JP5612820B2 - Purification method for organic chlorine chemical contamination - Google Patents

Description

  The present invention relates to a method for chemically purifying soil, groundwater and the like contaminated with chemical substances, particularly organic compounds.

  Organochlorine compounds such as trichlorethylene (TCE) and tetrachloroethylene (PCE) are widely used as cleaning agents in various factories and cleaning shops, but these organochlorine compounds are suspected to be carcinogenic substances. Contamination of soil and groundwater with organochlorine compounds has become a major social problem.

  Conventionally, as a method for treating soil contaminated with organochlorine compounds, mainly containment treatment of contaminated soil, excavation / containment treatment of contaminated soil, and the like. In addition, groundwater contaminated with organochlorine compounds can be treated by pumping groundwater, transferring contaminated chemicals in the groundwater into the gas phase, purifying the groundwater (pumped water aeration treatment), and then using activated carbon. The pump-and-treat method, etc., that adsorbs the phase (activated carbon treatment) is mainly performed. In addition, the water after purification flows to the surface.

  However, the above containment process, excavation / containment process, and pump and treat method are not technologies for actively decomposing and detoxifying polluting chemicals, and enormous costs, energy, and labor are required. There are problems such as a long purification period of 10 to 20 years.

  On the other hand, in recent years, in-situ chemical oxidation in which an oxidizing agent is directly injected into a well has been developed. Oxidizing agents include potassium permanganate, hydrogen peroxide, persulfate, hypochlorous acid, perchloric acid, chlorine, ozone, etc., but in terms of solubility in water, operability, etc. Therefore, methods using potassium permanganate or hydrogen peroxide are mainly put into practical use.

  However, the method using potassium permanganate has a problem that the potassium permanganate itself has a purple color and it is not preferable to inject it directly into groundwater or the like. Further, the method using hydrogen peroxide has a problem that the purification range is small due to rapid hydrogen peroxide decomposition in the ground.

  In contrast, there are an increasing number of cases of research on decomposition of pollutants using persulfate. For example, Patent Document 1 discloses a method of adding a persulfate and a pH adjuster for maintaining a pH of 10 or more to a pollutant of an organic compound.

Special table 2008-506511

  However, as a result of experiments conducted by the present inventors to purify ground water that is actually polluted or ground water that is actually polluted and soil, the purifying method disclosed in Patent Document 1 has a purifying purpose. Decomposition of organochlorine compounds such as tetrachloroethylene is not always rapid, and the purification method maintains the pH at 10 or higher, resulting in high processing costs. Especially at pH 11 or higher, problems such as elution of heavy metals occur. It was confirmed that there was a possibility.

  Moreover, as a result of the present inventors conducting an experiment of decomposing organochlorine compounds using persulfate, a case where distilled water was used and actual groundwater or a combination of actual groundwater and soil was used. In addition, it was confirmed that the decomposition behavior of the organochlorine compound differs greatly when the organochlorine compound has a low concentration of several mg / L or less and a high concentration of several tens mg / L. And since the purification method of patent document 1 uses distilled water and is a purification method under special environmental conditions where the organochlorine compound has a high concentration, applying the purification method to an actual site. Is practically difficult.

  Therefore, the present invention has been made in view of the above-described circumstances, and contaminants (soil, groundwater, etc.) contaminated with a chemical substance such as an organic chlorine compound are reliably and safely used using a persulfate and an alkali agent. The purpose is to provide a method of purifying.

The present invention is a chemical contamination purification method for purifying contaminants by adding persulfate and caustic soda to contaminants contaminated with chemical substances, wherein the concentration of persulfate in the reaction region is 5000 mg / L or more. In addition to adding persulfate so that the final pH of the reaction region is in the range of 5 to less than 10, the caustic soda is added in a molar ratio of 0.4 to 2. Add in the range of 0 or less.

