CN203578349U - Environment-friendly energy-saving organic polluted soil thermal desorption recovery treatment system - Google Patents

Environment-friendly energy-saving organic polluted soil thermal desorption recovery treatment system Download PDF

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CN203578349U
CN203578349U CN201320687239.1U CN201320687239U CN203578349U CN 203578349 U CN203578349 U CN 203578349U CN 201320687239 U CN201320687239 U CN 201320687239U CN 203578349 U CN203578349 U CN 203578349U
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China
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thermal desorption
tail gas
gas temperature
leads
discharge
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CN201320687239.1U
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Chinese (zh)
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杨勇
殷晓东
王海东
陈美平
黄海
王瑜瑜
农泽喜
崔朋
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中科华南(厦门)环保有限公司
北京鼎实环境工程有限公司
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Abstract

The utility model relates to an environment-friendly energy-saving organic polluted soil thermal desorption recovery treatment system and aims to provide an energy-saving, environment-friendly and high-efficiency organic polluted soil thermal desorption recovery treatment system. The environment-friendly energy-saving organic polluted soil thermal desorption recovery treatment system comprises a feed system, a thermal desorption system, a soil discharge system, a combustion and tail gas treatment system, a smoke temperature control system, a tail gas cooling and dust removing system, and a tail gas exhaust system, wherein the feed system is communicated with the thermal desorption system; the thermal desorption system is respectively communicated with the soil discharge system and the combustion and tail gas treatment system; the combustion and tail gas treatment system is communicated with the smoke temperature control system; the smoke temperature control system is communicated with the thermal desorption system; the thermal desorption system is communicated with the tail gas cooling and dust removing system; the tail gas cooling and dust removing system is communicated with the tail gas exhaust system.

Description

A kind of organic polluted soil thermal desorption restoration processing system of environmental protection and energy saving

Technical field

The utility model relates to soil remediation field, particularly relates to a kind of organic polluted soil thermal desorption restoration processing system.

Background technology

Thermal desorption technology is one of effective technology of repairing volatility/half volatile organic polluted soil, has successfully been applied to the reparation of the contaminated soils such as polycyclic aromatic hydrocarbon, non-chloro volatility and half volatile organic contaminant, benzene homologues, organic agricultural chemicals, herbicide.The improvement technique that domestic thermal desorption renovation technique is the earliest a kind of volatility and semi-volatile organic matter contaminated soil and device (ZL200410056888.7), the direct-fired mode of this process using low temperature can make soil comparatively be rapidly heated, but this system can not continuous feed, and treatment effeciency is on the low side; Tsing-Hua University's utility model the reverse direct heat hot desorption equipment of a kind of drum-type (ZL201010598161.7), adopt the mode of hot gas and soil adverse current, improved heat utilization efficiency, but because clean thermal current becomes dusty gas after mixing with the dusty gas in soil, virtually increased follow-up vent gas treatment load.Indirect thermal desorption device (CN101780467A) has adopted to be had double-deck rotary kiln soil is carried out to indirect, has reduced vent gas treatment amount, but the thermal source of this system is only for heating rotary kiln, and heat utilization efficiency is low.

