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    • 5. 发明授权
    • Process for the remediation of contaminated particulate material
    • 污染颗粒材料的修复方法
    • US5436384A
    • 1995-07-25
    • US137457
    • 1993-10-18
    • David C. GrantEdward J. LahodaC. P. Keegan
    • David C. GrantEdward J. LahodaC. P. Keegan
    • G21F9/28B03B9/00B09C1/00B09C1/02G21F9/30G21F9/00
    • B03B9/00B09C1/02G21F9/30
    • A method for segregating fines from the clean coarse fraction of the soil, preparing the contaminated fines for subsequent processing, and then separating the contaminants from the clean fines. The process produces a small, highly concentrated contaminanth fraction and a large fraction of clean soil. Metals, metallic compounds, and/or radioactive contaminants are removed from the fine fraction using either gravity separation, multistage gravity separation, a centrifugal jig, regular magnetic or paramagnetic separation using a high gradient magnetic separator, and/or a superconducting separator. Preparation of the fines requires selective segregation of the targeted particles size range and the removal of interfering soil fractions, and vegetation such as root hairs. This preparation is accomplished by a combination of attrition scrubbing, countercurrent jigging, and screening.
    • 一种将细粒与干净的粗糙部分分离的方法,为污染的细粉制备后续加工,然后将污染物与干净的细粉分离。 该过程产生小的,高度浓缩的污染物部分和大部分清洁的土壤。 和/或超导分离器,使用重力分离,多级重力分离,离心夹具,常规磁性或顺磁性分离法,从精细馏分中除去金属,金属化合物和/或放射性污染物。 细粉的制备需要选择性分离目标颗粒尺寸范围和去除干扰的土壤部分,以及植被如根毛。 该制备通过磨擦擦洗,逆流夹击和筛选的组合来实现。
    • 7. 发明授权
    • Method and apparatus for cleaning contaminated particulate material
    • 清洁污染颗粒物的方法和设备
    • US5268128A
    • 1993-12-07
    • US648673
    • 1991-01-31
    • Edward J. LahodaDavid C. Grant
    • Edward J. LahodaDavid C. Grant
    • B09C1/02G21F9/04G21F9/00B03B5/28
    • B09C1/02G21F9/04
    • Particulate material is treated by first washing the contaminated material with a contaminant mobilizing solution comprising a leaching agent, a surfactant or a mixture thereof. Large particles, typically greater than 5 mm are mechanically separated, washed with water and returned to the site as recovered soil. Fines, along with contaminants dissolved or dispersed in the contaminant mobilizing solution are separated from intermediate sized particles by a countercurrent flow of the contaminant mobilizing solution, preferably in a mineral jig. The intermediate sized particles are then abraded in an attrition scrubber to dislodge attached mineral slimes or fines. These additional fines are separated from the intermediate sized particles with a countercurrent flow of wash water in a second mineral jig. The preferred oxidizing agent is chlorine, and hydrogen is the preferred reducing agent.
    • 通过首先用包含浸出剂,表面活性剂或其混合物的污染物移动溶液洗涤被污染的材料来处理颗粒材料。 通常大于5mm的大颗粒机械分离,用水洗涤并作为回收的土壤返回到现场。 细粉以及溶解或分散在污染物移动溶液中的污染物通过污染物移动溶液的逆流流动,优选在矿物夹具中与中等尺寸的颗粒分离。 然后在磨耗洗涤器中研磨中等尺寸的颗粒以除去附着的矿物质泥或细粒。 这些额外的细粉与中等尺寸的颗粒分离,在第二矿物夹具中具有逆流的洗涤水。 优选的氧化剂是氯,氢是优选的还原剂。