WO2023061818A1 - System for the decontamination of contaminated materials by means of heating tubes with conductive supports - Google Patents

System for the decontamination of contaminated materials by means of heating tubes with conductive supports Download PDF

Info

Publication number
WO2023061818A1
WO2023061818A1 PCT/EP2022/077664 EP2022077664W WO2023061818A1 WO 2023061818 A1 WO2023061818 A1 WO 2023061818A1 EP 2022077664 W EP2022077664 W EP 2022077664W WO 2023061818 A1 WO2023061818 A1 WO 2023061818A1
Authority
WO
WIPO (PCT)
Prior art keywords
contaminated
heating
soil
contaminated materials
fins
Prior art date
Application number
PCT/EP2022/077664
Other languages
French (fr)
Inventor
Jan Haemers
Rabih JENADRI
Original Assignee
The Soil Research Lab Sprl
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 The Soil Research Lab Sprl filed Critical The Soil Research Lab Sprl
Publication of WO2023061818A1 publication Critical patent/WO2023061818A1/en

Links

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
    • B09C1/062Reclamation of contaminated soil thermally by using electrode or resistance heating elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/40Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
    • EFIXED CONSTRUCTIONS
    • E02HYDRAULIC ENGINEERING; FOUNDATIONS; SOIL SHIFTING
    • E02DFOUNDATIONS; EXCAVATIONS; EMBANKMENTS; UNDERGROUND OR UNDERWATER STRUCTURES
    • E02D3/00Improving or preserving soil or rock, e.g. preserving permafrost soil
    • E02D3/11Improving or preserving soil or rock, e.g. preserving permafrost soil by thermal, electrical or electro-chemical means
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE
    • B09B2101/00Type of solid waste
    • B09B2101/90Soil, e.g. excavated soil from construction sites