Vent gas treatment technology is one of key technology of thermal desorption technology.The processing method of existing thermal desorption tail gas has dual firing chamber's combustion method, active carbon adsorption, organic solvent method for separating and recovering, ultraviolet catalytic/O 3oxidizing process, low-temperature plasma method etc.Active carbon adsorption and organic solvent method before processing all need high-temperature gas to lower the temperature, general wash cooling tower or the condenser of adopting lowered the temperature, because tail in thermal desorption process is large-minded, the high cost that causes lowering the temperature of temperature is high, efficiency is low, adsorb saturated active carbon and belong to hazardous waste, need to be transported to the general mechanism processing of relevant treatment qualification, transportation and processing formality complexity and cost are high.Ultraviolet catalytic/O 3oxidizing process mainly utilizes ultraviolet radiation to destroy pollutant, but ultraviolet light energy is lower, can only process organic gas simple and that be easily oxidized, as methyl mercaptan.Low temperature plasma has higher energy, can destroy the molecule of most organic gas, but this technology is mainly for processing gas at normal temperature, need to significantly lower the temperature, and equipment one-time investment is larger for the rotary kiln exhaust gas of high temperature.Dual firing chamber's combustion method is decomposing harmful substances thoroughly, and when tail gas is in furnace temperature >=1000 ℃, the time of staying >=2.0s, can reach 99.999% to the clearance of organic pollution; But dual firing chamber's combustion method energy consumption is large, according to general contaminated soil, process experience, in traditional thermal desorption system, dual firing chamber's energy consumption is approximately 1.5 times that rotary kiln heats energy consumption.Although dual firing chamber's combustion method treatment effeciency is high, huge energy consumption has limited the application of this method, is generally used for the vent gas treatment that organic gas content is high.

Utility model content

The technical problems to be solved in the utility model is to provide a kind of organic polluted soil thermal desorption restoration processing system of environmental protection and energy saving, comprise feed system, thermal desorption system, soil discharge system, burning and exhaust treatment system, flue gas temperature-controlling system, tail gas temperature-reduction dust-removal system and tail gas discharge system, described feed system leads to described thermal desorption system, described thermal desorption system is led to respectively soil discharge system and described burning and exhaust treatment system, described burning and exhaust treatment system lead to described flue gas temperature-controlling system, described flue gas temperature-controlling system leads to described thermal desorption system, described thermal desorption system is led to tail gas temperature-reduction dust-removal system, described tail gas temperature-reduction dust-removal system leads to tail gas discharge system.

Wherein said feed system leads to described thermal desorption system afterbody entrance, described soil discharge system and described burning and exhaust treatment system are led to respectively in described thermal desorption system head outlet, described flue gas temperature-controlling system leads to described thermal desorption system head entrance, described tail gas temperature-reduction dust-removal system is led in described thermal desorption system afterbody outlet, and described tail gas temperature-reduction dust-removal system leads to tail gas discharge system.

Wherein said thermal desorption system comprises Dual-barrel rotary kiln, described Dual-barrel rotary kiln is the double-barrel structure of inner/outer tube, described Dual-barrel rotary kiln is provided with inner core kiln head cover, inner core kiln hood, urceolus kiln head cover, urceolus kiln hood, described feed system leads to described inner core kiln hood, described soil discharge system is led in described inner core kiln head cover lower end, and described burning and exhaust treatment system are led in described inner core kiln head cover upper end; Described flue gas temperature-controlling system leads to described urceolus kiln head cover, and described urceolus kiln hood leads to described tail gas temperature-reduction dust-removal system, and described tail gas temperature-reduction dust-removal system leads to tail gas discharge system.

Wherein said Dual-barrel rotary kiln inner core inwall is provided with lifting blade, and outer tube inner wall is built alumina firebrick, and outer drum outer wall is laid one layer of heat preservation material.

Wherein also comprise monitoring system, described monitoring system is connected with described feed system, described thermal desorption system, described burning and exhaust treatment system, described flue gas temperature-controlling system, described tail gas temperature-reduction dust-removal system, described tail gas discharge system and described soil discharge system respectively, for monitoring inner each equipment running status.

Wherein said feed system comprises feeding bin, disintegrating machine, conveyer belt, steady feed bin and weighing balance, in described feeding bin, classifying screen is set, disintegrating machine is led in described feeding bin outlet, described conveyer belt is positioned at described classifying screen and described disintegrating machine below, described steady feed bin is set under described conveyer belt discharge end, described steady feed bin has weighing balance, and described weighing balance discharge end leads to described thermal desorption system.

Wherein said burning and exhaust treatment system comprise burner and combustion chamber, and described burner is connected with combustion chamber; Described burner is led in described thermal desorption system head outlet, and described combustor exit leads to described flue gas temperature-controlling system.

