CA2590990A1 - In-situ salt remediation and ground heating technology - Google Patents
In-situ salt remediation and ground heating technology Download PDFInfo
- Publication number
- CA2590990A1 CA2590990A1 CA002590990A CA2590990A CA2590990A1 CA 2590990 A1 CA2590990 A1 CA 2590990A1 CA 002590990 A CA002590990 A CA 002590990A CA 2590990 A CA2590990 A CA 2590990A CA 2590990 A1 CA2590990 A1 CA 2590990A1
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- bore hole
- well screen
- soil
- bore
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- 238000011065 in-situ storage Methods 0.000 title claims abstract description 15
- 238000005067 remediation Methods 0.000 title claims abstract description 13
- 150000003839 salts Chemical class 0.000 title claims description 8
- 238000010438 heat treatment Methods 0.000 title description 5
- 239000002689 soil Substances 0.000 claims abstract description 86
- 238000000034 method Methods 0.000 claims abstract description 63
- 239000000356 contaminant Substances 0.000 claims abstract description 52
- 239000013618 particulate matter Substances 0.000 claims abstract description 15
- 239000012530 fluid Substances 0.000 claims description 32
- 238000010926 purge Methods 0.000 claims description 10
- 230000035699 permeability Effects 0.000 claims description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 5
- 229910052799 carbon Inorganic materials 0.000 claims description 5
- 239000008187 granular material Substances 0.000 claims description 5
- 229930195733 hydrocarbon Natural products 0.000 claims description 5
- 238000001962 electrophoresis Methods 0.000 claims description 4
- 239000004215 Carbon black (E152) Substances 0.000 claims description 3
- 230000003247 decreasing effect Effects 0.000 claims 1
- 238000005370 electroosmosis Methods 0.000 claims 1
- 125000001183 hydrocarbyl group Chemical group 0.000 claims 1
- 239000002184 metal Substances 0.000 claims 1
- 238000005086 pumping Methods 0.000 claims 1
- 238000012856 packing Methods 0.000 abstract description 3
- 238000011109 contamination Methods 0.000 description 31
- 230000005684 electric field Effects 0.000 description 10
- 238000000605 extraction Methods 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 150000002500 ions Chemical class 0.000 description 7
- 229910001415 sodium ion Inorganic materials 0.000 description 7
- 239000011236 particulate material Substances 0.000 description 6
- 238000011282 treatment Methods 0.000 description 6
- 239000000460 chlorine Substances 0.000 description 5
- -1 chlorine ions Chemical class 0.000 description 5
- 239000004020 conductor Substances 0.000 description 5
- 238000011010 flushing procedure Methods 0.000 description 5
- 239000011148 porous material Substances 0.000 description 5
- 229910052801 chlorine Inorganic materials 0.000 description 4
- 150000002430 hydrocarbons Chemical class 0.000 description 4
- 150000001768 cations Chemical class 0.000 description 3
- 229910001385 heavy metal Inorganic materials 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 150000002894 organic compounds Chemical class 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 150000001450 anions Chemical class 0.000 description 2
- 239000003124 biologic agent Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 240000006829 Ficus sundaica Species 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000009412 basement excavation Methods 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09C—RECLAMATION OF CONTAMINATED SOIL
- B09C1/00—Reclamation of contaminated soil
- B09C1/08—Reclamation of contaminated soil chemically
- B09C1/085—Reclamation of contaminated soil chemically electrochemically, e.g. by electrokinetics
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09C—RECLAMATION OF CONTAMINATED SOIL
- B09C1/00—Reclamation of contaminated soil
- B09C1/06—Reclamation of contaminated soil thermally
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Soil Sciences (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
A method for in-situ soil remediation is provided. Electrodes are placed below the ground surface extending horizontally. The electrodes are positioned such that a first electrode is positioned above a second electrode and the electrodes surround a region of soil containing contaminants. A plurality of electrodes can be placed in an upper plane corresponding with a plurality of electrodes placed in a lower plane. By passing a current between the electrodes contaminants are mobilized towards the electrodes where the contaminants can be extracted. The electrodes are constructed by boring substantially horizontal bore holes, inserting a well screen in the bore hole and packing an annulus formed between the well screen and the bore hole with electrically conductive particulate matter.
Description
IN-SITU SALT REIEDIATION AND GROUND HEATING TECHNOLOGY
This invention is in the field of soil remediation and more particularly in-situ electrokinctic remediation.
BACKGROUND
Contamination of subsurface soils is a matter of great concem and can cause many environmental problems if left in the subsurface soil. This contamination of subsurface soil can occur in a number of ways, such as accidental spills, leaks from storage facilities or tanks (in the past, it was not uncommon for gasoline storage tanks under service stations to leak and contaminate the soil beneath the storage tanks), landfill seepage, etc.
Sometimes the contamination is a result of an industrial process or resource extraction.
In most circumstances it is desirable or even necessary to deal with the subsurface soil eontamination. Sometimes clean-up of the contamination is even required by regulation.
The most basic method of treating contaminated subsurface soil is also the most labor intensive; simply excavating the contaminated soil and hauling it off-site for disposal, such as by incineration. The problem with this method is that although it is straightforward and rather uncomplicated, it is very labor and resource intensive.
Because this method is so labor intensive and uneconomical in all but the rarest ( circumstances, there have been numerous attempts at developing in-situ soil rcmediation, where the contamination is addressed in the subsurface soil without having to make cxtensive excavations. Of these in-situ soil remediation methods, various methods have been tried or used such as injection teehniques, where chemicals or biological agents are injected in-situ in the soil to treat the contaminant within the subsurface soil.
One of the more popular in-situ soil remediation methods that is commonly used is soil vapor extrnction or SVE. SVE applies a vacuum to a well hole drilled vertically in to the contaminated subsurface soils. When the vacuum is applied, air is forced to travel through the pore spaces in the soil, eausing liquid in the soil to volatize and be carricd out. The air carrie.s the volatized contaminants and the volatized contaminants are removed from the well hole by the vacuum created. The extracted gases are then either vented to atmosphere or into a containment system for later trcatment.
However SVE works best in highly permeable soils because it allows a greater area around the well bore to be treated by the SVE. The more permeable the soil, ihe greater the area of surrounding soil that will allow volatized contaminants to be drawn out by the vacuum created in the well hole. The less permeable the soil, the smaller the area of subsurtacc soil around the well hole that will be treated by the SVE and the effectiveness of SVE methods will quickly diminish in less pcrmeable soils.
To increase the effectivene.cs of soil vapor extraction methods, a number of different methods have been tried and used to try to increase the effective range of these soil vapor extraction methods surrounding the down hole. Because of this requirement that the subsurface soil have relatively high permeability for SVE to be really effective, a number of methods and treatments have been used to try and increase the permeability of the soil surrounding the well hole. Some of these methods include: pneuinalic fracturing where air is forced down the well hole in pressure wavcs in an attempt to create fractures in the surrounding soil to increase the permeability of the soil; and heat treating methods to decrease the viscosity and increase the volatility of fluids in the soil.
