CN207577115U - The organic polluted soil dystopy thermal desorption repair system that a kind of waste heat efficiently utilizes - Google Patents

The organic polluted soil dystopy thermal desorption repair system that a kind of waste heat efficiently utilizes Download PDF

Info

Publication number
CN207577115U
CN207577115U CN201721586073.9U CN201721586073U CN207577115U CN 207577115 U CN207577115 U CN 207577115U CN 201721586073 U CN201721586073 U CN 201721586073U CN 207577115 U CN207577115 U CN 207577115U
Authority
CN
China
Prior art keywords
air
outlet
soil
entrance
temperature
Prior art date
Legal status (The legal status 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 status listed.)
Active
Application number
CN201721586073.9U
Other languages
Chinese (zh)
Inventor
籍龙杰
杨乐巍
李泰平
刘鹏
张岳
王文峰
张晓艺
李书鹏
张建灿
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BCEG Environmental Remediation Co Ltd
Original Assignee
BCEG Environmental Remediation Co Ltd
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 BCEG Environmental Remediation Co Ltd filed Critical BCEG Environmental Remediation Co Ltd
Priority to CN201721586073.9U priority Critical patent/CN207577115U/en
Application granted granted Critical
Publication of CN207577115U publication Critical patent/CN207577115U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Processing Of Solid Wastes (AREA)

Abstract

The utility model provides the organic polluted soil dystopy thermal desorption repair system that a kind of waste heat efficiently utilizes.The burner is connected with high-temperature oxydation room, the high temperature flue gas pipeline of high-temperature oxydation room is connected respectively with rotary kiln heat treatment system and air heat exchanger, the high temperature air outlet of air heat exchanger is connected with burner, the flue gas pipeline of air preheater is connected with the entrance of chilling tower, the outlet of chilling tower is connected with the entrance of bag filter, the outlet of bag filter is connected with the entrance of extracting tower, the outlet of extracting tower is connected with the air inlet of air-introduced machine two, and the outlet of air-introduced machine two is connected with chimney.The utility model can reduce the consumption of fuel, system carries out exhaustive oxidation degradation to organic pollution, reduce the discharge of pollutant, reduce secondary pollution risk, can stablize, continuously, efficiently carry out thermal desorption processing, suitable for different type, the repairing and treating of organic material contaminated soil/bed mud of concentration.

