WO2020005966A1 - Pfas remediation method and system - Google Patents

Pfas remediation method and system Download PDF

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Publication number
WO2020005966A1
WO2020005966A1 PCT/US2019/039020 US2019039020W WO2020005966A1 WO 2020005966 A1 WO2020005966 A1 WO 2020005966A1 US 2019039020 W US2019039020 W US 2019039020W WO 2020005966 A1 WO2020005966 A1 WO 2020005966A1
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WO
WIPO (PCT)
Prior art keywords
soil
pfas
temperature
degrees celsius
heating
Prior art date
Application number
PCT/US2019/039020
Other languages
French (fr)
Inventor
Daniel Oberle
Emily Crownover
Original Assignee
Trs Group, Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Trs Group, Inc. filed Critical Trs Group, Inc.
Priority to US16/452,141 priority Critical patent/US10675664B2/en
Priority claimed from US16/452,141 external-priority patent/US10675664B2/en
Publication of WO2020005966A1 publication Critical patent/WO2020005966A1/en
Priority to US16/864,889 priority patent/US20200260533A1/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09CRECLAMATION OF CONTAMINATED SOIL
    • B09C1/00Reclamation of contaminated soil
    • B09C1/06Reclamation of contaminated soil thermally

Definitions

  • the present disclosure relates to environmental remediation.
  • environmental remediation In particular, to removal of perfluoroalkyl and polyfluoroalkyl substances from soil.
  • PFAS per perfluoroalkyl and polyfluoroalkyl substances
  • PFAS compounds have been widely used in consumer products and industrial products and processes.
  • the PFAS characteristics that make them beneficial for these applications can also prevent them from readily degrading and challenging to remediate.
  • the unique characteristics of PFAS compounds render many remediation techniques that are effective on other contaminants ineffective to remediate PFAS compounds. Bioremediation is mostly ineffective for treating PFAS-contaminated soil. Additionally, limited success has been found by applying soil vapor extraction and other common hydrocarbon remediation techniques. Furthermore, it is generally accepted that very high temperatures, above 600 degrees Celsius for example, are necessary to effectively remediate PFAS compounds.
  • the disclosed methods and systems may be used to remediate soil containing
  • PFAS compounds and organic carbon include volatilizing these compounds from a soil matrix, which may contain relatively high concentrations of total organic carbon (TOC), or amounts generally found in United States soil, typically about .25% by weight.
  • Illustrative embodiments also include soil remediation in which the percent of TOCs is initially less than .25%. TOC is reduced by heating the soil at a sufficient temperature and for a sufficient duration to reduce surface effects between the PFAS compounds and the organic carbon to permit evaporation of the PFAS compounds from the soil.
  • TOC total organic carbon
  • soil is treated in-situ at a temperature in the range of above about 225 degrees Celsius and below about 440 degrees Celsius, and in a further illustrative embodiment at a temperature in the range of about 300 degrees Celsius to about 400 degrees Celsius.
  • the invention includes various combinations of temperature levels and duration of heating to remediate PFAS compounds.
  • the Figure is a flow chart of an illustrative PFAS remediation method.
  • a method of remediation of soil containing PFAS compounds is disclosed, and a system in which the method is implemented.
  • the Figure provides a flow chart of an illustrative PFAS remediation method. The method is carried out using thermal remediation techniques.
  • heater wells are installed.
  • step 104 total organic carbon (TOC) is reduced by heating the soil at a sufficient temperature and for a sufficient duration to reduce surface effects between the PFAS compounds and the organic carbon by breaking down the organic carbon.
  • the surface effects may be, for example, electrostatic forces and van der Walls forces. This permits evaporation of the PFAS compounds from the soil.
  • the soil is heated to reduce TOC to less than about 0.15% by weight.
  • soil is heated at a temperature and for a duration sufficient to reduce total organic carbon to less than about 0.10% by weight. In yet another embodiment soil is heated at a temperature and for a duration sufficient to reduce total organic carbon to less than about 0.05% by weight.
  • An illustrative range of TOC reduction is to about 0.01% to about 0.15%.
  • Temperature ranges for remediating PFAS compounds include, for example, about 225 degrees Celsius to below 440 degrees Celsius; about 300 degrees Celsius to about 400 degrees Celsius; about 320 degrees Celsius to about 380 degrees Celsius, and about 330 degrees Celsius to about 350 degrees Celsius.
  • Heating duration for remediating PFAS compounds include about one day to about 30 days, about five days to about 25 days, and about two days to about 10 days.
  • Heating may be performed by various thermal remediation techniques.
  • heating is performed by conductive heat transfer using heater wells installed into the soil.
  • One or more heater wells are installed to create a temperature gradient in the soil to establish conductive heat transfer through the soil from the heater wells. When the temperature of the heater well is higher than the surrounding soil, heat energy will flow to the soil. Details of an illustrative conductive heat transfer method and system are provided below.