The present invention also relates to a chemical contamination purification method for purifying soil and groundwater by adding persulfate and caustic soda in situ to soil and groundwater contaminated with chemical substances, wherein the persulfate in the reaction region The persulfate is added so that the concentration becomes 5000 mg / L or more, and the caustic soda is added in a molar ratio of 0 to the persulfate so that the final pH of the reaction region is in the range of 5 to less than 10. Add in the range of 4 to 2.0.

In the chemical contamination purification method, the amount of the persulfate and the caustic soda is monitored so that the final pH of the reaction region is in the range of 5 or more and less than 10 by monitoring the pH of the reaction region. Is preferably adjusted.

  In the chemical substance contamination purification method, the persulfate is preferably potassium persulfate, sodium persulfate, or ammonium persulfate.

  In the chemical substance contamination purification method, the alkaline agent is preferably potassium hydroxide, caustic soda or ammonium hydroxide.

  In the chemical substance contamination purification method, the chemical substance is preferably an organic chlorine compound.

  Further, the chemical substance contamination purification apparatus of the present invention comprises a persulfate addition means for adding persulfate in situ to soil and groundwater contaminated with chemical substances, and an alkaline agent in situ to the soil and groundwater. An alkali agent addition means for adding, wherein the persulfate addition means adds persulfate so that the persulfate concentration in the reaction region is 5000 mg / L or more, and the alkali agent addition means The alkaline agent is added in a molar ratio range of 0.4 to 2.0, relative to the persulfate, so that the final pH of the region is in the range of 5 to 10.

  The chemical contamination purification apparatus further comprises monitoring means for monitoring the pH of the reaction region, wherein the persulfate addition means and the alkaline agent addition means are based on the pH monitored by the monitoring means. It is preferable to adjust the addition amount of the persulfate and the alkali agent so that the final pH of the solution is in the range of 5 or more and less than 10.

  Further, in the purification apparatus for chemical substance contamination, the persulfate is preferably potassium persulfate, sodium persulfate or ammonium persulfate.

  In the chemical substance contamination purification apparatus, the alkaline agent is preferably potassium hydroxide, caustic soda or ammonium hydroxide.

  In the chemical substance contamination purification apparatus, the chemical substance is preferably an organic chlorine compound.

  According to the present invention, contaminants (soil, groundwater, etc.) contaminated with a chemical substance such as an organic chlorine compound can be reliably and safely purified using a persulfate and an alkali agent.

  Embodiments of the present invention will be described below. This embodiment is an example for carrying out the present invention, and the present invention is not limited to this embodiment.

  FIG. 1 is a schematic diagram showing an example of the configuration of a chemical substance contamination purification apparatus according to an embodiment of the present invention. As shown in FIG. 1, the chemical contamination purification apparatus 1 includes a persulfate storage tank 10 as a persulfate addition means, a first pump 12, a persulfate injection line 14 and an injection well 16, and an alkaline agent addition means. As an alkaline agent storage tank 18, a second pump 20 and an alkaline agent injection line 22 (and an injection well 16), a pumping pump 24 as a pumping means, a pumping line 26 and a pumping well 28, and an aeration tank 30 as an aeration processing means. And an aeration treated water line 32.

  As the configuration of the persulfate addition means, FIG. 1 illustrates the configurations of the persulfate storage tank 10, the persulfate injection line 14, the first pump 12, and the injection well 16, but the soil and groundwater contaminated with chemical substances are used. The configuration is not limited to the above as long as the persulfate can be added in-situ. In the present embodiment, one end of the persulfate injection line 14 is connected to the persulfate storage tank 10, and the persulfate is in situ (substantially the injection well 16) from the other end of the persulfate injection line 14. The other end of the persulfate injection line 14 is disposed in the injection well 16 for release into the injection well 16. The persulfate injection line 14 is provided with a first pump 12.

