METHOD AND SYSTEM FOR THE IN-SITU DECONTAMINATION OF CONTAMINATED SOILS

Abstract

A method and an associated system for in-situ decontamination of a contaminated soil region (2) which contains degradable pollutants, in which a fluid substance is introduced into the soil (1) using an injection device (4, 4), wherein the fluid substance is introduced into the soil using a pressure injection method in a pressure-controlled manner and/or with an injection device that has a valve pipe with a pressure-controlled outlet valve.

Claims

1. (canceled)

2. The method as claimed in claim 18, wherein said injecting comprises repeated injections of the fluid substance into at least the contaminated soil region.

3. (canceled)

4. The method as claimed in claim 20, further comprising: producing the fluid substance by mixing at least two components.

5. The method as claimed in claim 4, wherein the at least two components are mixed at a soil depth between the upper and the lower axial boundaries.

6. (canceled)

7. The method as claimed in claim 18, wherein at least one of the two components contains permanganate.

8. The method as claimed in claim 4, wherein at least one of the two components contains potassium permanganate.

9. The method as claimed in claim 4, wherein the fluid substance is a mixture of two components forming Fenton's reagent.

10. (canceled)

11. (canceled)

12. The system as claimed in claim 21, wherein the injection line comprises a valve pipe, and the valve pipe further comprises a sleeve pipe having at least one sleeve valve.

13. The system as claimed in claim 24, further comprising: a mixing device configured to produce the fluid substance by mixing at least two components.

14. The system as claimed in claim 13, wherein the mixing device is arranged at the depth of the soil of the contaminated soil region.

15. The system as claimed in claim 13, wherein the mixing device is arranged in an interior of the valve pipe.

16. (canceled)

17. The system as claimed in claim 21, wherein an outer wall of the valve pipe comprises radially protruding horizontal bars configured to direct the fluid substance into the contaminated soil region radially away from the valve pipe.

18. A method for in-situ decontamination of a contaminated soil region which contains pollutants degradable with a decontaminating fluid substance through chemical oxidation, comprising: selecting an injection pressure from a plurality of available injection pressures, introducing a first component of the fluid substance via a first conduit to a depth horizon of the contaminated soil region, introducing a second component of the fluid substance via a second conduit segregated from the first conduit to the depth horizon of the contaminated soil region, mixing the introduced first component and the introduced second component at the depth horizon to produce the decontaminating fluid substance, and injecting the decontaminating fluid substance at the selected pressure from at least one outlet valve into at least the contaminated soil region.

19. A method for in-situ decontamination of a contaminated soil region which contains pollutants degradable with a decontaminating fluid substance through chemical oxidation, comprising: selecting an injection pressure from a plurality of available injection pressures, selecting from among a plurality of available upper and lower axial boundaries constraining propagation elevations for the decontaminating fluid substance, and injecting the decontaminating fluid substance at the selected pressure and within the selected boundaries from at least one outlet valve into at least the contaminated soil region, wherein the axial boundaries each extend radially outward and at least partly around the outer valve.

20. The method as claimed in claim 19, wherein the axial boundaries each extend radially outward and at least partly around the outlet valve

21. A system for in-situ decontamination of a contaminated soil region which contains degradable pollutants, comprising: a source configured to provide a first component of a decontaminating fluid substance and a second component of the fluid substance segregated from the first component, an outlet valve arranged at a depth of the contaminated soil region in the soil, an injection line extending between the source and the outlet valve, a pump arranged in the injection line, and a mixing device arranged in the injection line between the pump and the outlet valve, and configured to mix the first component and the second component, wherein the injection line comprises a superterranean portion and a subterranean portion, and wherein the mixing device is arranged in the subterranean portion of the injection line.

22. The system as claimed in 21, wherein the mixing device is arranged at a depth in the soil corresponding at least substantially to a depth in the soil of the outlet valve.

23. The system as claimed in claim 21, wherein the injection line comprises a valve pipe, and further comprising obstructions extending radially from the valve pipe towards the contaminated soil region and configured to delimit a propagation direction of the decontaminating fluid substance in the soil.