In an effort to increase the effects of soil vapor extraction electric soil heating systenis have been tried. Soil heating imparts an electrical field across a contamination zone to caase contaminants to move towards the electrodes. However, previous attempts have not had very consistent or promising results.
SUMMARY OF THE INVENTION
It is an object of the present invention to overcome problems in the prior art.
In a first aspect, a method for in-situ soil remediation is provided. The method comprises: placing a first electrode below a ground surface, the first electrode extending substantially horizontally; placing a second electrode below the f~irst electrode, the sccond electrode extending substantially horizontally, soil between the first electrode and second electrode containing contaminants; and passing an electric current between the first electrode and second electrode through the soil between the first electrode and second electrode, using the first electrode and second electrode, the first electrode having opposite charge from the second electrode, to induce mobilization of contaminants in the soil bctween thc fust elcctrode and second electrode towards at lcast one of:
the first electrode and second electrode.
In a second aspect, a method for in-situ soil remediation is provided. The metbod comprises: horizontally boring a first bore hole below a ground surface, the first bore hole extending substantially horizontally; horizontally boring a second bore hole below the ficst bore hole, the second bore hole extending substantially parallel to the first bore liole, soil between the first bore hole and second bore liole containing contaminants;
inserting a first well screen in the first bore hole, a cross-sectional area of the first well screen being less than a cross-sectional area of the first bore hole;
inserting a second well screen in the second bore hole, a cross-sectional area of the second well screen being less than a cross-sectional area of the second bore hole; filling an annuls foi-med between the first well screen and the first bore hole with electrically conductive particulate matter to form a first electrode; filling an annuls formed between the second well screen and the fust bore hole with electrically conductive particulate matter to form a second electrode;
and passing an electric current between the fust electrode and second electrode through the soil between the first bore hole and second hole, the first electrode having opposite charge from the second electrode, to induce mobilization contaminants in the soil betw=een the first electrode and second electrcxle towards at least one of:
the First electrode and second electrode.
~
1n a third aspect, a method of constructing an electrode for electro-kinetic in-situ remediation of soil with an expanded cross-section is provided. The method comprises:
creating a bore hole through soil beneath a ground surface; inserting a well screen in the bore hole, the well screen having a cross-section that is less than a cross-scction of thc bore hole; and filling an annulus formed between the an outside surface of the well screen and an inner surface of the bore hole with a electrically-conductive granular material.
In a fourth aspect, a method of consttvcting an electrode for electro-kinetic in-situ remediation of soil with an expanded cross-section is provided. The method comprises:
creating a bore hole through soil beneath a ground surface; inserting a well screen in the bore hole, the well screen having a cross-section that is less than a cross-section of the bore hole; and filling an annulus formed between the an outside surface of the well screen and an inner surface of the bore hole with a electrically-conductive granular material.
The present invention. in one aspect, is a method of removing contaminatits from subsurface soil. A first set of horizontal bore holes are bored under a ground surface in subsurface soil, typically above a contamination zone. These bore holes will form a first set of horizontal bore holes located betieath the grnund surface and oriented in a first plane. Next, a sccond set of horizontal bore holes are bored under a ground subsurface and below the first set of horizontal bore holes. Typically, the second set of bore holes are located either partially through or entirely below the contamination zone so that at least a part of the contamination zone is situated between the first and second set of horizontal bore holes. The second set of horizontal bore holes are oriented in a second plane which is substantially parallel to the first plane containing the first set of horizontal bore holes.
Each of the bore holes are bored with a horizontal boring tool. When the horizontal boring tool reaches the surface at a far end of the bore hole, a well screen is attached to the end of the boring tool. When the horizontal boring tool is retracted back through the bore hole, the well screen is pulled back into the bore hole.
When each of the bore holes are drilled and a well screen is positioned in each of the bore holes, the annulus of each of the bore holes surrounding the well screen will be injected full of an electrically-conducting particulate matter, so that the entire well bore forms an electrode. Optionally, a conductor, such as a copper wire, is positioned running along the outside of the well screen and running the entire length of the well screen.
In this manner, if an air pocket occurs in the annulus of the well bore where no electrically-conducting particulate matter is present, an electrical current will be carried by the conductor across the air pocket to the electrically-conducting partieulate on the other side of the electrically-conducting particulate.
At this point, the first set of horizontal bore holes and the second set of horizontal bore holes are packed with an electrically-conducting particulate matter to form a number of relatively large upper and lower electrodes, respectively, running substantially horizontal under the ground surface in the subsurface soil with the upper electrodes ninning (o substantially parallel to thc lower clcctrodcs.
Next, a power delivery system is connected across the upper and lower electrodes, so that when a voltage is supplied across first and the second set of bore holes, an electrical field will be created between the upper and lower electrodes and through at least a portion of the contamination zone.
If the contanunant, in the contamination zone, is salt, heavy metals, radionuclides or organic compounds, ions present in the contamination zone will move, as a result of electromigration, towards the respective electrodes in an anode-cathodc reaction. For example, if the contaminant in the contamination zone is salt, sodium ions and chlorine ions are present in relatively large concxntrations in the contamination zone.
When a voltage is supplied to the electrodes and an electric field is created across the contamination zone, the sodium ions will migrate towards the cathode or negatively charged electrode and the chlorine ions will migrate towards the anode or the positively charged electrode.
This movement of ions to the electrodes (electromigration) causes the ions to concentrate around the electrodes. As a result of the voltage placed across the first and second set of horizontal bore holes, some of the ions will have moved towards the first and second set of horizontal bore holes and can more easily be removed from the subsurface soil in a number of ways. A vacuum system can be used to apply a vacuum to the well bores so that volatized liquid and gases can be removed from the bore hole.
Additionally or '7 altematively, a flushing system can be used that flushes out the horizontal bore holes with a non-contaminating purging fluid such as water.
The electromigration of the eontaminants towards the electrodes exterxls the range around the bore holes that can be treated by soil vapor extraction and/or fluid purging.
Fewer bore holes can be drilled and these bore holes placed further apart than they would have to be if electrokinetics was not used.
Because the electrode is formed by packing the annulus of the bore hoIe between the well screen and the bore of the hole with electrically-conductive particulate, such as granular carbon, the electrodes will be much larger than if steel rods or other conductive material alone were used for the electrode material.
In comparison to placing electrodes in the ground surface extending vertically down into the subsurface soil, by placing the electrodes horizontally a more uniform electrical field is created over the contamination zone and a larger area can be covered with less electrodes.
Alternatively, if the contaminant is not susceptible to an anode-cathode reaction, i.e. the contaminants will not be induced into electromigration, the same method can be uscxi to heat the subsurface soil and increase the viscosity of some contaminants, such as hydrocarbons. Typically, the voltage placed across the electrodes is increased. The electrical voltage is then used to heat the subsurface soil between the electrodes, which q will decrease the viscosity and/or increase the volatility of some types of contamiiiants.
The heated contaminants will then be more susceptible to removal using a vapor extraction system, a multiphase vapor extraction or pump and treat system.