  As the configuration of the alkaline agent addition means, the configuration of the alkaline agent storage tank 18, the second pump 20, the alkaline agent injection line 22 and the injection well 16 is illustrated in FIG. 1, but in situ in soil and groundwater contaminated with chemical substances. If it is the structure which can add an alkaline agent, it will not restrict | limit to the above. In this embodiment, one end of the alkaline agent injection line 22 is connected to the alkaline agent storage tank 18, and the alkaline agent is discharged from the other end of the alkaline agent injection line 22 to the original position (substantially in the injection well 16). In order to do this, the other end of the alkaline agent injection line 22 is connected to the persulfate injection line 14. The alkaline agent injection line 22 is provided with a second pump 20. In this embodiment, the alkaline agent injection line 22 is connected to the persulfate injection line 14, but it is not always necessary to connect to this, and the other end of the alkaline agent injection line 22 is in the injection well 16. It may be arranged.

  As a configuration of the pumping means, FIG. 1 illustrates the configuration of the pump 24, the pumping line 26, and the pumping well 28. However, the configuration is limited to the above as long as the groundwater after purification treatment can be pumped to the ground surface. It is not a thing. In the present embodiment, the pumping well 28 is disposed at least on the downstream side of the groundwater from the injection well 16 in order to pump up the groundwater after the purification treatment. A pumping pump 24 is provided in the pumping line 26 arranged in the pumping well 28. One end of the pumping line 26 is connected to the aeration tank 30.

  Although the configuration of the aeration tank 30 and the aeration treatment water line 32 is illustrated in FIG. 1 as the aeration treatment means, the aeration treatment means is not limited to the above as long as the aeration treatment means can perform aeration treatment of the pumped ground water. In the present embodiment, one end of the aerated treated water line 32 is connected to the aeration tank 30, and the other end is connected to the persulfate injection line 14.

  Below, operation | movement of the purification apparatus of the chemical substance contamination which concerns on this embodiment is demonstrated.

  First, the first pump 12 is operated, and the persulfate in the persulfate storage tank 10 is supplied from the persulfate injection line 14 to the soil and groundwater contaminated with chemical substances through the injection well 16. To do. Then, while the groundwater to which the persulfate is added flows through the reaction region X, the persulfate oxidatively decomposes (purifies) the contaminating chemical substance existing in the reaction region X. At this time, the persulfate is injected so that the persulfate concentration in the reaction region X is 5000 mg / L or more. In particular, it is preferable to inject the persulfate so that the perchloric acid concentration in the reaction region X is in the range of 5000 mg / L to 25000 mg / L, so that it is in the range of 10,000 mg / L to 25000 mg / L. It is more preferable to inject persulfate into the tube. If the persulfate concentration is less than 5000 mg / L, the persulfate is consumed due to the influence of organic substances and inorganic ions present in the soil and groundwater, and it is difficult to sufficiently decompose high-concentration pollutants. Become. In addition, the degradation rate of pollutant chemicals is also reduced. On the other hand, when the persulfate concentration exceeds 25000 mg / L, the amount of chemicals used increases, and the cost increases.

  Moreover, the 2nd pump 20 is operated and the alkaline agent in the alkaline agent storage tank 18 is supplied from the alkaline agent injection line 22 to the original position of soil and groundwater contaminated with chemical substances through the injection well 16. At this time, the alkali agent is in a range of 0.4 to 2.0 in molar ratio to the persulfate so that the final pH of the reaction region X is in the range of 5 to less than 10. inject. In particular, it is preferable to inject the alkali agent so as to have a molar ratio of 0.8 to 1.6 with respect to the persulfate. When the molar ratio of the alkaline agent to the persulfate is less than 0.4, it is difficult to make the final pH of the reaction region X 5 or more. When the final pH of the reaction zone X is less than 5, there is a concern about chemical corrosion on the concrete structure, and elution of heavy metals from the soil may occur. In addition, the impact on the ecosystem will increase. For these reasons, it is difficult to apply this method when purifying the pollution under the building or in an area where lakes and ponds exist around the purification area. Moreover, when the molar ratio of the alkaline agent to the persulfate exceeds 2.0, it becomes difficult to make the final pH of the reaction region X less than 10 and the decomposition rate of the chemical substance decreases. Further, the processing cost increases. In particular, when the pH is 11 or more, elution of heavy metals from soil may occur.

