首页> 外国专利> Cleaning contaminated materials such as pollutant-contaminated soils from pourable and/or pasty consistency or drying pasty materials and sludge from chamber presses, comprises moving the materials in a closed system into a drying chamber

Cleaning contaminated materials such as pollutant-contaminated soils from pourable and/or pasty consistency or drying pasty materials and sludge from chamber presses, comprises moving the materials in a closed system into a drying chamber

机译:从可倾倒和/或糊状的稠度中清洁受污染的材料(例如污染物污染的土壤),或者从室压机中干燥糊状的材料和污泥,包括将材料在密闭系统中移入干燥室

摘要

The method comprises moving contaminated materials such as pollutant-contaminated soils from pourable and/or pasty consistency in a closed system into a batch-wise loaded drying chamber (1) lockable in the operation and connected with an assigned condenser unit by a circulating mixer (16a) in a dispensed manner and then heating by a heating device for the purpose of the drainage, and transferring the loaded material pretreated in the drying chamber into a decontamination chamber (2) lockable and connected with the assigned condenser unit (4a) after a predetermined time. The method comprises moving contaminated materials such as pollutant-contaminated soils from pourable and/or pasty consistency in a closed system into a batch-wise loaded drying chamber (1) lockable in the operation and connected with an assigned condenser unit by a circulating mixer (16a) in a dispensed manner and then heating by a heating device for the purpose of the drainage, transferring the loaded material pretreated in the drying chamber into a decontamination chamber (2) lockable and connected with the assigned condenser unit (4a) after a predetermined time and after reaching a determined drying grade under a protective gas atmosphere, and exposing a negative pressure in the decontamination chamber for further heating under circulation and/or for evaporating pollutants and subsequently supplying the material from the decontamination chamber to a discharge over the mixer with a water injector. Nitrogen atmosphere is created in the drying and decontamination chambers and/or in dropping pipes, which connect the drying and decontamination chambers and are provided between the decontamination chamber and the mixer, before transferring the material from the drying chamber into the decontamination chamber. Each dropping pipe connects respective pre-arranged chamber at a controllable bottom flap (28a) and has a separating slider. After filling the drying chamber with nitrogen, the bottom flap arranged to the drying chamber opens and fills the dropping pipe area up to the slider with nitrogen and after filling the decontamination chamber with nitrogen, the slider opens and the material transfer is carried out under the protective gas atmosphere. A hot steam occasionally standing under pressure is injected into the drying chamber on both sides in dependent of the consistency, the type of the pollutant of the materials and/or the dimension of the mixer-torque required for the material circulation. The injection of the hot steam is regulated as a function of the continuously detected driving-torque of the mixer. The hot steam generator is heated with energy from a heat exchanger arranged in the exhaust gas flow of the central heating device for heating the chamber. The waste air of the decontamination chamber is subjected to a high temperature post-combustion process and the post-combusted waste air is subsequently supplied to a burner for heating the chamber. The material discharged from the decontamination chamber is cooled off in the closed mixer by injecting water at earth-moist consistency and the water steam developed in the mixer is cleaned and condensed in a closed system. The material in the mixer is admixed to an auxiliary material for immobilizing and connecting heavy metals. Bacteria is supplied to the material in an area of the closed mixer having a temperature of 30-40[deg] C and intensively intermixed with the material. The two drying chambers are operated together with the decontamination chamber for increasing the capacity and/or with high moisture content of the material to be cleaned in a time-delayed and time-overlapped manner. An independent claim is included for a device for cleaning contaminated materials such as pollutant-contaminated soils from pourable and/or pasty consistency or for drying pasty materials and sludge from chamber presses.
机译:该方法包括将污染物质(例如污染物污染土壤)从密闭系统中的可倾倒和/或糊状浓稠度移入可锁定运行的分批装载干燥室(1)中,并通过循环混合器与指定的冷凝器单元连接( 16a)以分配的方式,然后通过加热设备进行排水,然后将在干燥室中预处理过的装载物料转移到可锁定并与分配的冷凝器单元(4a)连接的去污室(2)中。预定时间。该方法包括将污染物质(例如污染物污染土壤)从密闭系统中的可倾倒和/或糊状浓稠度移入可锁定运行的分批装载干燥室(1)中,并通过循环混合器与指定的冷凝器单元连接( 16a)以分配的方式,然后通过加热设备进行排水,将在干燥室中预处理过的装料转移到可锁定的净化室(2)中,并在预定时间后与分配的冷凝器单元(4a)连接时间并在保护性气体气氛下达到确定的干燥等级后,在去污室中暴露负压,以便在循环下进一步加热和/或蒸发污染物,随后将来自去污室的物料供应到混合器上的出料口中注水器。在将材料从干燥室转移到去污室中之前,在干燥和去污室和/或滴管中产生氮气气氛,所述干燥室和干燥室连接干燥和去污室,并设置在去污室和混合器之间。每个下降管在可控制的底部活门(28a)处连接各自的预先布置的腔室,并且具有分离滑块。在用氮气填充干燥室之后,打开干燥室的底部挡板,并用氮气填充滴管区域直至滑块,然后在用氮气填充去污室之后,滑动板打开,并在管道下方进行物料转移。保护性气体气氛。取决于稠度,物料污染物的类型和/或物料循环所需的混合扭矩的大小,偶尔会在压力下站立的热蒸汽从两侧注入干燥室。根据连续检测到的混合器的驱动转矩来调节热蒸汽的注入。热蒸汽发生器被来自热交换器的能量加热,该热交换器布置在中央加热装置的排气流中,用于加热腔室。净化室的废气经过高温后燃烧过程,然后将燃烧后的废气供给燃烧器以加热该室。从去污室排出的物料在密闭的混合器中通过以湿地浓度注入水而冷却,并且在密闭的系统中清洁并冷凝在混合器中产生的水蒸汽。混合器中的物料与辅助物料混合,以固定和连接重金属。细菌在温度为30-40℃的密闭混合器的区域中被供应给物料,并与物料充分混合。两个干燥室与去污室一起操作,以便以时间延迟和时间重叠的方式增加待清洁材料的容量和/或高水分含量。包括一个独立的权利要求,涉及一种用于清洁污染的材料(例如污染物污染的土壤)的可倾倒和/或糊状稠度的设备,或用于干燥来自压滤机的糊状材料和污泥的设备。

著录项

  • 公开/公告号DE102008006719A1

    专利类型

  • 公开/公告日2009-08-06

    原文格式PDF

  • 申请/专利权人 CZETSCH ALEXANDER;

    申请/专利号DE20081006719

  • 发明设计人 CZETSCH ALEXANDER;

    申请日2008-01-30

  • 分类号A62D3/40;B09C1/06;

  • 国家 DE

  • 入库时间 2022-08-21 19:09:19

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