DESCRIPT ION OF THE DRAWINGS
While the invention is claimed in the concluding portions hereof, preferred embodiments are provided in the accompanying detailed description which may be best understood in conjunction with the accompanying diagrams where like parts in each of the several diagrams are labeted with like numbers, and where:
Fig. 1 is a perspectivc sectional view of a fust set of horizontal bore holes and a second set of horizontal bore holes, in accordance with a first step of the present invention;
Fig. 2 is a side cross-sectional view of a horizontal bore hole being drilled and having a well screen positioned in the bore hole;
Fig. 3 is a side view of a well screen;
Fig. 4 is a side cross-section view of the bore holes of Fig. 2, wherein the anmduses of the bore holes are packed with an electrically-conductive granulate in accordance with the present invention;
Fig. 5 is a cross-sectional view of a bore hole comprising a well screen and an annulus packed with electrically conductive granulate;
Fig. 6 is a schcmatic illustration of a side cross-sectional view of the upper and lower electrode with the treatment system in place, in accordance with the present invention; and Fig. 7 is a cross-section of a bore hole containing a fluid conduit as part of a pneumatic air lift system.
DETAILED DESCRIPTION OF IHE ILLUSTRATED EMBODt1V>ENTS:
Fig. 1 illustrates a first step of a method for the treatment of contaminated subsurface soil, in accordance with the present invention. In this step, a first set of horizontal bore holes 10 and a second set of horizontal bore holes 20 are horizontally drilled using a horizontal boring tool 15. The first set of bore holes 10 are located beneath a ground surface 2 and oriented in a first horizontal plane. The second set of bore holes 20 are located below the first set of bore holes 10 in the subsurface soil and are oriented in a second planc. The sccond plane is substantially parallel to the first plane.
to The first set of horizontal bore holes 10 and the second set of horizontal bore holes 20 are preferably located above and below a contamination zone 50, containing the contaminated soil, respectively. Alternatively, if the contamination zone 50 is too large to be effectively treated in one treatment, the contamination zone 50 could be trEated in a number of stages by positioned the first set of borc holes 10 and the second set of bore holes 20 so that a fust portion of the contamination zone 50 is located between the first set of horizontal bore holes 10 and the second set of horizontal bore holes 20 and then additional horizontal bore holes drilled at a later time to address the rest of the contamination zone 50.
The first step of the method is to drill the first set of horizontal bore holes 10 and the second set of horizontal bore holes 20, using a horizontal boring tool 15, as is comrnonly known in the art.
Fig. 2 illustrates a second step of the method of the present invention, wherein a well screen 30 is placcd in each of the bore holes 5 in the fust set of bore holes 10 and the second set of bore holes 20. When the horizontal boring tool 15 has bored a horizontal bore hole 5 and has resurfaced at a far end of a field being treated, a well screen 30 is attached to the end of the boring tool 15. The boring tool 15 is then retracted back through the bore hole 5. As the boring tool 15 is rctracted back through the bore hole 5, the well screen 30 is dragged into place in the bore hole 5.
Fig. 3 illustrates a well screen 30. The well screen 30 is typically a PVC
pipc with perforations 32 located along the length of the well screen 30. Additionally, an electrical cortductor 34, such as a copper wire, is located running along the length of the well screen 30.
Referring again to Fig. 2, for each of the horizontal bores 5 in the first set of horizontal bore holes 10 and for each horizontal bores 5 in the second set of horizontal bore holes 20, when the boring tool 15 has resurfaced at the far side of the bore, a well scaeen 30 is attached to the end of the boring tool 15 and pullcd into the bore hole 30, when the boring tool 15 is retracted.
When all of the bore holes 5 in the first set of bore holes 10 and all of the bore holes 5 in the second set of bore holes 20 have been drilled and the boring tool 15 removed, each of the bore holes 5 will have a well screen 30 passing through the bore hole S.
Fig. 4 illustrates the next step of the method, wherein the annulus 40 of the bore holes 5 between the outer surface of the bore hole 5 and the well screen 30 is packed with an electrically-conducting particulate material 42, such as granular carbon. This electrically-conducting particulate material 42 is injected down the bore hole 5 into the annulus 30 of the borc hole 5.
Fig. 5 is a cross-section view of a bore hole 5 with the well screen 30 and annulus 40 packed with the electrically-conducing particulate material 42.
(2 Referring again to Fig. 4, packing the annulus 40 with electrically-conducting particulate material 42 allows the bore hole 5 to form an electrode.
Optionally, the electrical conductor 34 is used to carry an electrical chargc through the entire length of the well bore 5 in the event that an air pocket in the electrically-conducing particulate material 42 is present which might prevent the electrical charge from traveling the entire length of the well bore 5.
Fig. 6 illustrates the system set up for operation. All of the bore holes 5 in the first set of horizontal bore holes 10 and the bore holes 5 in the second set of horizontal bore holes 20 have a well screen 30 and electrieally-conductive particulate material 42 packed in the annulus 40 of the well bores 5, forming a set of uppcr electrodes 52 and lower electrodes 54, respectively.
A power delivery system 110 is connected across the upper electrodes 52 and lower electrodes 54. The power delivery system 110 supplies DC power across the elcctrodcs formed by the upper electrodes 52 and the lower electrodes 54, with the upper electrodes 52 being negatively charged and the lower electrodes 54 being positively charged, or vice versa. By placing a charge across the electrodes using the power delivery system 110, an electrical field is created through the contauunated zone 50.
If the contaminant is salt, heavy metals, radionuclides or organic compounds, these types of contaminants can be induced to move towards the first set of horizontal bore holcs 10 and the second set of horizontal bore holes 20 by imposing an electric field over the contamination zone 50. For example, when salt is the contamination material in the contamination zonc 50 both sodium ions (Na) and chlorine ions (Cl') will exist in solution in the ground water. Under the imposed electrical field, the sodium ions (Na+) migrate towards the cathode and the chloride ions (CI) migrate towards the anode. '1'he power delivery system 110 will be used to supply a current across the contamination zone 50 for a pcriod of time. The longer the period of time, the more sodium ions (Na+) and chlorine ions (CT) that will migrate through the contamination zone 50 towards the electrodes 52, 54.
There are thrcc phcnonmenon that allow for the mobilization of contamuiants in the soil:
electromoosis, electromigration and electrophoresis. Electromigration occurs when positively charged ions (cations) move toward the cathode (negative electrode) and negatively charged ions (anions) move toward the anode (positive electrode).
However, etectromosis and electrophoresis can also aid in removing contaminants froni a soil region. Electromosis occurs when water and contaminants move from the anode to the cathode. Clay soil typically has negative surface charge; there is typically more cations than anions in the pore water. These extra cations, lined up along the pore walls and moving towards the cathode, drag the pore water along causing a net pore water flow to the cathode_ This process can remove water from a section of soil and carry contaminants into an extraction area. Electrophoresis is the movement of particles or (y colloids under the influence of the electric field. If particles carry a net surface charge, they can be transported through the soil matrix by passing an electric current through the soil.