24. A system for in-situ decontamination of a contaminated region which contains degradable pollutants in a soil, comprising: a source configured to provide a decontaminating fluid substance, an outlet valve arranged at a depth in the soil of the contaminated soil region, an injection line extending between the source and the outlet valve, a pump and a valve pipe arranged in the injection line, and obstructions extending radially from and at least partly circumferentially around the valve pipe towards the contaminated soil region, and configured to delimit propagation elevations of the decontaminating fluid substance to a depth range within the soil.

25. The system as claimed in claim 24, wherein the obstructions extend fully circumferentially around the valve pipe.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0019] The invention will be described in more detail hereinafter with the aid of the figures. In the figures:

[0020] FIG. 1 shows a schematic illustration of a system for in-situ chemical oxidation using a valve pipe introduced into the soil, in a first embodiment;

[0021] FIG. 2 shows a schematic illustration of a system for in-situ chemical oxidation in a second embodiment; and

[0022] FIG. 3 shows a detailed illustration of a section of the valve pipe from FIG. 1.

[0023] In the drawings, elements which correspond to each other are designated with the same reference numerals. The drawings illustrate a schematic exemplified embodiment and do not reproduce any specific parameters of the invention. Furthermore, the drawings are merely used to explain an advantageous embodiment of the invention and are not to be interpreted as limiting the scope of protection of the invention.

DETAILED DESCRIPTION

[0024] FIG. 1 shows a system 3 for injecting, in a pressure-controlled manner, an oxidant in a soil 1 which includes a contaminated soil region 2 to be treated. The impurities in the soil region 2 consist at least in part of pollutants which can be treated using in-situ chemical oxidation.

[0025] The oxidant is injected in a pressure-controlled manner using an injection device 4 having a valve pipe 5 which is introduced into the soil 1 and includes at least one outlet valve 7 which is controlled with pressure. In the present exemplified embodiment, the valve pipe 5 is designed as a sleeve pipe 9. The sleeve pipe 9 (see detailed illustration in FIG. 3) is a hollow body consisting of synthetic material or steel and provided with openings 21 in one (or more) outlet region(s) 30. In the present exemplified embodiment, the sleeve pipe 9 includes a single outlet region 30, the lateral extent and position of which on the sleeve pipe 9 is adapted to the geometric shape of the soil region 2 to be treated. The openings 31 are covered with a sleeve 32, e.g. a rubber sleeve, which expands upon reaching a predetermined injection pressure, thus permitting the oxidant introduced through the sleeve pipe 9 to exit through the openings 31 into the surrounding area. The openings 31 and the sleeve 32 thus together form a sleeve valve 10 which can be opened and closed in a pressure-controlled manner. By using such a sleeve valve 10, the oxidant can be injected in a pressure-controlled manner at injection pressures of up to 15 to 30 bar depending upon the design of the sleeve 32. If a plurality of soil regions 2 at different depths are to be treated using in-situ chemical oxidation, then the sleeve pipe 9 expediently comprises a plurality of axially spaced apart sleeve valves 10 which are arranged on the sleeve pipe 9 in a manner that corresponds to the specific application to which the injection device 4 is being put.

[0026] The oxidant is conveyed into an interior 8 of the sleeve pipe 9 via an injection line 15. The injection line 15 is closed at its end 18 introduced into the soil 1 and comprises an injection region 16 having openings 17, via which the oxidant is introduced into the outlet region 30 of the sleeve pipe 9. In order to ensure that the desired injection pressure builds up in the outlet region 30 of the sleeve pipe 9, the interior 8 of the sleeve pipe 9 is provided with a so-called double packer 33 which includes two sealing sleeves 34 which expand in a controlled manner and surround the injection line 15 annularly, wherein sealing sleeves 34 are arranged respectively below and above the outlet region 30. In the active state, these sealing sleeves 34 terminate the outlet region 30 at the bottom and at the top and prevent the oxidant from axially escaping from the outlet region 30. After the oxidant has been injected, the expansion of the sealing sleeves 34 of the double packer 33 can be reversed by pressure relief. The double packer 33 can then be displaced within the valve pipe 5 so thatwhen a plurality of sleeve valves 10 are utilizedthe injection can be controlled and repeated as often as necessary in different regions.