Definitions

  • the present invention consists of a heating system designed to improve the thermal treatment of contaminated materials by means of conductive steel supports increasing the exchange surface between the heating tube and its environment.
  • the invention relates in particular to a heating system suitable for ex-situ thermal desorption treatment (excavated contaminated materials) to remediate materials containing hydrocarbons and/or other organic contaminants.
  • Soil contamination is a problem of great importance in a world where the environment and sustainable development are becoming more and more important. This often invisible problem can be caused by a wide variety of chemical, biological or even radioactive contaminants and an equally wide range of pollution sources. Left unchecked, contamination can spread to other resources essential to the surrounding flora and fauna. It is therefore important, in the interest of environmental protection and public health, to eliminate these contaminants before they have too great an impact.
  • Soil remediation technologies are multiple and can be separated into three main categories: thermal, biological and physicochemical.
  • the choice of the technique depends on several parameters such as the nature of the contamination, the soil properties, the physical constraints of the site and the total cost of the project.
  • thermal desorption is based on heating the soil to volatilize the contaminants and allow their extraction and destruction/reuse after condensation. Thermal desorption is effective against organic contaminants, cyanides, mercury and any other component that can be volatilized at temperatures below 550°C.
  • Heating via thermal conduction is one of the techniques used in the field of thermal desorption (W02001078914A8). With this technique, energy from heating tubes is propagated radially through the soil by conduction. This has several advantages over other soil remediation options because thermal conduction allows soil to be heated to temperatures in excess of 350°C (which is not possible, for example, with resistive electric heating (US5656239A)) and to easily and quickly treat soils contaminated with a wide variety of contaminants, regardless of soil heterogeneity. Indeed, thermal conductivity has the particularity of not fluctuating by large orders of magnitude with the materials present in the soil. Therefore, thermal conduction is much more efficient than other heat transfer methods in heterogeneous soils.
  • This technique is applicable both ex-situ and in-situ.
  • ex-situ thermal desorption With ex-situ thermal desorption (ESTD), contaminated soil is excavated and used to form piles or placed in containers that are thermally treated.
  • in-situ thermal desorption the heating tubes are inserted directly into the contaminated soil, thus avoiding excavation and transport of soil. This also allows the treatment of soils in restricted areas and/or with limited access such as remote sites, sites in urban areas, basements of houses, etc. In general, this technique is faster and has a reduced environmental impact.
  • the present invention presents a heating system for improving the thermal treatment of contaminated materials by means of steel conductive supports increasing the exchange surface between the heating tube and its environment.
  • the present invention also relates to a heating system for improving the thermal treatment of contaminated materials by means of cast-iron conductive supports increasing the exchange surface between the heating tube and its environment.
  • the heating tubes are placed horizontally between layers of contaminated materials.
  • These tubes can be up to 20 meters long and the volume of said contaminated materials around the last few meters of the heating tube, which are the furthest away from the heat source, rises in temperature slower than the rest of the stack due to uneven heat distribution along the heating tubes.
  • current processes do not allow the heat to be voluntary directed to selected portions of the heating tube, which is useful when certain zones of the contaminated material volume contain more moisture or require higher treatment temperatures than the remaining zones.
  • the present invention presents a solution to correct this heating offset by increasing the exchange surface between this portion of the heating tube and the contaminated materials surrounding it by means of conductive supports, known as "fins".
  • This invention also makes it possible to modulate, according to external parameters, the heating within the volume to be treated and to bring enough energy to the required zones, thus avoiding important energy losses.
  • CN110295588A and US20080069640A1 aim to increase the contact area of the heating tube and the soil, in order to improve efficiency of the heating tube in heating the soil.
  • the present invention improves the application with 2 advantages over the prior art.
  • the first advantage is the independence of the fins from the heating tube, it allows the user to select where on the heating tube the heat transfer surface must be augmented and by how much.
  • the second advantage is the simple shape of the fins, this makes their manufacturing easier and thus cheaper; this causes less friction when initiating and ending; and reduces the chance of having air pockets.