Altematively, if the contaminant in thc contamination zone 50 is not salt, a heavy metal, a radionuclide, organic compounds or other substance that will be induced into electromigration as a result of the electrical field, the system can also be used to heat up the contaminant in the contamination zone 50 to decrease the viscosity and/or increase the volatility of the contaminant. For example, hydrocarbons could be the contaminant and the electrical field is used to heat up the contamination zone 50. By heating the hydrocarbon in the contamination zone 50, the hydrocarbon can be more easily removed from the surrounding sub-surface soil using vapor extraL4ion and flushing methods, Next, a vacuum system 120 is used to extract volatized liquid from the bore holcs 5. The vacuum system 120 comprises a vacuum source used for vapor extraction such as a multi-phase vapor extraction system. The vacuum systeni 120 is u.sed to apply a vacuum to the bore hole 5. A vacuum source is applied to one end of each of the bore holes 5 to extract vapor from the bore holes 5. Vapor, including volatized contaminant and partially volatized contaminant from the hore hole 5 and sub-surface soil surrounding the bore hole 5, is extracted from the bore hole 5 as a result of the pressure differential created by the vacuum system 120.
~~
A pneumatic air lift system 130 is used to increase the ptessure differential created by the vacuum system 120 and extend the effective range of the vacuum system 120, allowing more volatized and partially volatized contaminants to be removed from the bore holes 5.
The pneumatic air lift system 130 comprises an air supply and a fluid conduit that runs through the bore holcs 5. Fig. 7 illustrates a cross-section of a bore hole S
with a fluid conduit 200 passing through it. The fluid conduit 200 has a plurality of reversing ports 210 located along the fluid conduit 200 at regular intervals. Pressurized air is forced through the fluid conduit 200 where it exits the reversing ports 210 forcing fluid in the bore hole 5 back towards the vacuum system 120.
Referring again to Fig. 6, a flushing system 140 can also or alternatively be used to flush contaminants out of the bore tiole 5 and the surrounding soil. Non-contaminating purging fluid, such as clean water is used to flush out the bore hole 5 (although the purging fluid can have chemicals or biological agents added to further act on the contaminants). The purging fluid is forced into the bore holes 5 and then eztracted to remove contaminant in the bore hole 5 or around the bore hole 5, from the surrounding subsurface soil.
The purging fluid can be temporarily stored onsite until it is removed for treatment at an offsite location to remove the contaminant in the used purging fluid, or alternatively, a descaler 150 or other water treatment system is provided. The recovered piuging fluid that is extracted from the bore holes 5 can be routed to the descaler 150 where the descaler 150 will clean a substantial portion of the contaminant from the water. The treated purging fluid can then be reused by the flushing system 140.
1 c.
Optionally, further systems can be incorporated to increase the permeability of the sub-surface soil, such as a pneumatic fracturing system 160. The pneumatic fracturing system 160 forces a burst of air down the bore holes 5 to create cracks in the subsurface soil surrounding the bore hoics 5. The fractures in the subsurface created by the pneumatic fracturing system 160 increase the permeability of the subsurface soil.
The power supply system 110. vacuum system 120 and flushing system 140 can be repeatedly used in stages with the system used in series one after another repeatedly, until a satisfactory amount of contaminants have been removed from the contamination zone 50.
Additionally, in some circumstances it may not be necessary or desirable to use the horizontal bore holes. Rather, more conventional vertical bore holes can be used with the conductive-material packed annulus in some circumstances.
The foregoing is considered as illustrativc only of the principles of the invention.
Further, since numerous changes and modifications will readily occur to those skilled in the art, it is not desired to limit the invention to the exact constniction and operation shown and described, and accordingly, all such suitable changes or modifications in structure or operation which may be resorted to are intended to fall within the scope of the claimed invention ~1
This invention is in the field of soil remediation and more particularly in-situ electrokinctic remediation.
BACKGROUND
Contamination of subsurface soils is a matter of great concem and can cause many environmental problems if left in the subsurface soil. This contamination of subsurface soil can occur in a number of ways, such as accidental spills, leaks from storage facilities or tanks (in the past, it was not uncommon for gasoline storage tanks under service stations to leak and contaminate the soil beneath the storage tanks), landfill seepage, etc.
Sometimes the contamination is a result of an industrial process or resource extraction.
In most circumstances it is desirable or even necessary to deal with the subsurface soil eontamination. Sometimes clean-up of the contamination is even required by regulation.
The most basic method of treating contaminated subsurface soil is also the most labor intensive; simply excavating the contaminated soil and hauling it off-site for disposal, such as by incineration. The problem with this method is that although it is straightforward and rather uncomplicated, it is very labor and resource intensive.
Because this method is so labor intensive and uneconomical in all but the rarest ( circumstances, there have been numerous attempts at developing in-situ soil rcmediation, where the contamination is addressed in the subsurface soil without having to make cxtensive excavations. Of these in-situ soil remediation methods, various methods have been tried or used such as injection teehniques, where chemicals or biological agents are injected in-situ in the soil to treat the contaminant within the subsurface soil.
One of the more popular in-situ soil remediation methods that is commonly used is soil vapor extrnction or SVE. SVE applies a vacuum to a well hole drilled vertically in to the contaminated subsurface soils. When the vacuum is applied, air is forced to travel through the pore spaces in the soil, eausing liquid in the soil to volatize and be carricd out. The air carrie.s the volatized contaminants and the volatized contaminants are removed from the well hole by the vacuum created. The extracted gases are then either vented to atmosphere or into a containment system for later trcatment.
However SVE works best in highly permeable soils because it allows a greater area around the well bore to be treated by the SVE. The more permeable the soil, ihe greater the area of surrounding soil that will allow volatized contaminants to be drawn out by the vacuum created in the well hole. The less permeable the soil, the smaller the area of subsurtacc soil around the well hole that will be treated by the SVE and the effectiveness of SVE methods will quickly diminish in less pcrmeable soils.
To increase the effectivene.cs of soil vapor extraction methods, a number of different methods have been tried and used to try to increase the effective range of these soil vapor extraction methods surrounding the down hole. Because of this requirement that the subsurface soil have relatively high permeability for SVE to be really effective, a number of methods and treatments have been used to try and increase the permeability of the soil surrounding the well hole. Some of these methods include: pneuinalic fracturing where air is forced down the well hole in pressure wavcs in an attempt to create fractures in the surrounding soil to increase the permeability of the soil; and heat treating methods to decrease the viscosity and increase the volatility of fluids in the soil.
In an effort to increase the effects of soil vapor extraction electric soil heating systenis have been tried. Soil heating imparts an electrical field across a contamination zone to caase contaminants to move towards the electrodes. However, previous attempts have not had very consistent or promising results.
SUMMARY OF THE INVENTION
It is an object of the present invention to overcome problems in the prior art.
In a first aspect, a method for in-situ soil remediation is provided. The method comprises: placing a first electrode below a ground surface, the first electrode extending substantially horizontally; placing a second electrode below the f~irst electrode, the sccond electrode extending substantially horizontally, soil between the first electrode and second electrode containing contaminants; and passing an electric current between the first electrode and second electrode through the soil between the first electrode and second electrode, using the first electrode and second electrode, the first electrode having opposite charge from the second electrode, to induce mobilization of contaminants in the soil bctween thc fust elcctrode and second electrode towards at lcast one of:
the first electrode and second electrode.