[0027] The sealing sleeves 34 can be expanded in particular in a hydraulic manner. For instance, an expansion tube (not shown in FIG. 3) is connected to the sealing sleeves 34 and is used to supply a hydraulic medium. Alternatively, sealing sleeves 34 which are actuated in a pneumatic, electric or mechanical manner can also be provided.

[0028] In order to prepare for the soil treatment using in-situ chemical oxidation, in a first step a hole 20 having a depth which reaches at least as far as the soil region 2 to be treated is produced by pile driving, vibrating or boring in the soil 1. The sleeve pipe 9 is then introduced into this hole 20, which typically has a diameter of 80 to 150 mm, to such a depth that the outlet region 30 of the sleeve valve 10 is located in the soil region 2 to be treated. The annular space formed between an inner wall of the hole 20 and an outer wall 12 of the sleeve pipe 9 is then filled with a hardenable sheathing compound consisting of e.g. water, cement and bentonite. After hardening of the sheathing compound, this forms a casing 21 around the sleeve pipe 9 which fixes the sleeve pipe 9 in position.

[0029] The oxidant can now be injected into the soil region 2. For this purpose, the double packer 33 and the injection line 15 are inserted into the sleeve pipe 9 to such a depth that the double packer 33 and the injection region 16 of the injection line 15 lie opposite the sleeve valve 10 of the sleeve pipe 9 (see FIG. 3). In this position, the sealing sleeves 34 are now clamped, whereby the sealing pipe 9 is sealed at the top and bottom in the region of the double packer 33. Then, the oxidant is injected through the injection line 15 using a high-pressure pump 14, more particularly a high-pressure piston pump. The pressure in the annular space formed between the sealing sleeves 34 increases until the sheathing material of the casing 21 breaks open upon reaching the injection pressure in the outlet region 30 of the sleeve pipe 9 and the oxidant is injected into the surrounding soil 2 at high pressure through the perforation 31 in the sleeve pipe 9 (arrow 36). Therefore, the oxidant is injected in a pressure-controlled manner. In order to ensure that the oxidant is injected in the horizontal direction into the soil region 2 to be treated, the outer wall 12 of the valve pipe 5 can be provided, below and above the outlet region 30, with radially protruding, preferably annular horizontal bars 13. These horizontal bars 13 concentrate the flow of oxidant in the radial direction and ensure precise placement of the oxidant in the soil region 2 to be treated.

[0030] In order to treat laterally extended soil regions 2, it is expedient to introduce a plurality of laterally mutually offset valve pipes 5 into the soil 1, whereby the arrangement of the valve pipes is adapted to the outline of the distribution of the pollutants in the soil region 2. The distance between the valve pipes 5 is dependent upon the permeability of the soil 2 to be treated and the type and properties of the oxidant. The pressure building up during the injection process is an important indication for the propagation of the oxidant in the soil 2 and is thus continuously monitored during the injection process.

[0031] Different fluids which are produced by mixing a plurality of components can be used as the oxidant. The term fluid is intended to mean a flowable substance, in particular a supercritical fluid, a liquid or a liquid mixture, e.g. an emulsion, a solution or a liquid provided with solids. The oxidant must be selected such that it is suitable for degrading the pollutants contained in the soil region 2 and is adapted to the geochemical conditions.

[0032] In the exemplified embodiment in FIG. 1, a permanganate, in particular potassium permanganate, with water is used as the oxidant. Generally speaking, some of the substances used as starting materials for producing the oxidant are explosive, combustible and/or toxic substances and must therefore be stored physically separate from one another and in compliance with specific safety protocols. In the present exemplified embodiment, the starting materials permanganate and H.sub.2O are supplied to a central mixing device 6 via separate metering devices just before being introduced into the soil region 2. The oxidant is then prepared in this mixing device by mixing these two components. The mixture produced from the two components in the mixing device 6 is then fed directly to the high-pressure pump 14, which pumps the mixture into the injection line 15 under pressure.