  • Figure 1 Example of a portion of a heating tube with 4 fins
  • Figure 2a Zoom on a fin below the heating tube
  • FIG. 3 Example of several heating tubes with fins in ex-situ mode
  • contaminated soil and "contaminated material” are used here synonymously and should be understood to include all types of soil, sludge or other materials that may be contaminated with any cocktail of pollutants, such as organic contaminants, e.g. hydrocarbons, and inorganic contaminants, whose boiling temperature, Tb, at atmospheric pressure is less than 600°C and/or heavy metals.
  • Conductive heat occurs when two materials or material objects are in direct contact and the temperature of one is higher than the temperature of the other.
  • Thermal conduction consists of a transfer of kinetic energy from the hotter medium to the colder one.
  • the term “conduction” as used herein is therefore intended to refer to all types of heat transfer in which heat is moved from one (warmer) object to another (cooler) object by direct contact. It should be understood that in the present invention, when heat transfer by conduction is mentioned, a very small amount of heat is usually also transferred to the contaminated material by means of radiation.
  • the present invention relates to a system having a number of thermally conductive tubes each made of 2 pipes, inner and outer, placed in contaminated soil (the outer pipe is in direct contact with the soil).
  • the pipes are in communication with a heat source causing a heated fluid to flow through the pipes from the inner to the outer, causing the temperature of the surrounding soil to rise.
  • the invention is intended to increase the exchange surface between the heating tube and the surrounding soil volume by using steel or cast-iron plates, hereinafter referred to as "fins", placed on the outer pipe of the heating tube.
  • the contaminated soil is excavated and then treated on site or moved to a designated cleanup site.
  • the soil is then used to form piles or placed in containers for batch processing (ex-situ, ESTD).
  • the heating tubes are inserted horizontally in rows through the pile in a way that the entire volume of contaminated soil is heated.
  • the present invention concerns fins (2) (3) placed or welded directly below or above each heating tube (1) ( Figure 2a). Since steel or cast-iron have a thermal conductivity that is tens of times higher than that of various soil types, the heat is transferred quicker to the volume of contaminated soil (4) (figure 3) surrounding a heating tube with fins. As a result, the heating time is accelerated and the treatment time is decreased, resulting in a treatment with higher energy efficiency..
  • the fins are not attached or welded to the heating tubes, but simply placed on or under them.
  • the fins are made of any grade of steel or cast-iron having a heat conductivity higher than 14 W/mK at 25°C and a density higher than 7.6 g/cm 3 .
  • the material choice is abundant and can be adapted in case of acidic contaminants.
  • the fins are made of malleable and conductive metal, different from steel. Thus, they can be lighter and easier to place.
  • the number of fins to be placed and their size depends on the total length of the heating tube.
  • the position and size of the fins depend on the quality of the materials to be treated, particularly their moisture content and/or their concentration of pollutants.
  • the heating tubes have one large fin.
  • the heating tubes have a plurality of small sized fins ( Figure 1). The fins on a single heating tube are spaced a few tens of centimeters apart and can be of different sizes: with the one with the largest surface area (3) placed at the end of the tube and the smallest surface area (2) moving away from the end of the tube.
  • the thickness of the fins is between 1mm and 20mm and preferably between 2 and 10mm.
  • the shape of the fin is rectangular on the sides and semicircular in the middle between the two rectangular parts ( Figure 2b).
  • the shape of the fin is rectangular on the sides and semicircular in the middle between the two rectangular parts to match the shape of the heating tube and to maximize contact.
  • the length of the fin is between 350mm and 1500mm and preferably between 500 and 1200mm.
  • the width of the fin (wingspan) is between 400mm and 1000mm and preferably between 500 and 800mm.
  • the fins are oriented parallel to the layers of material to be treated.
  • the invention relates to the usage of a fin for the treatment of contaminated materials, wherein the fin is connected to a heating pipe for a distance, measured over the cross section of the heating pipe, of at least the outer radius and maximally 90% of the outer circumference of the heating pipe, preferably 40-60% of the outer circumference of the heating pipe.
  • the wingspan of the fin is between 2 and 100 times the outer diameter of the heating tube. In an embodiment, the wingspan of the fin is between 5 and 25 times the outer diameter of the heating tube.
  • the wingspan is the maximum distance of the fin, measured from tip to tip in the axial plane.
  • the axial plane is the plane extending radially from the longitudinal axis of the pipe.