Description

The organic polluted soil dystopy thermal desorption repair system that a kind of waste heat efficiently utilizes
Technical field
The utility model is related to the organic polluted soil dystopy thermal desorption repair systems that a kind of waste heat efficiently utilizes, and belonging to has Machine contaminated soil heterotopic thermal desorption repair system technical field.
Background technology
At present, with the implementation of " moving back two into three, Tui Chengjin gardens ", domestic many carryover contamination places, especially chemical industry are dirty Place is contaminated, it is found that there are serious organic pollutions for soil.If do not taken timely and effectively control measures, can to ambient atmosphere and Biology is possible to deposit with rainwater there are health threat, and permeate the ground water, serious threat human health.Soil is organic Object pollution problem has caused the extensive concern of people, and soil remediation is imperative.
The current organic contaminated sites in China are mainly organic agricultural chemicals insecticide, persistence organic pollutant and petroleum hydrocarbon etc. Non- organo-chlorine pollutant.For organic pollution place, it is applied successfully at present there are many recovery technique.For example, Room temperature desorption, curing/stabilizing technology, thermal desorption in situ, in situ chemical oxidation and biodegradation technique etc..For different pollutions Object, different contaminated sites, need to take suitable technical solution and recovery technique.It is meanwhile efficient, thorough, cost savings type Recovery technique scheme also can cause organic contamination place to reach reparation target in a short time, realize its recycle value.Cause This, researches and develops a kind of practical " contaminated sites rapid treating technology and equipment ", has great application value and prospect.
Heat treatment technics is mostly dystopy processing, is often referred to pollution medium being transferred to specific processing unit or combustion chamber Deng being then exposed under high temperature, so as to destroy or remove a kind of repair process of wherein pollutant.Showering technology Main advantage is that process cycle is short, and processing procedure is visual, and the continuous mixing of pollution medium and homogenizing process are easily controllable.But Pollutant distribution is uneven in contaminated soil domain, and pollutant often has higher boiling point, needs a large amount of thermal energy in processing procedure Consumption, repair process can generate a large amount of high-temperature tail gas.For traditional rotary kiln heating system, soil treatment amount is 25m3/h When, the thermal loss that high-temperature flue gas distributes is 30%~60%, is the major part of heat-energy losses in thermal desorption system.And high temperature It is difficult also to lead to the problem of vent gas treatment while heat losses are brought for flue gas.Therefore, how by optimizing thermal desorption system System, realizes the efficient utilization of waste heat, for reducing heat losses, reduces contaminated soil cost of disposal, has important engineering significance.
Chinese patent (204247684 U of CN) discloses a kind of contaminated soil thermal desorption system of the efficient reuse of waste heat, combustion A part of direct cooling treatment of high-temperature flue gas that room generates is burnt, causes a large amount of thermal loss;And another portion that combustion chamber comes out Enter rotary kiln after dividing high-temperature flue gas mixing fresh air so that the oxygen content in thermal desorption region increases, also to a certain extent Increase the generation risk of the noxious materials such as thermal desorption Guo journey Zhong bioxin.Chinese patent (102218446 A of CN) discloses one The system that UTILIZATION OF VESIDUAL HEAT IN is carried out during kind Polluted Soil thermal desorption, the device use two-stage combustion, and system energy consumption is higher, is manipulated so This certainly will also increase;The mating Turbo-generator Set of cogeneration need, system complex, cost are higher.
Chinese patent (105080957 A of CN) discloses the contaminated soil thermal desorption repair system that a kind of waste heat recycles, Using surface-type heat-exchange device, combustion air is helped to carry out at preheating room temperature the high-temperature tail gas generated in repair process Reason since vent gas treatment process is using activated carbon adsorption, is not carried out the thorough degradation of pollutant, only realize pollutant by Gas phase becomes hazardous waste after activated carbon adsorption saturation to the transfer process of solid phase, need to carry out after-treatment, cost of disposal compared with It is high.Chinese patent (104741372 A of CN) discloses a kind of replaces activated carbon as tail gas adsorption agent and utilization by the use of charcoal Charcoal mixes the novel thermal desorption repair system and method that thermal desorption heat supply is used for as combustion heat source, the invention with contaminated soil Complete thermal desorption device is not provided for above-mentioned thermal desorption process.Moreover, the adsorption effect of charcoal Dui bioxin needs into one Step is demonstrate,proved.