  • heat is selectively modulated to balance the energy input to the system with heat losses, such as to the atmosphere.
  • the heat must also be regulated to sufficiently reduce TOC while maintaining temperatures at levels that will not damage the heater wells.
  • the timing and amount of heat transferred to the soil is regulated based on factors such as types and concentrations of PFAS compounds, for example. Accordingly, the temperature may be monitored throughout the soil matrix and also at the heater wells.
  • Heat sensors provide temperature level information, which can be accessed and monitored manually, or configured to provide input to the heater wells to increase or decrease power to the heater wells to regulate the temperature. .
  • evaporated PFAS compounds can be captured once released from the soil pursuant to the application of heat.
  • a vapor recovery system can be used to capture the evaporated PFAS.
  • PFAS can be removed from the vapor stream by cooling the vapor stream and condensing the PFAS.
  • 112 steam may be produced in the process or added to the process to allow for capture of the PFAS in a condensed and concentrated aqueous solution where the PFAS are then destroyed in a continuous process using electro-oxidation techniques such as advanced electrochemical oxidation or an electrical discharge plasma reactor as provided in step 114.
  • the combination of heating duration and temperature level can be adjusted for the particular PFAS being remediated.
  • Embodiments of the remediation method include the various combinations of any of the illustrative temperature ranges and time ranges.
  • the most common PFAS compounds perfluorooctanoic acid (PFOA) and perfluorooctane sulfonate (PFOS), may be remediated to concentrations of less than 1 microgram per kilogram by applying temperatures in the range of 350 to 400 degrees Celsius to the soil.
  • the method can be performed in-situ or soil can be removed and treated ex- situ.
  • heater wells are installed in in the soil to be remediated, distributed in an array according to factors, such as for example, contaminant concentration and location, soil characteristics and heater well characteristics.
  • Heater wells may be installed at regular intervals, or varying intervals depending, for example, on the necessary energy to be imparted into the soil and the temperatures needed to adequately remediate the contaminants ⁇
  • Heater wells generally comprise heating components or elements disposed within steel pipes. The heat may either move the contaminants in the soil toward the heater wells or destroy the contaminants in-situ.
  • PFAS compounds may be removed from the vapor stream by passing the heated vapors through a condensing system such as a heat exchanger or scrubber where the PFAS compounds are concentrated into an aqueous solution for treatment.
  • a flexible, generally, helical heater is implemented to uniquely achieve PFAS remediation in soils by effectively bringing the soil to the necessary temperature or temperatures.
  • the term“helical” or“helix” as used to describe the flexible heater shall include coils that are true helixes and those that are not necessarily a true mathematical helix.
  • the flexible helical heater includes an electrical resistance heating wire coiled about a current return wire that fits inside a small diameter metal casing.
  • the electrical resistance heating wire may be comprised, for example, of a nickel-chromium alloy such as NiChrome®, a copper-nickel alloy such as Cuprothal® or an iron-chromium- aluminum ferritic allow such as Kanthal®.
  • Heating soils to temperatures in the range of 225 to 440 degrees Celsius requires relatively tight spacing for heater wells, which may drive up the price and complexity of remediation.
  • the flexible helical heaters can fit into smaller diameter metal casings than traditional heaters, which may significantly reduce the cost and complexity of the PFAS remediation.
  • specific zones along the length of a heater well that contain more PFAS or TO than other zones are targeted with higher temperature by adjusting the coil spacing.
  • heat loss is compensated for by adjusting coil spacing to put more heat in at the top and bottom of a casing to compensate for heat loss.
  • PFAS remediation may be affected by site characteristics, types of PFAS compounds being remediated due to varying chemical and physical characteristics, source of the PFAS, whether there are multiple types of PFAS compounds, nature of the release pathways, the make-up of other contaminants and materials in the soil.
  • the disclosed remediation technique can take into consideration these variables and the number of carbon bonds and the alkyl functional group of the PFAS being remediated. In general, the larger the molecule, the higher the boiling point, but this general relationship can vary.
  • the disclosed methods may include combinations of the remediation techniques.
  • Various embodiments of the invention have been described, each having a different combination of elements. The invention is not limited to the specific embodiments disclosed, and may include different combinations of the elements disclosed, omission of some elements or the replacement of elements by the equivalents of such structures.