In a second aspect, a method for in-situ soil remediation is provided. The metbod comprises: horizontally boring a first bore hole below a ground surface, the first bore hole extending substantially horizontally; horizontally boring a second bore hole below the ficst bore hole, the second bore hole extending substantially parallel to the first bore liole, soil between the first bore hole and second bore liole containing contaminants;
inserting a first well screen in the first bore hole, a cross-sectional area of the first well screen being less than a cross-sectional area of the first bore hole;
inserting a second well screen in the second bore hole, a cross-sectional area of the second well screen being less than a cross-sectional area of the second bore hole; filling an annuls foi-med between the first well screen and the first bore hole with electrically conductive particulate matter to form a first electrode; filling an annuls formed between the second well screen and the fust bore hole with electrically conductive particulate matter to form a second electrode;
and passing an electric current between the fust electrode and second electrode through the soil between the first bore hole and second hole, the first electrode having opposite charge from the second electrode, to induce mobilization contaminants in the soil betw=een the first electrode and second electrcxle towards at least one of:
the First electrode and second electrode.
~
1n a third aspect, a method of constructing an electrode for electro-kinetic in-situ remediation of soil with an expanded cross-section is provided. The method comprises:
creating a bore hole through soil beneath a ground surface; inserting a well screen in the bore hole, the well screen having a cross-section that is less than a cross-scction of thc bore hole; and filling an annulus formed between the an outside surface of the well screen and an inner surface of the bore hole with a electrically-conductive granular material.
In a fourth aspect, a method of consttvcting an electrode for electro-kinetic in-situ remediation of soil with an expanded cross-section is provided. The method comprises:
creating a bore hole through soil beneath a ground surface; inserting a well screen in the bore hole, the well screen having a cross-section that is less than a cross-section of the bore hole; and filling an annulus formed between the an outside surface of the well screen and an inner surface of the bore hole with a electrically-conductive granular material.
The present invention. in one aspect, is a method of removing contaminatits from subsurface soil. A first set of horizontal bore holes are bored under a ground surface in subsurface soil, typically above a contamination zone. These bore holes will form a first set of horizontal bore holes located betieath the grnund surface and oriented in a first plane. Next, a sccond set of horizontal bore holes are bored under a ground subsurface and below the first set of horizontal bore holes. Typically, the second set of bore holes are located either partially through or entirely below the contamination zone so that at least a part of the contamination zone is situated between the first and second set of horizontal bore holes. The second set of horizontal bore holes are oriented in a second plane which is substantially parallel to the first plane containing the first set of horizontal bore holes.
Each of the bore holes are bored with a horizontal boring tool. When the horizontal boring tool reaches the surface at a far end of the bore hole, a well screen is attached to the end of the boring tool. When the horizontal boring tool is retracted back through the bore hole, the well screen is pulled back into the bore hole.
When each of the bore holes are drilled and a well screen is positioned in each of the bore holes, the annulus of each of the bore holes surrounding the well screen will be injected full of an electrically-conducting particulate matter, so that the entire well bore forms an electrode. Optionally, a conductor, such as a copper wire, is positioned running along the outside of the well screen and running the entire length of the well screen.
In this manner, if an air pocket occurs in the annulus of the well bore where no electrically-conducting particulate matter is present, an electrical current will be carried by the conductor across the air pocket to the electrically-conducting partieulate on the other side of the electrically-conducting particulate.
At this point, the first set of horizontal bore holes and the second set of horizontal bore holes are packed with an electrically-conducting particulate matter to form a number of relatively large upper and lower electrodes, respectively, running substantially horizontal under the ground surface in the subsurface soil with the upper electrodes ninning (o substantially parallel to thc lower clcctrodcs.
Next, a power delivery system is connected across the upper and lower electrodes, so that when a voltage is supplied across first and the second set of bore holes, an electrical field will be created between the upper and lower electrodes and through at least a portion of the contamination zone.
If the contanunant, in the contamination zone, is salt, heavy metals, radionuclides or organic compounds, ions present in the contamination zone will move, as a result of electromigration, towards the respective electrodes in an anode-cathodc reaction. For example, if the contaminant in the contamination zone is salt, sodium ions and chlorine ions are present in relatively large concxntrations in the contamination zone.
When a voltage is supplied to the electrodes and an electric field is created across the contamination zone, the sodium ions will migrate towards the cathode or negatively charged electrode and the chlorine ions will migrate towards the anode or the positively charged electrode.
This movement of ions to the electrodes (electromigration) causes the ions to concentrate around the electrodes. As a result of the voltage placed across the first and second set of horizontal bore holes, some of the ions will have moved towards the first and second set of horizontal bore holes and can more easily be removed from the subsurface soil in a number of ways. A vacuum system can be used to apply a vacuum to the well bores so that volatized liquid and gases can be removed from the bore hole.
Additionally or '7 altematively, a flushing system can be used that flushes out the horizontal bore holes with a non-contaminating purging fluid such as water.
The electromigration of the eontaminants towards the electrodes exterxls the range around the bore holes that can be treated by soil vapor extraction and/or fluid purging.
Fewer bore holes can be drilled and these bore holes placed further apart than they would have to be if electrokinetics was not used.
Because the electrode is formed by packing the annulus of the bore hoIe between the well screen and the bore of the hole with electrically-conductive particulate, such as granular carbon, the electrodes will be much larger than if steel rods or other conductive material alone were used for the electrode material.
In comparison to placing electrodes in the ground surface extending vertically down into the subsurface soil, by placing the electrodes horizontally a more uniform electrical field is created over the contamination zone and a larger area can be covered with less electrodes.
Alternatively, if the contaminant is not susceptible to an anode-cathode reaction, i.e. the contaminants will not be induced into electromigration, the same method can be uscxi to heat the subsurface soil and increase the viscosity of some contaminants, such as hydrocarbons. Typically, the voltage placed across the electrodes is increased. The electrical voltage is then used to heat the subsurface soil between the electrodes, which q will decrease the viscosity and/or increase the volatility of some types of contamiiiants.
The heated contaminants will then be more susceptible to removal using a vapor extraction system, a multiphase vapor extraction or pump and treat system.
DESCRIPT ION OF THE DRAWINGS
While the invention is claimed in the concluding portions hereof, preferred embodiments are provided in the accompanying detailed description which may be best understood in conjunction with the accompanying diagrams where like parts in each of the several diagrams are labeted with like numbers, and where:
Fig. 1 is a perspectivc sectional view of a fust set of horizontal bore holes and a second set of horizontal bore holes, in accordance with a first step of the present invention;
Fig. 2 is a side cross-sectional view of a horizontal bore hole being drilled and having a well screen positioned in the bore hole;
Fig. 3 is a side view of a well screen;
Fig. 4 is a side cross-section view of the bore holes of Fig. 2, wherein the anmduses of the bore holes are packed with an electrically-conductive granulate in accordance with the present invention;
Fig. 5 is a cross-sectional view of a bore hole comprising a well screen and an annulus packed with electrically conductive granulate;
Fig. 6 is a schcmatic illustration of a side cross-sectional view of the upper and lower electrode with the treatment system in place, in accordance with the present invention; and Fig. 7 is a cross-section of a bore hole containing a fluid conduit as part of a pneumatic air lift system.