Wherein said soil discharge system comprises biaxial rneader, high-pressure spraying humidification apparatus and feed bin, described inner core kiln head cover leads to described biaxial rneader entrance, described high-pressure spraying humidifier is positioned at described biaxial rneader top, and described feed bin is led in described biaxial rneader outlet.

Wherein said tail gas temperature-reduction dust-removal system comprises cyclone dust collectors and spraying cooling cleaner, described thermal desorption system connects described cyclone dust collectors entrance, described cyclone dust collectors outlet connects described spraying cooling cleaner, and described spraying cooling cleaner connects described tail gas discharge system.

Wherein also comprise the high temperature wireway of high-temperature resistant thermal insulating material, described high temperature wireway is for being connected of thermal desorption system and described combustion gas and exhaust treatment system, flue gas temperature-controlling system, tail gas temperature-reduction dust-removal system and being connected of burning and exhaust treatment system and described flue gas temperature-controlling system.

The utility model difference from prior art is that the utility model obtained following technique effect:

1, the utility model proposes a kind of thermal desorption system of utilizing rotary kiln thermal source to process the organic gas of thermal desorption process generation, thereby saved the huge dual firing chamber's system of energy consumption, significantly reduced the energy consumption of system;

2, the indirect Dual-barrel rotary kiln that the utility model provides, can reduce the treating capacity of organic exhaust gas;

3, Dual-barrel rotary kiln outer tube inner wall and outer wall are all laid heat-barrier material, have reduced scattering and disappearing of heat, have improved the utilization rate of heat;

4, the soil discharge system that the utility model provides, can, to high temperature earth material cooling, dust preventing, adjusting moisture, be convenient to follow-up transportation backfill or utilization;

5, in native system, vent gas treatment adopts spray column equipment, and spray process can and be removed fine dusts particle and sour gas (NOx, the SO in tail gas to high-temperature tail gas cooling 2), guarantee tail gas qualified discharge;

6, native system whole process has monitoring system automatically to detect the running status of each equipment, has realized the automation control of system.

Below in conjunction with accompanying drawing, the utility model is described in further detail.

Accompanying drawing explanation

Fig. 1 is the organic polluted soil thermal desorption restoration processing system block diagram of the utility model environmental protection and energy saving;

Fig. 2 is the structural representation of the organic polluted soil thermal desorption restoration processing system of the utility model environmental protection and energy saving.

Description of reference numerals: 1-feed system; 2-thermal desorption system; 3-burning and exhaust treatment system; 4-tail gas temperature-reduction dust-removal system; 5-tail gas discharge system; 6-soil discharge system; 7-flue gas temperature-controlling system; 8-monitoring system; 9-feeding bin; 10-classifying screen; 11-disintegrating machine; The steady feed bin of 12-; 13-weighing balance; 14-Dual-barrel rotary kiln; 15-inner core kiln hood; 16-urceolus kiln hood; 17-urceolus kiln head cover; 18-inner core kiln head cover; 19-combustion chamber; 20-baffle plate; 21-burner; 22-air exhauster; 23-flue gas temperature controlling instruments; 24-cyclone dust collectors; 25-spray column; 26-demister; 27-spray thrower; 28-filler; 29-circular water treating system; 30-alkali lye feeding mechanism; 31-exhaust blower; 32-chimney; 33-biaxial rneader; 34-water jet; 35-water supply pressurized equipment; 36-feed bin; 37-combustion gas; 38-combustion air; 39-cold air.

The specific embodiment

Below in conjunction with drawings and Examples, technical characterictic and the advantage with other above-mentioned to the utility model are described in more detail.