[0033] The targeted and safe introduction of the oxidant into the subsoil is a formidable challenge. As already mentioned, common oxidants are highly reactive reagents and are thus hazardous substances. Therefore, depending upon the oxidant used, various technical and structural fire/explosion protection constraints imposed to ensure safe operation must be satisfied. This is achieved through various systems technologies that are provided with process-integrated technical safety measures, which, in turn, permit the systems to be used safely and which satisfy the various applicable safety requirements.

[0034] FIG. 2 shows an alternative embodiment of a system 3 for injecting an oxidant in a pressure-controlled manner into the contaminated soil region 2 which is to be treated using in-situ chemical oxidation, and is suitable in particular for cases in which a short-lived oxidant, more particularly Fenton's reagent, is to be used.

[0035] The oxidant Fenton's reagent is produced by activating H.sub.2O.sub.2 with Fe.sup.2+. Hydroxyl radicals having an extremely high redox potential are thereby produced. Concentrated H.sub.2O.sub.2 solutions are generally used as the starting product, and are activated by FeSO.sub.4 solutions. The hydroxyl radical is very unstable and breaks down quickly in the subsoil. When using the conventional injection processes, the radical can thus only be transported over short distances and has a small radius of action that extends over only a few meters.

[0036] By using the pressure-controlled injection in accordance with the invention, Fenton's reagent can be injected into the ground in surges at a higher pressure, whereby the area of action can be considerably increased. Furthermore, in the system 3 in FIG. 2in contrast to the exemplified embodiment in FIG. 1the individual components are mixed in a mixing device 6 which is arranged within the valve pipe 5, and therefore mixing does not occur until shortly before the expulsion of the oxidant into the soil 2. In this manner, the reaction time is utilized in an optimum manner because the oxidant is injected into the soil 2 straight after mixing.

[0037] As can be seen in FIG. 2, the starting substances for Fenton's reagent are stored in physically separate tanks 11a and 11b. The FeSO.sub.4 solution is fed from the tank 11a via a line 40a and a metering pump 41a into a first injection line 15a whereas the H.sub.2O.sub.2 solution is fed from the tank 11b via a line 40b and a metering pump 41b into a second injection line 15b. Flowmeters 42a, 42b are provided in the lines 40a, 40b and can control the supplied amounts. A high-pressure pump 14a, 14b is arranged in each of the injection lines 15a, 15b, and therefore the two components are compressed separately and are conveyed separated through the interior 8 of the sleeve pipe 9 to a mixing device 6, where they are mixed to produce Fenton's reagent and -similarly to the exemplified embodiment described in FIG. 1are injected into the soil 2 through the sleeve valve 10. The pressure and through-flow are measured using sensors 43a, 43b. Therefore, the mixing of the components FeSO.sub.4 and H.sub.2O.sub.2 to produce the oxidant Fenton's reagent takes place in this exemplified embodiment just before the injection into the soil 1 via the sleeve valve 10, and therefore the oxidant decomposes to only a minimal extent before the oxidant starts to act on the soil region 2. If need be, supply lines for further reagents (such as e.g. H.sub.2SO.sub.4) or purification media can be provided. The closed injection system is designed for a working pressure of at most 100 bar.

[0038] In addition to the features shown in the figures, the overall system 3, 3 of FIGS. 1 and 2 comprises a control unit (not shown in the figures) for in-process control, which controls, in a fully-automatic manner, the metering of the individual components, the mixing process, the charging of the pumps 14, 14a, 14b and the injection process on the basis of the measurement values from a multiplicity of sensors provided in the system (for pressure, through-flow amount, etc.). For instance, in particular the injection line 15, 15a, 15bas illustrated in FIG. 2is advantageously provided with sensors for pressure, through-flow, temperature and pH/redox potential values. During the injection process, the course of the injection is monitored in time and space, wherein the through-flow of the oxidant or the supplied components, the electrical conductivity and/or pH/redox potential are measured. Furthermore, preferably, the injection line can be flushed with osmosis water and the injection system has an exhaust system.

[0039] The systems 3 and 3 shown in FIGS. 1 to 3 for the pressure-controlled injection of an oxidant into a soil 1, which includes a contaminated soil region 2 to be treated, can likewise be used for the pressure-controlled injection of a culture medium for micro-organisms, as stated above.