DETAILED DESCRIPTION OF IHE ILLUSTRATED EMBODt1V>ENTS:
Fig. 1 illustrates a first step of a method for the treatment of contaminated subsurface soil, in accordance with the present invention. In this step, a first set of horizontal bore holes 10 and a second set of horizontal bore holes 20 are horizontally drilled using a horizontal boring tool 15. The first set of bore holes 10 are located beneath a ground surface 2 and oriented in a first horizontal plane. The second set of bore holes 20 are located below the first set of bore holes 10 in the subsurface soil and are oriented in a second planc. The sccond plane is substantially parallel to the first plane.
to The first set of horizontal bore holes 10 and the second set of horizontal bore holes 20 are preferably located above and below a contamination zone 50, containing the contaminated soil, respectively. Alternatively, if the contamination zone 50 is too large to be effectively treated in one treatment, the contamination zone 50 could be trEated in a number of stages by positioned the first set of borc holes 10 and the second set of bore holes 20 so that a fust portion of the contamination zone 50 is located between the first set of horizontal bore holes 10 and the second set of horizontal bore holes 20 and then additional horizontal bore holes drilled at a later time to address the rest of the contamination zone 50.
The first step of the method is to drill the first set of horizontal bore holes 10 and the second set of horizontal bore holes 20, using a horizontal boring tool 15, as is comrnonly known in the art.
Fig. 2 illustrates a second step of the method of the present invention, wherein a well screen 30 is placcd in each of the bore holes 5 in the fust set of bore holes 10 and the second set of bore holes 20. When the horizontal boring tool 15 has bored a horizontal bore hole 5 and has resurfaced at a far end of a field being treated, a well screen 30 is attached to the end of the boring tool 15. The boring tool 15 is then retracted back through the bore hole 5. As the boring tool 15 is rctracted back through the bore hole 5, the well screen 30 is dragged into place in the bore hole 5.
Fig. 3 illustrates a well screen 30. The well screen 30 is typically a PVC
pipc with perforations 32 located along the length of the well screen 30. Additionally, an electrical cortductor 34, such as a copper wire, is located running along the length of the well screen 30.
Referring again to Fig. 2, for each of the horizontal bores 5 in the first set of horizontal bore holes 10 and for each horizontal bores 5 in the second set of horizontal bore holes 20, when the boring tool 15 has resurfaced at the far side of the bore, a well scaeen 30 is attached to the end of the boring tool 15 and pullcd into the bore hole 30, when the boring tool 15 is retracted.
When all of the bore holes 5 in the first set of bore holes 10 and all of the bore holes 5 in the second set of bore holes 20 have been drilled and the boring tool 15 removed, each of the bore holes 5 will have a well screen 30 passing through the bore hole S.
Fig. 4 illustrates the next step of the method, wherein the annulus 40 of the bore holes 5 between the outer surface of the bore hole 5 and the well screen 30 is packed with an electrically-conducting particulate material 42, such as granular carbon. This electrically-conducting particulate material 42 is injected down the bore hole 5 into the annulus 30 of the borc hole 5.
Fig. 5 is a cross-section view of a bore hole 5 with the well screen 30 and annulus 40 packed with the electrically-conducing particulate material 42.
(2 Referring again to Fig. 4, packing the annulus 40 with electrically-conducting particulate material 42 allows the bore hole 5 to form an electrode.
Optionally, the electrical conductor 34 is used to carry an electrical chargc through the entire length of the well bore 5 in the event that an air pocket in the electrically-conducing particulate material 42 is present which might prevent the electrical charge from traveling the entire length of the well bore 5.
Fig. 6 illustrates the system set up for operation. All of the bore holes 5 in the first set of horizontal bore holes 10 and the bore holes 5 in the second set of horizontal bore holes 20 have a well screen 30 and electrieally-conductive particulate material 42 packed in the annulus 40 of the well bores 5, forming a set of uppcr electrodes 52 and lower electrodes 54, respectively.
A power delivery system 110 is connected across the upper electrodes 52 and lower electrodes 54. The power delivery system 110 supplies DC power across the elcctrodcs formed by the upper electrodes 52 and the lower electrodes 54, with the upper electrodes 52 being negatively charged and the lower electrodes 54 being positively charged, or vice versa. By placing a charge across the electrodes using the power delivery system 110, an electrical field is created through the contauunated zone 50.
If the contaminant is salt, heavy metals, radionuclides or organic compounds, these types of contaminants can be induced to move towards the first set of horizontal bore holcs 10 and the second set of horizontal bore holes 20 by imposing an electric field over the contamination zone 50. For example, when salt is the contamination material in the contamination zonc 50 both sodium ions (Na) and chlorine ions (Cl') will exist in solution in the ground water. Under the imposed electrical field, the sodium ions (Na+) migrate towards the cathode and the chloride ions (CI) migrate towards the anode. '1'he power delivery system 110 will be used to supply a current across the contamination zone 50 for a pcriod of time. The longer the period of time, the more sodium ions (Na+) and chlorine ions (CT) that will migrate through the contamination zone 50 towards the electrodes 52, 54.
There are thrcc phcnonmenon that allow for the mobilization of contamuiants in the soil:
electromoosis, electromigration and electrophoresis. Electromigration occurs when positively charged ions (cations) move toward the cathode (negative electrode) and negatively charged ions (anions) move toward the anode (positive electrode).
However, etectromosis and electrophoresis can also aid in removing contaminants froni a soil region. Electromosis occurs when water and contaminants move from the anode to the cathode. Clay soil typically has negative surface charge; there is typically more cations than anions in the pore water. These extra cations, lined up along the pore walls and moving towards the cathode, drag the pore water along causing a net pore water flow to the cathode_ This process can remove water from a section of soil and carry contaminants into an extraction area. Electrophoresis is the movement of particles or (y colloids under the influence of the electric field. If particles carry a net surface charge, they can be transported through the soil matrix by passing an electric current through the soil.
Altematively, if the contaminant in thc contamination zone 50 is not salt, a heavy metal, a radionuclide, organic compounds or other substance that will be induced into electromigration as a result of the electrical field, the system can also be used to heat up the contaminant in the contamination zone 50 to decrease the viscosity and/or increase the volatility of the contaminant. For example, hydrocarbons could be the contaminant and the electrical field is used to heat up the contamination zone 50. By heating the hydrocarbon in the contamination zone 50, the hydrocarbon can be more easily removed from the surrounding sub-surface soil using vapor extraL4ion and flushing methods, Next, a vacuum system 120 is used to extract volatized liquid from the bore holcs 5. The vacuum system 120 comprises a vacuum source used for vapor extraction such as a multi-phase vapor extraction system. The vacuum systeni 120 is u.sed to apply a vacuum to the bore hole 5. A vacuum source is applied to one end of each of the bore holes 5 to extract vapor from the bore holes 5. Vapor, including volatized contaminant and partially volatized contaminant from the hore hole 5 and sub-surface soil surrounding the bore hole 5, is extracted from the bore hole 5 as a result of the pressure differential created by the vacuum system 120.
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A pneumatic air lift system 130 is used to increase the ptessure differential created by the vacuum system 120 and extend the effective range of the vacuum system 120, allowing more volatized and partially volatized contaminants to be removed from the bore holes 5.