Chinese patent (CN 101530858A) discloses a kind of direct thermal desorption device of contaminated soil, wherein hot-air with Contaminated soil contacts in the same direction, it is impossible to realize being sufficiently mixed for hot-air and contaminated soil, thermal desorption is less efficient.Chinese patent (CN 101780467A) discloses a kind of indirect thermal desorption equipment of contaminated soil, and the patent core apparatus heating rotary kiln is by interior Layer structure is formed with layer structure, and heating fuel system heats between endothecium structure and layer structure, contaminated soil and heat source Heat exchange can not be come into full contact with, causes thermal desorption less efficient.
The shortcomings of more than dystopy thermal desorption system or device are low there are utilization efficiency of heat energy, and vent gas treatment design is unreasonable.
Utility model content
The purpose of this utility model is to solve the above-mentioned problems of the prior art, and then it is efficient to provide a kind of waste heat The organic polluted soil dystopy thermal desorption repair system utilized.
The purpose of this utility model is achieved through the following technical solutions:
The organic polluted soil dystopy thermal desorption repair system that a kind of waste heat efficiently utilizes, including:Burner, high-temperature oxydation Room, rotary kiln heat treatment system, air-introduced machine one, cyclone dust collectors, soil pretreatment system, feed system, air heat exchanger, Chilling tower, bag filter, extracting tower, soil moistening and lowering temperature device, soil discharge system, normal temperature air entrance, high temperature air Outlet, chimney, air blower and air-introduced machine two, the burner are connected with high-temperature oxydation room, the high-temperature flue gas of high-temperature oxydation room Pipeline is connected respectively with rotary kiln heat treatment system and air heat exchanger, the air outlet of air blower and air heat exchanger it is normal Warm air entrance is connected, and the high temperature air outlet of air heat exchanger is connected with burner, the flue gas pipeline of air preheater Be connected with the entrance of chilling tower, the outlet of chilling tower is connected with the entrance of bag filter, the outlet of bag filter with The entrance of extracting tower is connected, and the outlet of extracting tower is connected with the air inlet of air-introduced machine two, the outlet of air-introduced machine two and chimney It is connected, the air inlet phase of the volatility/half volatile organic contaminant pipeline and air-introduced machine one of rotary kiln heat treatment system Connection, the air outlet of air-introduced machine one are connected with the entrance of cyclone dust collectors, the air of the heating contaminated soil of cyclone dust collectors Pipeline is connected with high-temperature oxydation room, the dust pipeline of cyclone dust collectors and the outlet of soil pretreatment system respectively with charging The arrival end of system is connected, and the outlet of feed system is connected with the material inlet of rotary kiln heat treatment system, rotary kiln The material outlet of heat treatment system is connected with the entrance of soil moistening and lowering temperature device, the outlet of soil moistening and lowering temperature device with Soil discharge system is connected.
The beneficial effects of the utility model:
Tthe utility model system high temperature oxidizing chamber sets two outlets, is respectively connected to entering for rotary kiln thermal desorption device The high-temperature flue gas that high-temperature oxydation room comes out is divided into two strands of air-flows by the entrance of mouth and air preheater.The utility model can subtract The consumption of few fuel, system carry out exhaustive oxidation degradation to organic pollution, reduce the discharge of pollutant, reduce secondary pollution wind Danger, can stablize, continuously, efficiently carry out thermal desorption processing, suitable for different type, various concentration organic pollution soil The repairing and treating of earth/bed mud.
The flue-gas temperature entered in rotary kiln in Tthe utility model system is higher, while realizes removing and the soil of pollutant The preheating and drying process of earth is equivalent in rotary kiln and exists simultaneously preheating and drying section and thermal desorption section two parts.The utility model It is stable to the purification process of contaminated soil, uniform, it is not affected by environment, it can effectively increase the place of unit interval contaminated soil Reason amount improves operational efficiency, realizes that stable, continuous, efficient thermal desorption is handled to organic polluted soil, applicable different pollutions Type, concentration organic polluted soil improvement.