Abstract

The present invention relates to a system for the thermal treatment of materials contaminated with hydrocarbons and/or other volatile organic or inorganic pollutants at 600°C. The present invention proposes a system for treating said contaminated materials via thermally conductive tubes provided with conductive steel or cast-iron supports, called "fins", locally increasing the heat transfer to the contaminated materials.

Description

SYSTEM FOR THE DECONTAMINATION OF CONTAMINATED MATERIALS BY MEANS OF HEATING TUBES WITH CONDUCTIVE SUPPORTS
FIELD OF THE INVENTION
The present invention consists of a heating system designed to improve the thermal treatment of contaminated materials by means of conductive steel supports increasing the exchange surface between the heating tube and its environment. The invention relates in particular to a heating system suitable for ex-situ thermal desorption treatment (excavated contaminated materials) to remediate materials containing hydrocarbons and/or other organic contaminants.
BACKGROUND OF THE INVENTION
Soil contamination is a problem of great importance in a world where the environment and sustainable development are becoming more and more important. This often invisible problem can be caused by a wide variety of chemical, biological or even radioactive contaminants and an equally wide range of pollution sources. Left unchecked, contamination can spread to other resources essential to the surrounding flora and fauna. It is therefore important, in the interest of environmental protection and public health, to eliminate these contaminants before they have too great an impact.
Soil remediation technologies are multiple and can be separated into three main categories: thermal, biological and physicochemical. The choice of the technique depends on several parameters such as the nature of the contamination, the soil properties, the physical constraints of the site and the total cost of the project.
One of these techniques, thermal desorption, is based on heating the soil to volatilize the contaminants and allow their extraction and destruction/reuse after condensation. Thermal desorption is effective against organic contaminants, cyanides, mercury and any other component that can be volatilized at temperatures below 550°C.
Heating via thermal conduction is one of the techniques used in the field of thermal desorption (W02001078914A8). With this technique, energy from heating tubes is propagated radially through the soil by conduction. This has several advantages over other soil remediation options because thermal conduction allows soil to be heated to temperatures in excess of 350°C (which is not possible, for example, with resistive electric heating (US5656239A)) and to easily and quickly treat soils contaminated with a wide variety of contaminants, regardless of soil heterogeneity. Indeed, thermal conductivity has the particularity of not fluctuating by large orders of magnitude with the materials present in the soil. Therefore, thermal conduction is much more efficient than other heat transfer methods in heterogeneous soils.
This technique is applicable both ex-situ and in-situ. With ex-situ thermal desorption (ESTD), contaminated soil is excavated and used to form piles or placed in containers that are thermally treated. With in-situ thermal desorption, the heating tubes are inserted directly into the contaminated soil, thus avoiding excavation and transport of soil. This also allows the treatment of soils in restricted areas and/or with limited access such as remote sites, sites in urban areas, basements of houses, etc. In general, this technique is faster and has a reduced environmental impact.
Current techniques increase the temperature of the heating tube by circulating hot gases (combustion gases), coming from a burner, in two concentric metal tubes (BE1024596B1).
The present invention presents a heating system for improving the thermal treatment of contaminated materials by means of steel conductive supports increasing the exchange surface between the heating tube and its environment.
The present invention also relates to a heating system for improving the thermal treatment of contaminated materials by means of cast-iron conductive supports increasing the exchange surface between the heating tube and its environment.
In particular, in an ESTD mode, the heating tubes are placed horizontally between layers of contaminated materials. These tubes can be up to 20 meters long and the volume of said contaminated materials around the last few meters of the heating tube, which are the furthest away from the heat source, rises in temperature slower than the rest of the stack due to uneven heat distribution along the heating tubes. In addition, current processes do not allow the heat to be voluntary directed to selected portions of the heating tube, which is useful when certain zones of the contaminated material volume contain more moisture or require higher treatment temperatures than the remaining zones. The present invention presents a solution to correct this heating offset by increasing the exchange surface between this portion of the heating tube and the contaminated materials surrounding it by means of conductive supports, known as "fins". This invention also makes it possible to modulate, according to external parameters, the heating within the volume to be treated and to bring enough energy to the required zones, thus avoiding important energy losses.
CN110295588A and US20080069640A1 aim to increase the contact area of the heating tube and the soil, in order to improve efficiency of the heating tube in heating the soil.