Abstract

A method and system to remediate soil containing PFAS compounds and organic carbon. Total organic carbon is reduced by heating the soil at a sufficient temperature and for a sufficient duration to reduce surface effects between the PFAS compounds and the organic carbon to permit evaporation and treatment of the PFAS compounds from the soil.

Description

PFAS REMEDIATION METHOD AND SYSTEM
FIELD
[0001] The present disclosure relates to environmental remediation. In particular, to removal of perfluoroalkyl and polyfluoroalkyl substances from soil.
BACKGROUND
[0002] Per perfluoroalkyl and polyfluoroalkyl substances (PFAS) are contaminants of concern. There are about 3,000 types of these compounds in the environment. They are soluble, highly resistant to biotic and abiotic degradation, and can withstand extremely high temperatures before breaking down.
[0003] PFAS compounds have been widely used in consumer products and industrial products and processes. The PFAS characteristics that make them beneficial for these applications can also prevent them from readily degrading and challenging to remediate. The unique characteristics of PFAS compounds render many remediation techniques that are effective on other contaminants ineffective to remediate PFAS compounds. Bioremediation is mostly ineffective for treating PFAS-contaminated soil. Additionally, limited success has been found by applying soil vapor extraction and other common hydrocarbon remediation techniques. Furthermore, it is generally accepted that very high temperatures, above 600 degrees Celsius for example, are necessary to effectively remediate PFAS compounds.
Although most PFAS compounds boil at temperatures in the range of 76 degrees Celsius to 218 degrees Celsius, there is very poor removal even at 225 degrees Celsius applied over multiple days.
[0004] Accordingly, there is a need for an effective PFAS remediation technique in soil.
SUMMARY
[0005] The disclosed methods and systems may be used to remediate soil containing
PFAS compounds and organic carbon. Illustrative embodiments include volatilizing these compounds from a soil matrix, which may contain relatively high concentrations of total organic carbon (TOC), or amounts generally found in United States soil, typically about .25% by weight. Illustrative embodiments also include soil remediation in which the percent of TOCs is initially less than .25%. TOC is reduced by heating the soil at a sufficient temperature and for a sufficient duration to reduce surface effects between the PFAS compounds and the organic carbon to permit evaporation of the PFAS compounds from the soil. In an illustrative embodiments soil is treated in-situ at a temperature in the range of above about 225 degrees Celsius and below about 440 degrees Celsius, and in a further illustrative embodiment at a temperature in the range of about 300 degrees Celsius to about 400 degrees Celsius. The invention includes various combinations of temperature levels and duration of heating to remediate PFAS compounds.
DESCRIPTION OF DRAWINGS
[0006] The detailed description refers to the accompanying Figure, which depicts an illustrative embodiment.
[0007] The Figure is a flow chart of an illustrative PFAS remediation method.
DETAILED DESCRIPTION OF EMBODIMENTS
[0008] The descriptions provided herein may have been simplified to illustrate aspects that are relevant for an understanding of the systems and methods described herein while eliminating, for the purpose of clarity, other aspects that may be found in typical systems and methods. Those of ordinary skill may recognize that other elements or operations may be desirable or necessary to implement the systems and methods described herein. Because such elements and operations are well known in the art, and because they do not facilitate a better understanding of the present disclosure, a discussion of such elements and operations may not be provided herein. This disclosure is deemed to inherently include all such elements, variations, and modifications to the described aspects that could be implemented by those of ordinary skill in the art.