The pneumatic air lift system 130 comprises an air supply and a fluid conduit that runs through the bore holcs 5. Fig. 7 illustrates a cross-section of a bore hole S
with a fluid conduit 200 passing through it. The fluid conduit 200 has a plurality of reversing ports 210 located along the fluid conduit 200 at regular intervals. Pressurized air is forced through the fluid conduit 200 where it exits the reversing ports 210 forcing fluid in the bore hole 5 back towards the vacuum system 120.
Referring again to Fig. 6, a flushing system 140 can also or alternatively be used to flush contaminants out of the bore tiole 5 and the surrounding soil. Non-contaminating purging fluid, such as clean water is used to flush out the bore hole 5 (although the purging fluid can have chemicals or biological agents added to further act on the contaminants). The purging fluid is forced into the bore holes 5 and then eztracted to remove contaminant in the bore hole 5 or around the bore hole 5, from the surrounding subsurface soil.
The purging fluid can be temporarily stored onsite until it is removed for treatment at an offsite location to remove the contaminant in the used purging fluid, or alternatively, a descaler 150 or other water treatment system is provided. The recovered piuging fluid that is extracted from the bore holes 5 can be routed to the descaler 150 where the descaler 150 will clean a substantial portion of the contaminant from the water. The treated purging fluid can then be reused by the flushing system 140.
1 c.
Optionally, further systems can be incorporated to increase the permeability of the sub-surface soil, such as a pneumatic fracturing system 160. The pneumatic fracturing system 160 forces a burst of air down the bore holes 5 to create cracks in the subsurface soil surrounding the bore hoics 5. The fractures in the subsurface created by the pneumatic fracturing system 160 increase the permeability of the subsurface soil.
The power supply system 110. vacuum system 120 and flushing system 140 can be repeatedly used in stages with the system used in series one after another repeatedly, until a satisfactory amount of contaminants have been removed from the contamination zone 50.
Additionally, in some circumstances it may not be necessary or desirable to use the horizontal bore holes. Rather, more conventional vertical bore holes can be used with the conductive-material packed annulus in some circumstances.
The foregoing is considered as illustrativc only of the principles of the invention.
Further, since numerous changes and modifications will readily occur to those skilled in the art, it is not desired to limit the invention to the exact constniction and operation shown and described, and accordingly, all such suitable changes or modifications in structure or operation which may be resorted to are intended to fall within the scope of the claimed invention ~1
Claims (32)
We claim:
1. A method for in-situ soil remediation, the method comprising:
placing a first electrode below a ground surface, the first electrode extending substantially horizontally;
placing a second electrode below the first electrode, the second electrode extending substantially horizontally, soil between the first electrode and second electrode containing contaminants; and passing an electric current between the first electrode and second electrode through the soil between the first electrode and second electrode, using the first electrode and second electrode, the first electrode having opposite charge from the second electrode, to induce mobilization of contaminants in the soil between the first electrode and second electrode towards at least one of: the first electrode and second electrode.
placing a first electrode below a ground surface, the first electrode extending substantially horizontally;
placing a second electrode below the first electrode, the second electrode extending substantially horizontally, soil between the first electrode and second electrode containing contaminants; and passing an electric current between the first electrode and second electrode through the soil between the first electrode and second electrode, using the first electrode and second electrode, the first electrode having opposite charge from the second electrode, to induce mobilization of contaminants in the soil between the first electrode and second electrode towards at least one of: the first electrode and second electrode.
2. The method of claim 1 wherein the second electrode extends substantially parallel to the first electrode.
3. The method of claim 2 wherein the first electrode is one of a first set of electrodes positioned in a first plane oriented substantially horizontally below the ground surface and the second electrode is one of a second set of electrodes positioned in a second plane oriented substantially horizontal and below and substantially parallel to the first plane.
4. The method of claim 2 wherein first electrode and second electrode are positioned under the ground surface by boring a first bore hole and positioning the first electrode in the first horizontal bore hole and boring a second horizontal bore hole below the first bore hole and positioning the second electrode in the second bore hole.
5. The method of claim 4 wherein the first electrode and second electrode are formed by inserting electrically conductive particulate matter in the first bore to form the first electrode and inserting electrically conductive particulate matter in the second bore hole to form the second electrode.
6. The method of claim 5 wherein the electrically conductive particulate matter is granular carbon.
7. The method of claim 4 wherein the first electrode is positioned in the first horizontal bore hole by placing a permeable first well screen in the first bore hole, a cross-sectional area of the first well screen being less than a cross-sectional area of the first bore hole, and filling an annuls formed between the first well screen and the first bore hole with electrically conductive particulate matter to form the first electrode and the second electrode is positioned in the second horizontal bore hole by placing a permeable second well screen in the second bore hole, a cross-sectional area of the second well screen being less than a cross-sectional area of the second bore hole, and filling an annuls formed between the second well screen and the first bore hole with electrically conductive particulate matter to form the second electrode.
8. The method of claim 7 wherein the first electrode is one of a first set of electrodes positioned in a first plane oriented substantially horizontally below the ground surface and the second electrode is one of a second set of electrodes positioned in a second plane oriented substantially horizontal and below and substantially parallel to the first plane.
9. The method of claim 7 wherein the first well screen and second well screen each comprise a PVC pipe containing a plurality of perforations.
10. The method of claim 7 wherein the first well screen and second well screen further comprise an electrical conductive wire running along an outside surface of the well screen.
11. The method of claim 7 wherein the electrically conductive particulate matter is granular carbon.
12. The method of claim 7 wherein the contaminants are mobilized towards at least one of: the first electrode; and the second electrode, by at least one of:
electroosmosis; electromigration; and electrophoresis.
electroosmosis; electromigration; and electrophoresis.
13. The method of claim 7 wherein the contaminant is salt and the electric current induces electromigration in the soil between the first electrode and the second electrode.
14. The method of claim 7 wherein the contaminant is a metal having an ionic charge and the electric current induces electromigration in the soil between the first electrode and second electrode.
15. The method of claim 7 wherein the contaminant is induced to mobilize by the electric current increasing the temperature of the soil, decreasing the viscosity of the contaminant.
16. The method of claim 15 wherein the contaminant is hydrocarbon.
17. The method of claim 7 further comprising extracting contaminants from the area surrounding the first electrode and the second electrode.
18. The method of claim 17 wherein contaminants are extracted from the area surrounding the first electrode and the second electrode by applying a vacuum source to a first end of the first bore hole and a fust end of the second bore hole to create a pressure differential between the first bore hole and the vacuum source and the second bore hole and the vacuum source, the pressure differential causing at least partially volatized contaminant from the first bore hole and second bore hole to move towards the vacuum source.
19. The method of claim 18 wherein the pressure differential between the vacuum source and the first and second bore hole is increased by increasing the pressure in the first bore hole and second bore hole.
20. The method of claim 19 wherein the pressure differential between the vacuum source and the first bore hole and the vacuum source and the second bore hole by placing a fluid conduit in each of the first bore hole and second bore hole, the fluid conduit having apertures passing out of the fluid conduit, and forcing pressurized fluid through the fluid conduit and out the apertures in the fluid conduit.