  Here, the final pH of the reaction region X is a pH after the decomposition of the persulfate, for example, a pH downstream of the reaction region X. Specifically, the final pH of the reaction region X is obtained by measuring the pH of groundwater flowing through the pumping line 26.

  Here, the addition timing of the alkaline agent may be simultaneous with the addition of the persulfate, but when the pH is neutral or lower, the decomposition rate of the pollutant chemical substance is increased. It is preferable to inject the alkaline agent after injecting into the groundwater and setting the pH of the reaction region X to neutral or lower to decompose the contaminating chemicals. Moreover, if the molar ratio of the alkaline agent to the persulfate is in the range of 0.4 to 2.0, the in-situ injection may be repeated in the order of the addition of the persulfate and the addition of the alkaline agent. Good.

  In the present embodiment, the adjustment of the amount of persulfate added by the persulfate addition means and the adjustment of the amount of alkali agent added by the alkali agent addition means are not particularly limited as long as they are added so as to satisfy the above numerical range. Although there is no pH monitoring means such as a pH meter for monitoring the pH of the reaction zone X, the amount of persulfate added by the persulfate addition means and the amount of alkali agent by the alkali agent addition means are determined based on the monitored pH value. It is preferable to adjust the addition amount.

  The pH of the reaction zone X is monitored by, for example, installing a pH meter in the pumping line 26 or the pumping well 28 and measuring the pH of groundwater passing through the pumping line 26 (or accumulating in the pumping well 28). This is done by monitoring the pH of reaction zone X.

  Next, by operating the pumping pump 24, the groundwater purified by the addition of persulfate is sent from the pumping line 26 to the aeration tank 30. In the aeration tank 30, for example, groundwater is flowed in a downward flow, air is aerated in the groundwater, and pollutant chemicals remaining in the water are transferred into the gas phase. The treated water after aeration is supplied to the original position of soil and groundwater through the aerated treated water line 32 and the persulfate injection line 14. Since the persulfate added by the persulfate addition means remains in the treated water after aeration, the remaining persulfate can be reused for purification of pollutant chemical substances. As a result, since the persulfate can be efficiently used for the purification of pollutant chemical substances, the amount of persulfate used can be suppressed.

  FIG. 2 is a schematic diagram showing an example of the configuration of a chemical substance contamination purifying apparatus according to another embodiment of the present invention. In the chemical substance contamination purification apparatus 2 shown in FIG. 2, the same components as those of the chemical substance contamination purification apparatus 1 shown in FIG. The chemical contamination purification apparatus 1 shown in FIG. 1 reuses the treated water after aeration for purification of the contaminated chemical substances, whereas the chemical contamination purification apparatus 2 shown in FIG. Through the water line 32, the treated water after aeration is discharged to the ground surface. The chemical contamination purification device 2 shown in FIG. 2 is suitable when the persulfate concentration in the groundwater passing through the pumping line 26 is low.

  Although the aeration processing means is provided in the chemical substance contamination purification apparatuses (1, 2) shown in FIGS. 1 and 2, the aeration processing means may be installed as necessary.

  FIG. 3 is a schematic diagram showing an example of the configuration of a chemical substance contamination purifying apparatus according to another embodiment of the present invention. In the chemical substance contamination purification apparatus 3 shown in FIG. 3, the same components as those in the chemical substance contamination purification apparatus 1 shown in FIG. In the present embodiment, since the groundwater after purification is not pumped, the reaction region Y to which the persulfate and the alkali agent are added spreads in a substantially circular shape around the injection well 16. 3, the observation well 34 for observing the pH of the reaction region Y is provided in the reaction region Y, and the pH of the groundwater accumulated in the observation well 34 is measured. However, the observation well 34 may be provided outside the reaction region Y.

  The persulfate used in the present embodiment is not particularly limited as long as it can purify contaminating chemicals, but potassium persulfate, persulfate, and water are highly soluble and inexpensive. Sodium sulfate or ammonium persulfate is preferred. In particular, sodium persulfate is particularly preferred because it generates sodium ions and sulfate ions during the purification of pollutant chemicals, both of which are relatively friendly from the standpoint of the environment and health.