[0009] A method of remediation of soil containing PFAS compounds is disclosed, and a system in which the method is implemented. The Figure provides a flow chart of an illustrative PFAS remediation method. The method is carried out using thermal remediation techniques. In step 102 heater wells are installed. In step 104 total organic carbon (TOC) is reduced by heating the soil at a sufficient temperature and for a sufficient duration to reduce surface effects between the PFAS compounds and the organic carbon by breaking down the organic carbon. The surface effects may be, for example, electrostatic forces and van der Walls forces. This permits evaporation of the PFAS compounds from the soil. In an illustrative embodiment, the soil is heated to reduce TOC to less than about 0.15% by weight. In a further embodiment, soil is heated at a temperature and for a duration sufficient to reduce total organic carbon to less than about 0.10% by weight. In yet another embodiment soil is heated at a temperature and for a duration sufficient to reduce total organic carbon to less than about 0.05% by weight. An illustrative range of TOC reduction is to about 0.01% to about 0.15%.
[00010] Temperature ranges for remediating PFAS compounds according to illustrative embodiments of the method include, for example, about 225 degrees Celsius to below 440 degrees Celsius; about 300 degrees Celsius to about 400 degrees Celsius; about 320 degrees Celsius to about 380 degrees Celsius, and about 330 degrees Celsius to about 350 degrees Celsius.
[00011] Heating duration for remediating PFAS compounds according to illustrative embodiments of the method include about one day to about 30 days, about five days to about 25 days, and about two days to about 10 days.
[00012] Heating may be performed by various thermal remediation techniques. In an illustrative embodiment, heating is performed by conductive heat transfer using heater wells installed into the soil. One or more heater wells are installed to create a temperature gradient in the soil to establish conductive heat transfer through the soil from the heater wells. When the temperature of the heater well is higher than the surrounding soil, heat energy will flow to the soil. Details of an illustrative conductive heat transfer method and system are provided below.
[00013] It has been accepted in the industry that conventional soil remediation heating techniques could not be applied because of the level of heat necessary to remediate PFAS compounds. Disclosed embodiments of PFAS remediation target the TOC reduction to more readily release the PFAS compounds from carbon compounds, thus facilitating use of various thermal remediation techniques.
[00014] Importantly, heat is selectively modulated to balance the energy input to the system with heat losses, such as to the atmosphere. The heat must also be regulated to sufficiently reduce TOC while maintaining temperatures at levels that will not damage the heater wells. The timing and amount of heat transferred to the soil is regulated based on factors such as types and concentrations of PFAS compounds, for example. Accordingly, the temperature may be monitored throughout the soil matrix and also at the heater wells.
Adjustments are made to balance the TOC reduction required with the temperature limits of the heater wells
[00015] Heat sensors provide temperature level information, which can be accessed and monitored manually, or configured to provide input to the heater wells to increase or decrease power to the heater wells to regulate the temperature. .
[00016] In step 106 evaporated PFAS compounds can be captured once released from the soil pursuant to the application of heat. For example, a vapor recovery system can be used to capture the evaporated PFAS. In step 108 PFAS can be removed from the vapor stream by cooling the vapor stream and condensing the PFAS. In steps 110, 112 steam may be produced in the process or added to the process to allow for capture of the PFAS in a condensed and concentrated aqueous solution where the PFAS are then destroyed in a continuous process using electro-oxidation techniques such as advanced electrochemical oxidation or an electrical discharge plasma reactor as provided in step 114.
[00017] The combination of heating duration and temperature level can be adjusted for the particular PFAS being remediated. Embodiments of the remediation method include the various combinations of any of the illustrative temperature ranges and time ranges. For example, the most common PFAS compounds, perfluorooctanoic acid (PFOA) and perfluorooctane sulfonate (PFOS), may be remediated to concentrations of less than 1 microgram per kilogram by applying temperatures in the range of 350 to 400 degrees Celsius to the soil.