The air preheater of the utility model can efficiently use the heat in the high-temperature flue gas that high-temperature oxydation room comes out, and carry The temperature of high combustion air reduces the consumption of fossil fuel;Meanwhile the operating load of chilling tower is reduced, reduce disappearing for water resource Consumption.
The utility model realizes maximally utilizing for thermal desorption system waste heat, efficient and saving energy.With as follows Some advantage:
1st, improve and overheavy firing, after the hot-air after air preheater enters in stove, accelerate fuel Fire and combustion process ensure to stablize burning in stove, play a part of improvement, overheavy firing.
2nd, augmentation of heat transfer, since burning is improved and strengthened in stove, in addition the hot blast temperature entered in stove improves, in stove Average temperature level is also improved, so as to strengthen radiant heat transfer in stove.
3rd, reduce stove internal loss, reduce exhaust gas temperature, improve the thermal efficiency.Due to flameholding in stove, radiant heat exchange Strengthen, loss of the inadequacy burning for chemistry mechanics reason can be reduced.
Description of the drawings
Fig. 1 is the organic polluted soil dystopy thermal desorption repair system schematic diagram that a kind of waste heat efficiently utilizes.
Fig. 2 is the structure diagram of soil pretreatment system 6.
Fig. 3 is the structure diagram of soil moistening and lowering temperature device 12.
Reference numeral in figure, 1 is burner, and 2 be high-temperature oxydation room, and 3 be rotary kiln heat treatment system, and 4 be air inducing Machine one, 5 be cyclone dust collectors, and 6 be soil pretreatment system, and 7 be feed system, and 8 be air heat exchanger, and 9 be chilling tower, and 10 are Bag filter, 11 be extracting tower, and 12 be soil moistening and lowering temperature device, and 13 be soil discharge system, and 14 be normal temperature air entrance, 15 export for high temperature air, and 16 be chimney, and 17 be air blower, and 18 be air-introduced machine two, and 61 be vibrating screen, and 62 be crusher, and 63 are Material mixing equipment, 64 be Magnet Separater, and 65 be belted electronic balance, and 66 devices in order to control, 121 be scrapper conveyor, and 122 be outer Cover, 123 be spray head, and 124 be cooling water pipe.
Specific embodiment
The utility model is described in further detail below in conjunction with attached drawing:The present embodiment is with the utility model skill Implemented under premised on art scheme, give detailed embodiment, but the scope of protection of the utility model be not limited to it is following Embodiment.
As shown in Figure 1, the organic polluted soil dystopy thermal desorption that a kind of waste heat involved by the present embodiment efficiently utilizes is repaiied Complex system, including:Burner 1, high-temperature oxydation room 2, rotary kiln heat treatment system 3, air-introduced machine 1, cyclone dust collectors 5, soil Earth pretreatment system 6, feed system 7, air heat exchanger 8, chilling tower 9, bag filter 10, extracting tower 11, soil humidification drop Warm device 12, soil discharge system 13, normal temperature air entrance 14, high temperature air outlet 15, chimney 16, air blower 17 and air inducing Machine 2 18, the burner 1 are connected with high-temperature oxydation room 2, and the high temperature flue gas pipeline of high-temperature oxydation room 2 adds respectively with rotary kiln Heat treatment system 3 is connected with air heat exchanger 8, the air outlet of air blower 17 and the normal temperature air entrance 14 of air heat exchanger 8 It is connected, the high temperature air outlet 15 of air heat exchanger 8 is connected with burner 1, the flue gas pipeline and chilling of air preheater 8 The entrance of tower 9 is connected, and the outlet of chilling tower 9 is connected with the entrance of bag filter 10, the outlet of bag filter 10 with The entrance of extracting tower 11 is connected, and the outlet of extracting tower 11 is connected with the air inlet of air-introduced machine 2 18, and air-introduced machine 2 18 goes out Mouth is connected with chimney 16, volatility/half volatile organic contaminant pipeline and the air-introduced machine one of rotary kiln heat treatment system 3 4 air inlet is connected, and the air outlet of air-introduced machine 1 is connected with the entrance of cyclone separator 5, the heating of cyclone dust collectors 5 The air pipe line of contaminated soil is connected with high-temperature oxydation room 2, the dust pipeline of cyclone dust collectors 5 and soil pretreatment system Arrival end of 6 outlet respectively with feed system 7 is connected, the outlet of feed system 7 and the object of rotary kiln heat treatment system 3 Material entrance is connected, and the material outlet of rotary kiln heat treatment system 3 is connected with the entrance of soil moistening and lowering temperature device 12, soil The outlet of earth moistening and lowering temperature device 12 is connected with soil discharge system 13.
The air heat exchanger 8 is coiled air heat exchanger.