Caustic soda is used as the alkaline agent used in the present embodiment . As reference example, for example, potassium hydroxide, water oxidation ammonium beam or the like.

  In the present embodiment, it is preferably used for purification of soil, sediment, sludge, groundwater, etc. contaminated with organic chlorine compounds such as trichlorethylene, tetrachloroethylene, dioxins, polychlorinated biphenyls, but is not limited thereto. It is not a thing. That is, the present invention can be applied not only to the purification of contaminants by organic chlorine compounds, but also to the purification of contaminants by other organic substances such as oil, benzene, toluene, xylene and the like.

  Hereinafter, although an example and a comparative example are given and the present invention is explained more concretely in detail, the present invention is not limited to the following examples.

Example 1
50 g of soil collected from the actual contamination site and 10 mL of contaminated groundwater were placed in a vial. Concentrations of contaminating chemical substances in the groundwater were cis 1,2-dichloroethylene: 0.09 mg / L, trichloroethylene: 0.09 mg / L, and tetrachloroethylene: 0.64 mg / L. Next, sodium persulfate was added to the vial so that the sodium persulfate concentration was 10,000 mg / L, and the molar ratio of sodium hydroxide to sodium persulfate was 0, 0.2, 0.4, 0.6, 0. Caustic soda was added to the vial so as to be 0.8, 1.0, 1.2, 1.6, and 2.0. And the pH of the groundwater in that case was measured. Thereby, pH (namely, initial pH) of groundwater in the state where persulfate is not decomposed can be checked.

  Next, 10 mL of contaminated groundwater was placed in a vial. Then, sodium persulfate was added to the vial so that the sodium persulfate concentration was 10,000 mg / L. Thereafter, heat treatment was carried out at 120 ° C. for 1 hour in an autoclave to react with sodium persulfate (decompose into sodium sulfate). After cooling, 50 g of soil collected from the actual contamination site is added to the vial, and the molar ratio of caustic soda to sodium persulfate is 0, 0.2, 0.4, 0.6, 0.8, 1 Caustic soda was added to the vials to 0.0, 1.2, 1.6, 2.0. And the pH of the groundwater in that case was measured. Thereby, pH after decomposition | disassembly of sodium persulfate (namely, final pH) can be confirmed.

  4 is a graph showing the relationship between the pH of groundwater and the molar ratio of caustic soda to sodium persulfate in Example 1. FIG. As shown in FIG. 4, when the molar ratio of caustic soda to sodium persulfate having a concentration of 10,000 mg / L is 1.0 to 2.0, the initial pH is 10 or more, but the final pH is 10 or less. And when the molar ratio of the caustic soda with respect to sodium persulfate was the range of 0.2-2.0, it was confirmed that final pH will be 5-10. If the final pH is 10 or less, elution of heavy metals due to high alkali can be suppressed. In particular, when the molar ratio of caustic soda to sodium persulfate is in the range of 0.4 to 2.0, it is possible to perform more reliable, safe and inexpensive purification treatment.

(Example 2)
50 g of soil collected from Site A and Site B, which are actual contamination sites, and 10 mL of contaminated groundwater were placed in separate vials. The concentration of contaminating chemicals in the ground water at Site A was cis 1,2-dichloroethylene: 1.80 mg / L (trichlorethylene and tetrachlorethylene are below the detection limit). Concentrations of contaminating chemicals in the groundwater at Site B were cis 1,2-dichloroethylene: 0.09 mg / L, trichlorethylene: 0.09 mg / L, and tetrachloroethylene: 0.64 mg / L.

  Next, sodium persulfate was added to the vial so that the sodium persulfate concentration was 5000 mg / L, and the molar ratio of caustic soda to sodium persulfate was 0, 0.2, 0.4, 0.6, 0. Caustic soda was added to the vial so as to be 0.8, 1.0, 1.2, 1.6, and 2.0. And the initial pH of the groundwater in that case was measured.