[00018] The method can be performed in-situ or soil can be removed and treated ex- situ.
[00019] In an illustrative thermal conduction heating method, heater wells are installed in in the soil to be remediated, distributed in an array according to factors, such as for example, contaminant concentration and location, soil characteristics and heater well characteristics. Heater wells may be installed at regular intervals, or varying intervals depending, for example, on the necessary energy to be imparted into the soil and the temperatures needed to adequately remediate the contaminants· Heater wells generally comprise heating components or elements disposed within steel pipes. The heat may either move the contaminants in the soil toward the heater wells or destroy the contaminants in-situ. For example, sufficient levels of heat can be produced to boil the water in the soil and vaporize the contaminants· Contaminants that migrate toward the heater wells can be collected and directed through the wells or piping to the surface, where they can be removed or treated. PFAS compounds may be removed from the vapor stream by passing the heated vapors through a condensing system such as a heat exchanger or scrubber where the PFAS compounds are concentrated into an aqueous solution for treatment.
[00020] In an illustrative embodiment, a flexible, generally, helical heater is implemented to uniquely achieve PFAS remediation in soils by effectively bringing the soil to the necessary temperature or temperatures. The term“helical” or“helix” as used to describe the flexible heater shall include coils that are true helixes and those that are not necessarily a true mathematical helix. The flexible helical heater includes an electrical resistance heating wire coiled about a current return wire that fits inside a small diameter metal casing. The electrical resistance heating wire may be comprised, for example, of a nickel-chromium alloy such as NiChrome®, a copper-nickel alloy such as Cuprothal® or an iron-chromium- aluminum ferritic allow such as Kanthal®. Heating soils to temperatures in the range of 225 to 440 degrees Celsius, for example, requires relatively tight spacing for heater wells, which may drive up the price and complexity of remediation. The flexible helical heaters can fit into smaller diameter metal casings than traditional heaters, which may significantly reduce the cost and complexity of the PFAS remediation. In an illustrative embodiment, specific zones along the length of a heater well that contain more PFAS or TO than other zones are targeted with higher temperature by adjusting the coil spacing. C. In a further embodiment, heat loss is compensated for by adjusting coil spacing to put more heat in at the top and bottom of a casing to compensate for heat loss.
[00021] PFAS remediation may be affected by site characteristics, types of PFAS compounds being remediated due to varying chemical and physical characteristics, source of the PFAS, whether there are multiple types of PFAS compounds, nature of the release pathways, the make-up of other contaminants and materials in the soil. The disclosed remediation technique can take into consideration these variables and the number of carbon bonds and the alkyl functional group of the PFAS being remediated. In general, the larger the molecule, the higher the boiling point, but this general relationship can vary. The disclosed methods may include combinations of the remediation techniques. [00022] Various embodiments of the invention have been described, each having a different combination of elements. The invention is not limited to the specific embodiments disclosed, and may include different combinations of the elements disclosed, omission of some elements or the replacement of elements by the equivalents of such structures.
[00023] While illustrative embodiments have been described, additional advantages and modifications will occur to those skilled in the art. Therefore, the invention in its broader aspects is not limited to specific details shown and described herein. Accordingly, it is intended that the invention not be limited to the specific illustrative embodiments, but be interpreted within the full spirit and scope of the appended claims and their equivalents.