The utility model provides a kind of soil indirect thermal desorption system of environmental protection and energy saving.As shown in Figure 1, this system comprises feed system 1, thermal desorption system 2, burning and exhaust treatment system 3, tail gas temperature-reduction dust-removal system 4, tail gas discharge system 5, soil discharge system 6, flue gas temperature-controlling system 7, monitoring system 8.Wherein feed system 1 leads to thermal desorption system 2, thermal desorption system 2 is led to respectively soil discharge system 6 and burning and exhaust treatment system 3, burning and exhaust treatment system 3 lead to flue gas temperature-controlling system 7, flue gas temperature-controlling system 7 leads to thermal desorption system 2, thermal desorption system 2 is led to tail gas temperature-reduction dust-removal system 4, and tail gas temperature-reduction dust-removal system 4 leads to tail gas discharge system 5.Monitoring system 8 connects respectively feed system 1, thermal desorption system 2, burning and exhaust treatment system 3, tail gas temperature-reduction dust-removal system 4, tail gas discharge system 5, soil discharge system 6 and flue gas temperature-controlling system 7, realizes the each equipment running status of monitoring in real time; High temperature wireway is connected and burning and exhaust treatment system and use the high temperature wireway connection of high temperature thermal insulation material being connected of described flue gas temperature-controlling system for thermal desorption system and described combustion gas and exhaust treatment system, flue gas temperature-controlling system, tail gas temperature-reduction dust-removal system.

As described in Figure 2, feed system 1 is comprised of feeding bin 9, classifying screen 10, disintegrating machine 11, steady feed bin 12 and weighing balance 13 and belt conveyor.The soil types that thermal desorption system 2 can be processed comprises clay, sand, silty clay etc., and soil moisture content should be less than 20%.First pending contaminated soil is admitted to feeding bin 9, through the screening of classifying screen 10 in feeding bin 9, oversize is admitted to disintegrating machine 11 fragmentations, screenings and broken rear soil enter the conveyer belt that is positioned at classifying screen 10 and disintegrating machine 11 belows, be brought into the steady feed bin 12 of conveyer belt discharge end, soil is through being positioned at the weighing balance 13 of steady feed bin 12 belows, and enter thermal desorption system 2 by weighing balance 13 discharge ends, weighing balance 13 can be recorded the soil weight that enters Dual-barrel rotary kiln 14, the treating capacity that enters Dual-barrel rotary kiln 14 by be connected with monitoring system 8 Real-Time Monitoring control.

Thermal desorption system 2 comprises Dual-barrel rotary kiln 14, and Dual-barrel rotary kiln 14 is comprised of inner core kiln hood 15, urceolus kiln hood 16, urceolus kiln head cover 17 and inner core kiln head cover 18.Dual-barrel rotary kiln 14 is indirect Dual-barrel rotary kiln 14, enters the inner core of Dual-barrel rotary kiln 14 through the soil of weighing balance 13 discharging openings through inner core kiln hood 15, and urceolus is thermal current, and kiln cylinder and ground are 3-5 ° of angle.The lifting blade of different angles and spacing is housed in Dual-barrel rotary kiln 14 inner cores, can guarantee in Dual-barrel rotary kiln 14 rotation processes, soil can fully disperse and by kiln Caudad kiln hood, be moved under Action of Gravity Field, thereby make soil in cylinder, have enough time of staying and sufficient decentralization, so as soil in inner core with urceolus in thermal current carry out sufficient heat exchange.In general, the time of staying of soil in rotary kiln is 20 ± 10min, can control the soil time of staying by the rotating speed of Dual-barrel rotary kiln 14.

Because native system thermal desorption system 2 can share a thermal source with vent gas treatment, therefore thermal desorption system 2 and burning and exhaust treatment system 3 can be connected together, inner core kiln head cover 18 gas outlets, upper end connect burner 21 air intakes of burning and exhaust treatment system 3, soil in Dual-barrel rotary kiln 14 is through the heating of thermal current in urceolus, volatility/half volatile organic gas evaporates, the organic pollutant volatilizing by the upper end wireway of inner core kiln head cover 18 and through the booster action of air exhauster 22 enter burning and exhaust treatment system 3 in, in, the burner 21 of outer triple channel structure, organic pollutant is transported in combustion chamber 19 and decomposes and destroy under thermal-flame, 19 gas outlets, combustion chamber connect the flue gas temperature controlling instruments 23 of flue gas temperature-controlling system 7, flue gas temperature controlling instruments 23 connects urceolus kiln head cover 17, and the thermal current that the interior flame combustion in combustion chamber 19 produces controls to after preference temperature by high temperature wireway and is delivered in the urceolus of Dual-barrel rotary kiln 14 and heats soil in inner core through flue gas temperature controlling instruments 23 and by cold air 39.