  Next, 10 mL of contaminated groundwater collected from Site A and Site B was placed in separate vials. Then, sodium persulfate was added to the vial so that the sodium persulfate concentration was 5000 mg / L. Thereafter, heat treatment was carried out at 120 ° C. for 1 hour in an autoclave to react with sodium persulfate (decompose into sodium sulfate). After cooling, 50 g of soil collected from Site A and Site B are added to separate vials, and the molar ratio of caustic soda to sodium persulfate is 0, 0.2, 0.4, 0.6, 0. Caustic soda was added to the vial so as to be 0.8, 1.0, 1.2, 1.6, and 2.0. Then, the final pH of the groundwater after the decomposition of sodium persulfate was measured.

  Table 1 summarizes the relationship between the molar ratio of sodium hydroxide to sodium persulfate and the initial and final pH at Site A and Site B.

  As can be seen from Table 1, if the molar ratio of caustic soda to sodium persulfate having a concentration of 5000 mg / L is in the range of 0.4 to 2.0, the final pH is 5 to less than 10. confirmed. If the final pH is 10 or less, elution of heavy metals due to high alkali can be suppressed. In particular, when the molar ratio of caustic soda to sodium persulfate is in the range of 0.8 to 1.6, it is possible to perform more reliable, safe and inexpensive purification treatment. These results showed the same tendency also in various soils.

(Example 3)
20 mL of ground water and trichlorethylene (concentration of about 0.66 mg / L) collected from the actual contamination site were placed in a vial. Next, sodium persulfate is added to the vial so that the sodium persulfate concentration is 10,000 mg / L, and the molar ratio of sodium hydroxide to sodium persulfate is 0, 0.8, 1.6, and 2.4. Caustic soda was added to the vial. Then, the concentration of trichlorethylene over time was measured.

  FIG. 5 is a graph showing the relationship between the concentration of trichlorethylene and the elapsed time at each molar ratio of sodium hydroxide to sodium persulfate. As shown in FIG. 5, the smaller the molar ratio of sodium hydroxide to sodium persulfate, the shorter the time required for the decomposition of trichlorethylene. However, as shown in the above examples, when the molar ratio of caustic soda to sodium persulfate is small, the final pH becomes strongly acidic, and when the molar ratio of caustic soda to sodium persulfate is large, the final pH is Strongly alkaline. When it becomes strongly acidic or strongly alkaline, there is a concern such as elution of heavy metals from the soil. Accordingly, the molar ratio of caustic soda to sodium persulfate is 0 in order to maintain the pH of groundwater (from 5 to less than 10) for safe purification treatment within a range where the time required for the decomposition of trichlorethylene is not prolonged. It is necessary to be within an appropriate range of 4 or more and 2.0 or less.

Example 4
20 g of soil collected from the actual contamination site, 20 mL of contaminated groundwater and trichlorethylene (concentration of about 5.6 mg / L) were placed in a vial. Next, sodium persulfate was added to the vial so that the sodium persulfate concentration was 5000 mg / L, and caustic soda was added to the vial so that the molar ratio of caustic soda to sodium persulfate was 1.6. Then, the concentration and pH of trichlorethylene over time were measured.

  FIG. 6 is a graph showing the relationship between the concentration of trichlorethylene and the elapsed time in Example 4. In addition, Table 2 summarizes the results of the pH of groundwater over time.

  As shown in FIG. 6, it was confirmed that trichlorethylene was reliably decomposed even when the sodium persulfate concentration was 5000 mg / L. Further, it was confirmed that when the molar ratio of caustic soda to sodium persulfate having a concentration of 5000 mg / L was 1.6, the final pH was maintained at 5 or more and less than 10.

(Example 5)
20 mL of pure water and trichlorethylene (concentration of about 2.0 mg / L) were placed in a vial. Next, sodium persulfate is added to the vial so that the sodium persulfate concentration is 5000 mg / L, and the molar ratio of sodium hydroxide to sodium persulfate is 0.2, 0.4, 0.8, 1.2. , 1.6, 2.0, 2.4 Caustic soda was added to the vial. Then, the concentration of trichlorethylene over time was measured.

