
Soil and Groundwater Contamination Survey and Countermeasure Technologies
| Category of Tchnology | Treatment | Treatment | |
| Media | Soil | ||
| Contaminants |
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| Applied (Demonstrated) Substances | Tetrachloroethylene | ||
| Scope | Concentration Range | ||
| Hydrogeological Conditions |
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| Chemical Soil Properties | |||
| Other Remarks | |||
| Technology Description | Classification | Decomposition | |
| Status |
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| Outline of Technology | The contaminated soil is heated at below 500°C within an indirect heating multi-cylinder rotary kiln, to vaporize the volatile matters and collect them. The waste gas is treated by absorption by activated carbon before being discharged to the ambient air. The waste gas from the heating process can be used as carrier gas. The treatment capacity is 2 tons/hour or 4 tons/hour. | ||
| Required Pre- and Post-treatment | Because the contaminated soil is heated indirectly by getting in touch with the retort pipes, the pre-treatment required before the soil enters the kiln includes the removal of wood chips, stones, etc., crushing of earth blocks and clays, and the removal of water contents if the soil is wet with groundwater. | ||
| Enhance Effectiveness through Combination | If high concentrations of contaminants exist in their original liquid form, vacuum extraction of such matters as a prior on-site treatment will be a good choice. | ||
| Case History | When the contaminated soil containing up to 1000 mg/kg of tetrachloroethylene was heated at low-temperature, the removal rate of the tetrachloroethylene was 99.1% at 135°C, 99.9% at 185°C and 99.99% at 235°C. In this test, the sensor tube did not detect tetrachloroethylene in the waste gas which was treated by active carbon. No analysis was made of other poisonous matters. | ||
| Application Examples | This method has been put to use at several locations, using the system with the processing capacity of 2 tons/hour. | ||
| Limitations | |||
| Properties of Treated Soil | Properties are Generally Retained
* Properties may change depending on the heating conditions. |
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| Schematic Flow Process |
Flow Chart of the Low-temperature Heating Devices and After-treatment |
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| Applicability | In Situ Applicability | Possible | |
| Ground Structures |
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| Required Excavation | Excavated soil is treated. (To be applied to excavated soil.) | ||
| Groundwater Extraction | |||
| Required Space | Space for the installation of a set of devices (For example, 4 m x 3 m) | ||
| Operational Time | |||
| Installation Time | |||
| Maintenance and Control Requirements | |||
| Additional Remarks | |||
| Secondary Impacts to Environment | Secondary Treatment Required? | ||
| Effects on Living Environment | Noise | ||
| Additives | |||
| Possibility of Contaminant Spreading | Contaminants may disperse in the pre-treatment. | ||
| Secondary By-products | A higher heating temperature will be needed to improve the contaminant removal rate of the soil. In this case, however, toxic substances may form in the heating process. | ||
Soil Environment Management Division, Water Environment Department, Environmental Management Bureau, Ministry of Environment
Tel: +81-3-5521-8319
E-mail: MOE@env.go.jp