As shown in Fig. 2, the soil pretreatment system 6 is by vibrating screen 61, crusher 62, material mixing equipment 63, magnetic separation Separator 64, belted electronic balance 65 and control device 66 are formed, the material mixing equipment 63, Magnet Separater 64 and control Device 66 processed is connected respectively with belted electronic balance 65, the discharge port of vibrating screen 61 respectively with the feed inlet and material of crusher 62 The feed inlet of mixing apparatus 63 is connected, and the discharge port of crusher 62 is connected with the feed inlet of material mixing equipment 63.
After being sorted by vibrating screen 61, soil of the grain size more than 50mm, which enters in crusher 62, to be crushed, and grain size is less than 50 The soil of mm is then directly entered material mixing equipment 63.
As shown in figure 3, the soil moistening and lowering temperature device 12 is equipped with scrapper conveyor 121, scrapper conveyor 121 carries outer cover 122, outside Cover 122 is internally provided with spray head 123, and spray head 123 is connected with cooling water pipe 124.
Operation principle
The fossil fuels such as natural gas or liquefied petroleum gas surrounding air it is combustion-supporting under, by burner 1, in high temperature oxygen Change vigorous combustion in room 2 and release heat.After the outlet smoke temperature of high-temperature oxydation room 2 reaches certain temperature, from high-temperature oxydation room 2 In out a high-temperature flue gas part flow in rotary kiln heat treatment apparatus 3.At this point, organic material contaminated soil is located in advance in soil In reason system 6, by broken, screening, moisture content is adjusted and except iron etc. pre-processes link, by soil feed system 7, into returning In rotary kiln heat treatment apparatus 3.High-temperature flue gas and contaminated soil in rotary kiln heat treatment apparatus 3 reverse flow, fully connect It touches, organic pollution is gradually desorbed from contaminated soil and comes out.By air-introduced machine 1 formed negative pressure, organic pollution with Flue gas enters cyclone dust collectors 5, and most of particulate matter is separated, and then mixes feeding charging system again with contaminated soil In system 7, process is further processed.After cyclone dust collectors 5, the smoke backflow containing organic pollution to high temperature oxygen Change and high-temp combustion degradation is carried out in room 2, realize the thorough removing of pollutant.
At the same time, another strand of high-temperature flue gas come out from high-temperature oxydation room 2 enters in air heat exchanger 8, fresh air Under the action of air blower 17, by normal temperature air entrance 14, into tubular air heat exchanger 8.In air heat exchanger 8, Fresh air is in Bottomhole pressure, and high-temperature flue gas flows outside pipe, and by heat transfer process, the portion of energy in high-temperature flue gas is transmitted To fresh air so that air themperature increases, and enters in burner 1 by high temperature air outlet 15, auxiliary as combustion air Help combustion of fossil fuel.Flue gas after heat exchange is entered in chilling tower 9, is acted on by the rapid cooling of chilling tower 9, fast Speed is cooled to 200 DEG C hereinafter, avoid the generation temperature range of bioxin, effectively prevent the generation of bioxin.Flue gas after chilling Particulate matter is isolated into bag filter 10.After flue gas leaves bag filter 10, into extracting tower 11, spray into lye with Neutralize the acidic materials in flue gas.It is discharged into air by chimney 16 by the flue gas of extracting tower 11.Flue gas is housed on chimney 16 Real time on-line monitoring device can be continued to monitor through dirts such as carbon monoxide, sulfur dioxide, the nitrogen oxides in the flue gas of monitoring point The concentration of substance is contaminated, assist operators monitor exhaust emissions concentration in real time.When necessary, it can be installed before bag filter 10 Charcoal canister sprays into activated carbon into pipeline, realizes activated carbon and bag-type dust combination removing dioxin in flue gas, it is ensured that tail gas Middle harmful constituent and dust etc. reach discharge standard.It is discharged by the tail gas handled above eventually by chimney 16.
At the same time, through 3 thermal desorption of rotary kiln heat treatment apparatus, treated that high temperature soil passes through moistening and lowering temperature device It is cooled off after 12 processing, becomes clean soil after soil cooling and discharged from discharge system 13, gone out by the way of high-temperature closed Material, is transported to workshop to be checked, carries out examination to be checked.
The preferable specific embodiment of the above, only the utility model, these specific embodiments are all based on this Different realization methods under utility model general idea, and the scope of protection of the utility model is not limited thereto, it is any ripe It knows in the technical scope that those skilled in the art disclose in the utility model, the change or replacement that can be readily occurred in, all It should cover and be within the protection scope of the utility model.Therefore, the scope of protection of the utility model should be with claims Subject to protection domain.