21. The method of 20 wherein the apertures in the fluid conduit arc directed down the first bore hole and second bore hole towards the vacuum source.
22. The method of claim 17 wherein contaminant surrounding the first electrode and second electrode is extracted by pumping purging fluid into the first bore hole and second bore hole and then removing the purging fluid along with contaminants from the first bore hole and second bore hole.
23. The method of claim 17 wherein pneumatic fracturing is used to increase the permeability of soil surrounding at least one of: the first bore hole and second bore hole.
24. A method for in-situ soil remediation, the method comprising:
horizontally boring a first bore hole below a ground surface, the first bore hole extending substantially horizontally;
horizontally boring a second bore hole below the first bore hole, the second bore hole extending substantially parallel to the first bore hole, soil between the first bore hole and second bore hole containing contaminants;
inserting a first well screen in the first bore hole, a cross-sectional area of the first well screen being less than a cross-sectional area of the first bore hole;
inserting a second well screen in the second bore hole, a cross-sectional area of the second well screen being less than a cross-sectional area of the second bore hole;
filling an annuls formed between the first well screen and the first bore hole with electrically conductive particulate matter to form a first electrode;
filling an annuls formed between the second well screen and the first bore hole with electrically conductive particulate matter to form a second electrode;
and passing an electric current between the first electrode and second electrode through the soil between the first bore hole and second hole, the first electrode having opposite charge from the second electrode, to induce mobilization contaminants in the soil between the first electrode and second electrode towards at least one of: the first electrode and second electrode.
horizontally boring a first bore hole below a ground surface, the first bore hole extending substantially horizontally;
horizontally boring a second bore hole below the first bore hole, the second bore hole extending substantially parallel to the first bore hole, soil between the first bore hole and second bore hole containing contaminants;
inserting a first well screen in the first bore hole, a cross-sectional area of the first well screen being less than a cross-sectional area of the first bore hole;
inserting a second well screen in the second bore hole, a cross-sectional area of the second well screen being less than a cross-sectional area of the second bore hole;
filling an annuls formed between the first well screen and the first bore hole with electrically conductive particulate matter to form a first electrode;
filling an annuls formed between the second well screen and the first bore hole with electrically conductive particulate matter to form a second electrode;
and passing an electric current between the first electrode and second electrode through the soil between the first bore hole and second hole, the first electrode having opposite charge from the second electrode, to induce mobilization contaminants in the soil between the first electrode and second electrode towards at least one of: the first electrode and second electrode.
25. The method of claim 24 wherein the first electrode is one of a first set of electrodes positioned in a first plane oriented substantially horizontally below the ground surface and the second electrode is one of a second set of electrodes positioned in a second plane oriented substantially horizontal and below and substantially parallel to the first plane.
26. A method of constructing an electrode for electro-kinetic in-situ remediation of soil with an expanded cross-section, the method comprising:
creating a bore hole through soil beneath a ground surface;
inserting a well screen in the bore hole, the well screen having a cross-section that is less than a cross-section of the bore hole; and filling an annulus formed between the an outside surface of the well screen and an inner surface of the bore hole with a electrically-conductive granular material.
creating a bore hole through soil beneath a ground surface;
inserting a well screen in the bore hole, the well screen having a cross-section that is less than a cross-section of the bore hole; and filling an annulus formed between the an outside surface of the well screen and an inner surface of the bore hole with a electrically-conductive granular material.
27. The method of claim 26 wherein the electrically conductive particulate matter is granular carbon.
28. The method of claim 26 further comprising running an electrically conductive wire along the outside surface of the well screen.
29. The method of claim 26 wherein the bore hole is oriented parallel to the ground surface.
30. The method of claim 26 wherein the bore hole is oriented perpendicular to the ground surface.
31. A method of extracting at least partially volatized contaminants from a bore hole, the method comprising:
inserting a fluid conduit into the bore hole, the fluid conduit having apertures passing out of the fluid conduit;
providing a vacuum source at a first end of the bore hole lo create a pressure differential between the vacuum source and an interior of a bore hole; and increasing the pressure differential by forcing pressurized fluid through the fluid conduit and out the apertures into the bore hole;
wherein the pressure differential moves at least partially volatized contaminants towards the vacuum source.
inserting a fluid conduit into the bore hole, the fluid conduit having apertures passing out of the fluid conduit;
providing a vacuum source at a first end of the bore hole lo create a pressure differential between the vacuum source and an interior of a bore hole; and increasing the pressure differential by forcing pressurized fluid through the fluid conduit and out the apertures into the bore hole;
wherein the pressure differential moves at least partially volatized contaminants towards the vacuum source.
32. The method of claim 31 wherein the apertures in the fluid conduit are directed towards the vacuum source.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA2590990A CA2590990C (en) | 2006-05-31 | 2007-05-31 | In-situ salt remediation and ground heating technology |
| CA2893882A CA2893882C (en) | 2006-05-31 | 2007-05-31 | In-situ salt remediation and ground heating technology |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA2,549,198 | 2006-05-31 | ||
| CA002549198A CA2549198A1 (en) | 2006-05-31 | 2006-05-31 | In-situ salt remediation and ground heating technology |
| CA2590990A CA2590990C (en) | 2006-05-31 | 2007-05-31 | In-situ salt remediation and ground heating technology |
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| CA2590990A Active CA2590990C (en) | 2006-05-31 | 2007-05-31 | In-situ salt remediation and ground heating technology |
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| US9428408B2 (en) | 2013-10-07 | 2016-08-30 | Dpra Canada Incorporated | Method and apparatus for treating tailings using an AC voltage with a DC offset |
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| US9896356B2 (en) | 2011-04-07 | 2018-02-20 | Electro-Kinetic Solutions Inc. | Electrokinetic process for consolidation of oil sands tailings |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108906851A (en) * | 2018-07-09 | 2018-11-30 | 北京中岩大地科技股份有限公司 | A kind of high-moisture low-permeability waste residue removes saline and alkaline dehydration combined governance method |
| CN108906852B (en) * | 2018-07-09 | 2021-07-06 | 北京中岩大地科技股份有限公司 | Method for removing salt and alkali from low-permeability salt-containing alkali waste residue |
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- 2007-05-31 CA CA2893882A patent/CA2893882C/en active Active
- 2007-05-31 CA CA2590990A patent/CA2590990C/en active Active
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9896356B2 (en) | 2011-04-07 | 2018-02-20 | Electro-Kinetic Solutions Inc. | Electrokinetic process for consolidation of oil sands tailings |
| US9428408B2 (en) | 2013-10-07 | 2016-08-30 | Dpra Canada Incorporated | Method and apparatus for treating tailings using an AC voltage with a DC offset |
| CN107211612A (en) * | 2017-06-29 | 2017-09-29 | 天津大学 | Modified saline land greening drives salt method with low-voltage DC |
Also Published As
| Publication number | Publication date |
|---|---|
| CA2590990C (en) | 2015-10-06 |
| CA2893882C (en) | 2018-02-27 |
| CA2893882A1 (en) | 2007-11-30 |
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