The present invention improves the application with 2 advantages over the prior art. The first advantage is the independence of the fins from the heating tube, it allows the user to select where on the heating tube the heat transfer surface must be augmented and by how much. The second advantage is the simple shape of the fins, this makes their manufacturing easier and thus cheaper; this causes less friction when initiating and ending; and reduces the chance of having air pockets.
BRIEF DESCRIPTION OF THE FIGURES
Figure 1 : Example of a portion of a heating tube with 4 fins
Figure 2a : Zoom on a fin below the heating tube
Figure 2b: Zoom on a single fin
Figure 3: Example of several heating tubes with fins in ex-situ mode
The legend of the figures is as follows:
1. heating tube
2. minimum wingspan
3. maximum wingspan
4. pile of contaminated materials
DETAILED DESCRIPTION OF THE INVENTION
The terms "contaminated soil" and "contaminated material" are used here synonymously and should be understood to include all types of soil, sludge or other materials that may be contaminated with any cocktail of pollutants, such as organic contaminants, e.g. hydrocarbons, and inorganic contaminants, whose boiling temperature, Tb, at atmospheric pressure is less than 600°C and/or heavy metals. Conductive heat occurs when two materials or material objects are in direct contact and the temperature of one is higher than the temperature of the other. Thermal conduction consists of a transfer of kinetic energy from the hotter medium to the colder one. The term "conduction" as used herein is therefore intended to refer to all types of heat transfer in which heat is moved from one (warmer) object to another (cooler) object by direct contact. It should be understood that in the present invention, when heat transfer by conduction is mentioned, a very small amount of heat is usually also transferred to the contaminated material by means of radiation.
The present invention relates to a system having a number of thermally conductive tubes each made of 2 pipes, inner and outer, placed in contaminated soil (the outer pipe is in direct contact with the soil). The pipes are in communication with a heat source causing a heated fluid to flow through the pipes from the inner to the outer, causing the temperature of the surrounding soil to rise. The invention is intended to increase the exchange surface between the heating tube and the surrounding soil volume by using steel or cast-iron plates, hereinafter referred to as "fins", placed on the outer pipe of the heating tube.
In a preferred embodiment, the contaminated soil is excavated and then treated on site or moved to a designated cleanup site. The soil is then used to form piles or placed in containers for batch processing (ex-situ, ESTD). The heating tubes are inserted horizontally in rows through the pile in a way that the entire volume of contaminated soil is heated.
The present invention concerns fins (2) (3) placed or welded directly below or above each heating tube (1) (Figure 2a). Since steel or cast-iron have a thermal conductivity that is tens of times higher than that of various soil types, the heat is transferred quicker to the volume of contaminated soil (4) (figure 3) surrounding a heating tube with fins. As a result, the heating time is accelerated and the treatment time is decreased, resulting in a treatment with higher energy efficiency..
In a preferred embodiment, the fins are not attached or welded to the heating tubes, but simply placed on or under them.
In a preferred embodiment the fins are made of any grade of steel or cast-iron having a heat conductivity higher than 14 W/mK at 25°C and a density higher than 7.6 g/cm3. Thus, the material choice is abundant and can be adapted in case of acidic contaminants. In a preferred embodiment the fins are made of malleable and conductive metal, different from steel. Thus, they can be lighter and easier to place.
The number of fins to be placed and their size depends on the total length of the heating tube.
In a preferred embodiment, the position and size of the fins depend on the quality of the materials to be treated, particularly their moisture content and/or their concentration of pollutants.
In a preferred embodiment, the heating tubes have one large fin. In another preferred embodiment, the heating tubes have a plurality of small sized fins (Figure 1). The fins on a single heating tube are spaced a few tens of centimeters apart and can be of different sizes: with the one with the largest surface area (3) placed at the end of the tube and the smallest surface area (2) moving away from the end of the tube.
In the present invention, the thickness of the fins is between 1mm and 20mm and preferably between 2 and 10mm. The shape of the fin is rectangular on the sides and semicircular in the middle between the two rectangular parts (Figure 2b).
The shape of the fin is rectangular on the sides and semicircular in the middle between the two rectangular parts to match the shape of the heating tube and to maximize contact.
The length of the fin is between 350mm and 1500mm and preferably between 500 and 1200mm. The width of the fin (wingspan) is between 400mm and 1000mm and preferably between 500 and 800mm. The fins are oriented parallel to the layers of material to be treated.
The invention relates to the usage of a fin for the treatment of contaminated materials, wherein the fin is connected to a heating pipe for a distance, measured over the cross section of the heating pipe, of at least the outer radius and maximally 90% of the outer circumference of the heating pipe, preferably 40-60% of the outer circumference of the heating pipe.
In an embodiment, the wingspan of the fin is between 2 and 100 times the outer diameter of the heating tube. In an embodiment, the wingspan of the fin is between 5 and 25 times the outer diameter of the heating tube. The wingspan is the maximum distance of the fin, measured from tip to tip in the axial plane. The axial plane is the plane extending radially from the longitudinal axis of the pipe.