Claims (4)

1. the organic polluted soil dystopy thermal desorption repair system that a kind of waste heat efficiently utilizes, including:Burner (1), high temperature oxygen Change room (2), rotary kiln heat treatment system (3), air-introduced machine one (4), cyclone dust collectors (5), soil pretreatment system (6), into Material system (7), air heat exchanger (8), chilling tower (9), bag filter (10), extracting tower (11), soil moistening and lowering temperature device (12), soil discharge system (13), normal temperature air entrance (14), high temperature air outlet (15), chimney (16), air blower (17) and Air-introduced machine two (18), which is characterized in that the burner (1) is connected with high-temperature oxydation room (2), the height of high-temperature oxydation room (2) Warm flue gas pipeline is connected respectively with rotary kiln heat treatment system (3) and air heat exchanger (8), the air outlet of air blower (17) It is connected with the normal temperature air entrance (14) of air heat exchanger (8), high temperature air outlet (15) and the burning of air heat exchanger (8) Device (1) is connected, and the flue gas pipeline of air preheater (8) is connected with the entrance of chilling tower (9), the outlet of chilling tower (9) with The entrance of bag filter (10) is connected, and the outlet of bag filter (10) is connected with the entrance of extracting tower (11), depickling The outlet of tower (11) is connected with the air inlet of air-introduced machine two (18), and the outlet of air-introduced machine two (18) is connected with chimney (16), The volatility of rotary kiln heat treatment system (3), half volatile organic contaminant pipeline are connected with the air inlet of air-introduced machine one (4) Logical, the air outlet of air-introduced machine one (4) is connected with the entrance of cyclone dust collectors (5), the heating contaminated soil of cyclone dust collectors (5) Air pipe line be connected with high-temperature oxydation room (2), the dust pipeline of cyclone dust collectors (5) and soil pretreatment system (6) Arrival end of the outlet respectively with feed system (7) be connected, outlet and the rotary kiln heat treatment system of feed system (7) (3) material inlet is connected, the material outlet of rotary kiln heat treatment system (3) and entering for soil moistening and lowering temperature device (12) Mouth is connected, and the outlet of soil moistening and lowering temperature device (12) is connected with soil discharge system (13).
2. the organic polluted soil dystopy thermal desorption repair system that waste heat according to claim 1 efficiently utilizes, feature It is, the air heat exchanger (8) is coiled air heat exchanger.
3. the organic polluted soil dystopy thermal desorption repair system that waste heat according to claim 2 efficiently utilizes, feature It is, the soil pretreatment system (6) is by vibrating screen (61), crusher (62), material mixing equipment (63), Magnet Separater (64), belted electronic balance (65) and control device (66) are formed, the material mixing equipment (63), Magnet Separater (64) with And control device (66) is connected respectively with belted electronic balance (65), the discharge port of vibrating screen (61) respectively with crusher (62) Feed inlet is connected with the feed inlet of material mixing equipment (63), the discharge port of crusher (62) and material mixing equipment (63) into Material mouth is connected.
4. the organic polluted soil dystopy thermal desorption repair system that waste heat according to claim 3 efficiently utilizes, feature It is, the soil moistening and lowering temperature device (12) is equipped with scrapper conveyor (121), and scrapper conveyor (121) is with outer cover (122), outer cover (122) spray head (123) is internally provided with, spray head (123) is connected with cooling water pipe (124).
CN201721586073.9U 2017-11-23 2017-11-23 The organic polluted soil dystopy thermal desorption repair system that a kind of waste heat efficiently utilizes Active CN207577115U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721586073.9U CN207577115U (en) 2017-11-23 2017-11-23 The organic polluted soil dystopy thermal desorption repair system that a kind of waste heat efficiently utilizes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721586073.9U CN207577115U (en) 2017-11-23 2017-11-23 The organic polluted soil dystopy thermal desorption repair system that a kind of waste heat efficiently utilizes