Claims

Claims:
1. A method of remediation of soil containing PFAS compounds and organic carbon, the method comprising: reducing the total organic carbon by heating the soil at a sufficient temperature and for a sufficient duration to reduce surface effects between the PFAS compounds and the TOCs to a sufficient level to permit evaporation of the PFAS from the soil.
2. The method of claim 1 comprising heating the soil at a temperature and for a duration sufficient to reduce total organic carbon to less than 0.15% by weight.
3. The method of claim 1 comprising heating the soil at a temperature and for a duration sufficient to reduce total organic carbon to less than 0.1% by weight.
4. The method of claim 1 comprising heating the soil at a temperature and for a duration sufficient to reduce total organic carbon to less than 0.05% by weight.
5. The method of claim 1 wherein the soil is heated to a temperature in the range of 225 degrees Celsius to 440 degrees Celsius.
6. The method of claim 1 wherein the soil is heated to a temperature in the range of 300 degrees Celsius to 400 degrees Celsius.
7. The method of claim 1 wherein the soil is heated to a temperature in the range of 320 degrees Celsius to 380 degrees Celsius.
8. The method of claim 1 wherein the soil is heated to a temperature in the range of 330 degrees Celsius to 350 degrees Celsius.
9. The method of claim 1 wherein the soil is heated for a duration in the range of 1 to 30 days.
10. The method of claim 1 wherein the soil is heated for a duration in the range of 5 to 25 days.
11. The method of claim 1 wherein the soil is heated for a duration in the range of 2 to 10 days.
12. The method of claim 1 wherein heating is performed by conductive heat transfer using heater wells installed into the soil.
13. The method of claim 1 further comprising capturing the evaporated PFAS by vapor recovery.
14. The method of claim 13 further comprising adding steam to the evaporated PFAS.
15. The method of claim 13 wherein the evaporated PFAS is in a vapor stream, the method further comprising removing PFAS from the vapor stream by cooling the vapor stream and condensing the PFAS.
16. The method of claim 14 further comprising condensing the PFAS and steam to produce a concentrated aqueous PFAS solution.
17. The method of claim 16 further comprising treating the concentrated aqueous PFAS solution by electro oxidation.
18. The method of claim 15 further comprising removing the PFAS from the vapor stream by passing the heated vapors through a scrubber to produce a concentrated aqueous PFAS solution for treatment.
19. The method of any of claim 1 comprising performing the method in-situ.
20 The method of any of claim 1 comprising performing the method ex-situ.
21. The method of claim 1 further comprising heating the soil to a plurality of sufficient temperatures along the length of a heater well using a flexible helical heater.
22. The method of claim 21 comprising heating the soil at the top and/or bottom of the heater well to a greater temperature thereby compensating for heat loss.
23. A system for remediation of soil containing PFAS comprising: a plurality of heater well distributed in an array; the heater well array configured when activated to reduce total organic carbon thereby reducing surface effects between the PFAS compounds and the TOCs to a sufficient level to permit evaporation of the PFAS from the soil.
PCT/US2019/039020 2018-01-19 2019-06-25 Pfas remediation method and system WO2020005966A1 (en)

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US16/452,141 US10675664B2 (en) 2018-01-19 2019-06-25 PFAS remediation method and system
US16/864,889 US20200260533A1 (en) 2018-01-19 2020-05-01 Pfas remediation method and system

Applications Claiming Priority (4)

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US201862689957P 2018-06-26 2018-06-26
US62/689,957 2018-06-26
US16/452,141 2019-06-25
US16/452,141 US10675664B2 (en) 2018-01-19 2019-06-25 PFAS remediation method and system

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PCT/US2018/014472 Continuation-In-Part WO2019143355A1 (en) 2018-01-19 2018-01-19 Flexible helical heater

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US16/452,141 Continuation-In-Part US10675664B2 (en) 2018-01-19 2019-06-25 PFAS remediation method and system

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11661360B2 (en) 2020-06-18 2023-05-30 Wp&E Technologies And Solutions, Llc System for removing per- and polyfluorinated alkyl substances from contaminated aqueous streams, via chemical aided filtration, and methods of use thereof

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WO2005019110A2 (en) * 2002-08-09 2005-03-03 Sievers Instruments, Inc. Inorganic carbon removal
US7004678B2 (en) * 2003-05-15 2006-02-28 Board Of Regents, The University Of Texas System Soil remediation with heated soil
WO2017131972A1 (en) * 2016-01-25 2017-08-03 Oxytec Llc Soil and water remediation method and apparatus for treatment of recalcitrant halogenated substances
WO2018097875A1 (en) * 2016-09-12 2018-05-31 Aecom (Delaware Corporation) Use of electrochemical oxidation for treatment of per-and polyfluoroalkyl substances (pfas) in waste generated from sorbent and resin regeneration processes

Patent Citations (4)

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Publication number Priority date Publication date Assignee Title
WO2005019110A2 (en) * 2002-08-09 2005-03-03 Sievers Instruments, Inc. Inorganic carbon removal
US7004678B2 (en) * 2003-05-15 2006-02-28 Board Of Regents, The University Of Texas System Soil remediation with heated soil
WO2017131972A1 (en) * 2016-01-25 2017-08-03 Oxytec Llc Soil and water remediation method and apparatus for treatment of recalcitrant halogenated substances
WO2018097875A1 (en) * 2016-09-12 2018-05-31 Aecom (Delaware Corporation) Use of electrochemical oxidation for treatment of per-and polyfluoroalkyl substances (pfas) in waste generated from sorbent and resin regeneration processes

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11661360B2 (en) 2020-06-18 2023-05-30 Wp&E Technologies And Solutions, Llc System for removing per- and polyfluorinated alkyl substances from contaminated aqueous streams, via chemical aided filtration, and methods of use thereof

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