Patent Number: 051280680
Section: summary

BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to a method and apparatus for cleaning particulate materials such as soils which are contaminated with a variety of contaminants such as heavy metals, radioactive compounds and organics, often in combination, through a combination of leaching, washing, attrition scrubbing, countercurrent flow size separation and density separation. 2. Background Information Contaminated soil is becoming a more common environmental problem. The contaminants can include heavy metals, such as for instance, copper, lead and mercury; radioactive species such as radium, uranium and thorium; and organics such as for example, oils, polychlorinated biphenyls, flue soot and others. Various techniques have been developed to remove specific contaminants. For instance, heavy metals are known to be found predominantly in the silt, humic or clay fraction of soil. Hence, they can be removed by size separation such as tiltable tables, cocurrent flow in a mineral jig and chemical techniques such as the use of precipitants. The radioactive compounds are generally soluble and can be removed to a large extent by leaching. Since these compounds are often also present in the finer particles, the most severely contaminated fraction can also be removed by countercurrent flow size separation. Organics can be removed by washing with surfactants, thermal treatment or biological processes. Special problems develop when the different types of contaminants are present in soil. Generally, biological or thermal processes are more effective for removing organics than washing. However, toxic inorganics such as lead or chromium (+6), if present, deactivate biological systems due to their toxicity and cause air pollution problems for thermal processes. In addition, thermal processes may mobilize otherwise fixed contaminants in the treated soil. Radioactive contamination (e.g., uranium, thorium radium, etc.) can be removed by soil washing. Soil washing provides a means to process soils having multiple contaminants. The washed soil is accessible to further biological or thermal treatment. Inorganic and radioactive compounds may be separated from organics for separate sale or disposal. Many soil washing processes are available. Most use mining equipment to provide intimate soil/surfactant contact U.S. Pat. No. 4,783,253 discloses a process for separating radioactive contaminants from soil using a cocurrent flow of water to float away lighter uncontaminated particles from heavy contaminated particles. The slurry of lighter particles is dewatered using a spiral classifier, centrifuge, filter or the like. U.S. Pat. No. 4,783,263 is directed to a process for removing toxic or hazardous substances, in particular organics, from soils and the like by converting the material to a slurry adding surfactants and/or alkaline agents, and concentrating the toxic substance in the liquid phase preferably with a modifier in a froth flotation cell. Some of the limitations of the currently used processes are that they are optimized for removing only one type of contaminant or for cleaning only one type of soil, they are geared to cleaning the larger particles while concentrating the fines in a fraction for later disposal, and they often use filtration for water removal which is a capital intensive operation with high operating costs. There is a need therefore for an improved process and apparatus for treating particulate materials, such as soil and the like, contaminated with mixed wastes such as radioactive materials, organics and heavy metals. There is a further need for such a process and apparatus which separates organic and inorganic contaminants thereby allowing for optimum disposal routes or post treatment strategies to be used on the concentrated contaminated fractions. There is also a need for such a process and apparatus which produces a high solids content fines. There is yet another need for such a process and apparatus which is not capital intensive, is economical to operate and can be made portable for on-site treatment. SUMMARY OF THE INVENTION These and other needs are satisfied by the invention which is characterized by treating particulate materials such as soils, sludges, sediments, scrap yard dust and the like, contaminated with radioactive compounds, heavy metals, and organics, either singly or in combination, by first washing the particulate material with a contaminant mobilizing solution which can consist of leaching solutions, surfactants, and mixtures thereof to mobilize soluble and dispersible contaminants in a liquid phase of the contaminant mobilizing solution. Mechanical separation means are then used to separate large particles of a size substantially free of residual contamination, typically larger than 5 mm, from intermediate sized particles and fines in the contaminant mobilizing solution. These separated large particles are washed with a water based cleaning solution to produce recovered particulate material. Fines are size separated from the intermediate sized particles in the contaminant mobilizing solution with a countercurrent flow of the contaminant mobilizing solution to form a waste slurry. The size separation is preferably performed in a mineral jig. The intermediate sized particles from which the fines have been separated are attrition abraded to dislodge attached fines. These dislodged fines are then separated from the intermediate sized particles by a countercurrent flow of wash water to form additional waste slurry and an effluent of the intermediate sized particles and wash water. The intermediate sized particles are dewatered to produce additional recovered particulate material. If the particulate material has been contaminated with insoluble heavy metals, they can be separated from the effluent of intermediate sized particles and wash water emerging from the second size separation by density separation such as by a cross-current pulsed flow of wash water prior to dewatering. The scrubbing of the particles removes the mineral slimes or fine particles adhering to the intermediate sized particles. As is known, these dislodged fine particles have a very large surface area which is chemically active. Some solubilized contaminants have a high affinity for the surface area of these fine particles. Hence, in accordance with the broad process defined by the invention, the dissolved contaminants are drawn off in the first size separation before scrubbing to dislodge fines. These dislodged fines are then separated in a second sizing countercurrent flow using wash water. In applications in which contamination of dislodged fines with dissolved contaminants is not a problem, another attrition abrading step can be carried out prior to the initial size separation of fines using a countercurrent flow of the contaminant mobilizing solution. The invention is further characterized by using the water obtained by dewatering the intermediate sized particles remaining after the second size separation as the wash water for the second size separating countercurrent flow. The countercurrent flow rate in the size separating steps can be adjusted to adjust the size of the fines removed. The adjustment is made to balance the percentage of soil particles recovered and allowable levels of residual contamination. Typically, fines smaller than about 60 microns are removed in the waste slurry. The actual size removed will be dependent upon the contaminant distribution as a function of particle size, and can vary from less than 200 to 10 microns. Another novel aspect of the invention is the operation of a mineral jig in a countercurrent flow mode to effect size separation of fines from the slurry while simultaneously washing the particulate material. In one stage the mobilizing solution is used to produce the countercurrent flow, while wash water is used in the final size separating stage for removing fines. The waste slurry from the two countercurrent flow size separating steps containing the fines, dissolved metals including the radioactive contaminants, and the organics, is further treated to remove the fines and contaminants and to produce clean contaminant mobilizing solution which is recirculated. In one embodiment of the invention the dissolved metals are precipitated by a sulfide. The precipitates and fine soil particles are removed by dewatering and the decontaminant mobilizing solution can be further treated such as in an ion exchange bed to remove radioactive solution contaminants and passed through a carbon bed to remove the organic load before being recycled.