Publications (1)

Publication Number Publication Date
CN207577115U true CN207577115U (en) 2018-07-06

Family

ID=62733348

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721586073.9U Active CN207577115U (en) 2017-11-23 2017-11-23 The organic polluted soil dystopy thermal desorption repair system that a kind of waste heat efficiently utilizes

Country Status (1)

Country Link
CN (1) CN207577115U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107971330A (en) * 2017-11-23 2018-05-01 北京建工环境修复股份有限公司 The organic polluted soil dystopy thermal desorption repair system and method that waste heat efficiently utilizes
CN112387766A (en) * 2020-10-27 2021-02-23 国家电投集团远达环保工程有限公司重庆科技分公司 System and method for treating polluted soil by using waste heat of boiler
CN117003468A (en) * 2023-09-28 2023-11-07 珙县华洁危险废物治理有限责任公司成都分公司 Shale gas drilling oil sludge dry residue treatment device and system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107971330A (en) * 2017-11-23 2018-05-01 北京建工环境修复股份有限公司 The organic polluted soil dystopy thermal desorption repair system and method that waste heat efficiently utilizes
CN112387766A (en) * 2020-10-27 2021-02-23 国家电投集团远达环保工程有限公司重庆科技分公司 System and method for treating polluted soil by using waste heat of boiler
CN117003468A (en) * 2023-09-28 2023-11-07 珙县华洁危险废物治理有限责任公司成都分公司 Shale gas drilling oil sludge dry residue treatment device and system
CN117003468B (en) * 2023-09-28 2023-12-05 珙县华洁危险废物治理有限责任公司成都分公司 Shale gas drilling oil sludge dry residue treatment device and system

Similar Documents

Publication Publication Date Title
CN107971330A (en) The organic polluted soil dystopy thermal desorption repair system and method that waste heat efficiently utilizes
CN203578349U (en) Environment-friendly energy-saving organic polluted soil thermal desorption recovery treatment system
CN203869049U (en) Hazardous waste incineration system
US9718105B2 (en) Indirect thermal desorption device with two-section screw conveyors
WO2020041917A1 (en) Green cleaning-thermal desorption integrated technology treatment method and system for high-concentration petroleum sludge
CN103962374A (en) Environment-friendly and energy-saving thermal-desorption remediation treatment system for organic contaminated soil
CN104874593B (en) A kind of two-part indirect thermal desorption PROCESS FOR TREATMENT organic contamination indigenous method and equipment
CN110479748A (en) A kind of contaminated soil thermal desorption repair system and its method
CN212188526U (en) Flue gas treatment system after sludge treatment
CN105363770A (en) Sectional type heating and modular thermal desorption equipment for restoring organic contaminated soil and method
CN106140801A (en) A kind of restorative procedure of organic material contaminated soil
CN208527686U (en) A kind of indirect thermal desorption coupling and catalyzing degradation prosthetic device of contaminated soil classification
CN205650605U (en) Restore organic contaminated soil's sectional type heating, modularization thermal desorption equipment
CN111167847B (en) Novel ex-situ thermal desorption method and system for efficiently utilizing waste heat in cascade mode
CN207577115U (en) The organic polluted soil dystopy thermal desorption repair system that a kind of waste heat efficiently utilizes
CN212976286U (en) Rotary kiln type indirect heating combined heat storage tail gas incineration soil restoration device
CN102962249B (en) Remediation system and method for contaminated soil
CN110986575A (en) Thermal desorption energy-saving system and method for repairing polycyclic aromatic hydrocarbon contaminated soil
CN204247684U (en) The contaminated soil thermal desorption system of the efficient reuse of a kind of waste heat
CN105983570A (en) Electromagnetic thermal desorption remediation method and device used for remediating contaminated sites
KR101447918B1 (en) Green and Energy saving Cinerator
CN204583847U (en) Two-part auger indirect thermal desorption apparatus
CN205807439U (en) A kind of double RTO stove VOCs retracting device
CN107879585A (en) A kind of recycling sludge utilizes devices and methods therefor
CN102829642B (en) Furnace dust incineration processing method of calcium carbid furnace

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant