 发明设计人 PATRICK JEULIN;

    申请日2001-03-20

  • 分类号F23G5/00;F23G5/02;F23G5/46;F27B9/14;B03B9/04;

  • 国家 FR

  • 入库时间 2022-08-21 23:38:06

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