Claims

7 CLAIMS
1. System for the treatment of contaminated materials by means of thermally conductive tubes with conductive steel supports, locally increasing their thermal conductivity.
2. System for the treatment of contaminated materials by means of thermally conductive tubes with cast-iron supports, locally increasing the heat transfer to the contaminated materials.
PCT/EP2022/077664 2021-10-12 2022-10-05 System for the decontamination of contaminated materials by means of heating tubes with conductive supports WO2023061818A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
BE20215796A BE1029844B1 (en) 2021-10-12 2021-10-12 SYSTEM FOR DEPOLLUTION OF CONTAMINATED MATERIALS BY MEANS OF HEATING TUBES WITH CONDUCTIVE SUPPORTS
BEBE2021/5796 2021-10-12

Publications (1)

Publication Number Publication Date
WO2023061818A1 true WO2023061818A1 (en) 2023-04-20

Family

ID=78269531

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP2022/077664 WO2023061818A1 (en) 2021-10-12 2022-10-05 System for the decontamination of contaminated materials by means of heating tubes with conductive supports

Country Status (2)

Country Link
BE (1) BE1029844B1 (en)
WO (1) WO2023061818A1 (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62112811A (en) * 1985-11-13 1987-05-23 Shimizu Constr Co Ltd Improving work of soft cohesive ground with heat pipe
US5656239A (en) 1989-10-27 1997-08-12 Shell Oil Company Method for recovering contaminants from soil utilizing electrical heating
WO2001078914A2 (en) 2000-04-14 2001-10-25 Shell Internationale Research Maatschappij B.V. Heater element for use in an situ thermal desorption soil remediation system
US20080069640A1 (en) 2004-06-11 2008-03-20 Jan Haemers Method and System for Cleaning a Soil Containing Contaminants
BE1024596B1 (en) 2016-09-23 2018-04-25 Soil Research Lab Sprl System and method for remediation of contaminated soil
CN110295588A (en) 2019-06-25 2019-10-01 东莞市广渠建筑工程有限公司 A kind of Soft Ground device and its processing method

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62112811A (en) * 1985-11-13 1987-05-23 Shimizu Constr Co Ltd Improving work of soft cohesive ground with heat pipe
US5656239A (en) 1989-10-27 1997-08-12 Shell Oil Company Method for recovering contaminants from soil utilizing electrical heating
WO2001078914A2 (en) 2000-04-14 2001-10-25 Shell Internationale Research Maatschappij B.V. Heater element for use in an situ thermal desorption soil remediation system
US20080069640A1 (en) 2004-06-11 2008-03-20 Jan Haemers Method and System for Cleaning a Soil Containing Contaminants
BE1024596B1 (en) 2016-09-23 2018-04-25 Soil Research Lab Sprl System and method for remediation of contaminated soil
CN110295588A (en) 2019-06-25 2019-10-01 东莞市广渠建筑工程有限公司 A kind of Soft Ground device and its processing method

Also Published As

Publication number Publication date
BE1029844B1 (en) 2023-05-08
BE1029844A1 (en) 2023-05-05

Similar Documents

Publication Publication Date Title
ES2330333T3 (en) PROCEDURE AND SYSTEM FOR CLEANING A FLOOR CONTAINING POLLUTANTS.
US5660500A (en) Enhanced deep soil vapor extraction process and apparatus utilizing sheet metal pilings
US10259024B2 (en) Device, system and process for treating porous materials
US10688545B2 (en) Thermal in situ sustainable remediation system and method for groundwater and soil restoration
US20150078827A1 (en) Induction heating system for thermal desorption processes
WO2012055818A2 (en) Devices and methods for soil remediation
Huon et al. In Situ Radio‐Frequency Heating for Soil Remediation at a Former Service Station: Case Study and General Aspects
CN211360044U (en) Soil thermal desorption processing system
CN105598149A (en) Circular fluid thermal desorption soil contamination processing method and device
WO2023061818A1 (en) System for the decontamination of contaminated materials by means of heating tubes with conductive supports
CN208213932U (en) A kind of original position combustion gas thermal desorption soil restoring device
TW570845B (en) Method of treating contaminated soil into harmless state and applicator therefor
US11185901B1 (en) Thermal in situ sustainable remediation system and method for groundwater and soil restoration
BE1028844B1 (en) Combination of depollution techniques: In Situ Thermal Desorption and Immobilization
CN211304219U (en) Organic pollution place prosthetic devices
Baker et al. In-pile thermal desorption of PAHs, PCBs and dioxins/furans in soil and sediment
CN210208077U (en) Heat transfer device for in-situ thermal desorption soil remediation
Lanzalaco et al. Electrochemically Assisted Thermal-Based Technologies for Soil Remediation
CN104858222A (en) Soil restoration electromagnetic pyrolysis steam rotary furnace
WO2020005966A1 (en) Pfas remediation method and system
CN107755416A (en) A kind of thermal desorption cooperating with low-temperature plasma soil restoring technology
CN108352207A (en) Passively cooling ion exchange column
Demcak et al. Overview of chosen techniques and methods for soils remediation
KR102222440B1 (en) Heating apparatus using microwave and thermal desorption system using the same
CN211538955U (en) Organic contaminated soil in-situ alternate electric heating desorption system

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 22801041

Country of ref document: EP

Kind code of ref document: A1