  FIG. 7 is a graph showing the relationship between the concentration of trichlorethylene and the elapsed time at each molar ratio of sodium hydroxide to sodium persulfate. As shown in FIG. 7, the smaller the molar ratio of caustic soda to sodium persulfate having a concentration of 5000 mg / L, the shorter the time required for decomposition of trichlorethylene. However, as shown in the above examples, when the molar ratio of sodium hydroxide to sodium persulfate is small, the final pH becomes strongly acidic, and when the molar ratio of sodium hydroxide to sodium persulfate is large, the final pH is strong. It becomes alkaline. When it becomes strongly acidic or strongly alkaline, there is a concern such as elution of heavy metals from the soil. Therefore, in order not to prolong the time required for the decomposition of trichlorethylene and to maintain a pH (5 or more and less than 10) for safe purification treatment, the molar ratio of caustic soda to sodium persulfate is set to 0. It is necessary to make it into the suitable range of 4 or more and 2.0 or less.

  As described above, the persulfate is added so that the persulfate concentration in the reaction region is 5000 mg / L or more, and the alkaline agent is added so that the final pH in the reaction region is 5 or more and 10 or less. By adding it in a molar ratio range of 0.4 to 2.0 with respect to persulfate, soil, groundwater, etc. contaminated with chemical substances such as organochlorine compounds can be more reliably and safely reduced. It can be purified at a low cost, and its usefulness is extremely large. Conventionally, since the final pH of the reaction region shows strong acidity or strong alkalinity, concerns such as elution of heavy metals arise, and when the final pH of the reaction region is strong acidity, the purification of the vicinity of the concrete structure is caused. Application of was difficult. However, the applicable purification range can be expanded by the present invention.

It is a schematic diagram which shows an example of a structure of the purification apparatus of the chemical substance contamination which concerns on embodiment of this invention. It is a schematic diagram which shows an example of a structure of the purification apparatus of the chemical substance contamination which concerns on other embodiment of this invention. It is a schematic diagram which shows an example of a structure of the purification apparatus of the chemical substance contamination which concerns on other embodiment of this invention. It is a figure which shows the relationship between the pH of groundwater in Example 1, and the molar ratio of the caustic soda with respect to sodium persulfate. It is a figure which shows the relationship between the density | concentration of trichlorethylene in each molar ratio of caustic soda with respect to sodium persulfate, and elapsed time. It is a figure which shows the relationship between the density | concentration of trichlorethylene in Example 4, and elapsed time. It is a figure which shows the relationship between the density | concentration of trichlorethylene in each molar ratio of caustic soda with respect to sodium persulfate, and elapsed time.

Explanation of symbols

  1 to 3 purification devices, 10 persulfate storage tank, 12 first pump, 14 persulfate injection line, 16 injection well, 18 alkaline agent storage tank, 20 second pump, 22 alkaline agent injection line, 24 pumping pump, 26 pumping water Line, 28 Pumping well, 30 Aeration tank, 32 Aeration treated water line, 34 Observation well.

Claims (2)

The soil and ground water contaminated with organic chlorine compounds from the injection wells by adding persulfate and sodium hydroxide to the original position to a method for purifying an organic chlorine compounds pollution to clean the soil and ground water,
The persulfate is added so that the persulfate concentration in the reaction region is 5000 mg / L or more, and at the same time, the final pH of the reaction region is 5 or more and 10 to 10 within a range in which the time required for the decomposition of the organic chlorine compound is not prolonged. A method for purifying organochlorine compound contamination, wherein the caustic soda is added in a molar ratio of 0.4 to 2.0 in a range of less than or equal to the persulfate so as to be less than the range. A claim 1 purification method of the organic chlorine compounds pollution, wherein the potassium persulfate persulfate, purification method of the organic chlorine compounds pollution, which is a sodium persulfate or ammonium persulfate.

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