For guaranteeing that volatility/half volatile organic gas is at high temperature decomposed into CO completely 2and H 2o removes, and the temperature in combustion chamber 19 need remain on >2s burning time of 1000-1300 ℃ and organic pollutant.The interior temperature in combustion chamber 19 can be by the temperature of the intake control combustion flame of the adjusting interior combustion gas 37 of burner 21 and combustion air 38; Combustion chamber 19 utilizes two baffle plates 20 to be set to S type structure, under 31 effects of outside exhaust blower, air-flow along S type path flows and in combustion chamber time of staying >2s, to guarantee that organic pollutant is thoroughly decomposed.

Combustion chamber 19 gas outlet flue-gas temperatures, generally 1000 ℃ of left and right, blast cold air 39 by flue gas temperature controlling instruments 23 and lower the temperature, and the temperature of controlling as required thermal current is controlled at 400-800 ℃ of scope.Thermal current is entered Dual-barrel rotary kiln 14 urceolus and is full of whole urceolus by high temperature wireway, and under the effect of exhaust blower 31, thermal current is moving to kiln wake flow by kiln hood; Due to the continuous supply of thermal current and outflow, hot stream temperature is stable, and in Dual-barrel rotary kiln 14 urceolus, thermal current just can be used as the stable thermal source heating soil of inner core.The heating-up temperature of Dual-barrel rotary kiln 14 can be determined according to the kind of the organic pollutant in soil, conventionally soil can be heated to 200-600 ℃, generally can all half volatilization/volatile organic matters of desorption at this temperature.In Dual-barrel rotary kiln 14, thermal current is constantly moving to kiln wake flow by kiln hood in rotary kiln urceolus, has guaranteed the stable of thermal source, and material flows and air-flow is reverse flow, has improved heat exchanger effectiveness.

Tail gas temperature-reduction dust-removal system 4 comprises cyclone dust collectors 24 and spraying cooling cleaner, the main particle that diameter is greater than 6 μ m, i.e. the bulky grain thing in tail gas removed of cyclone dust collectors 24.Described spraying cooling cleaner comprises spray column 25, circular water treating system 29 and alkali lye feeding mechanism 30, urceolus tail kiln hood 16 connects cyclone dust collectors 24 air intakes, cyclone dust collectors 24 gas outlets, top connect spray column 25 below air inlets, and spray column 25 is comprised of demister 26, spray thrower 27 and filler 28.Tail gas enters tower from the air inlet of spray column 25 belows, by tower top exhaust outlet, is discharged.Spray thrower 27 adopts alkali lye circulated sprinkling to lower the temperature to high-temperature gas; Meanwhile, spray alkali lye and filler 28 form moisture film, and moisture film can be removed the fine particle thing in tail gas on the one hand, and alkali lye can absorb the sour gas (SO in tail gas on the other hand 2, NO xdeng), guarantee the qualified discharge of tail gas.Circular water treating system 29 is for impurity such as cooling to the circulating water cooling of spray column 25 belows discharges, to remove described recirculated water particles; Alkali lye feeding mechanism 30 can be by detecting the acid-base value configuration alkali lye of recirculated water, for the alkali lye spray of spray column 25; Spray liquid in spray column 25 recycles, and has saved water resource.In addition, spray column 25 exhaust outlets are equipped with demister 26, water smoke of carrying secretly in the tail gas of demister 26 after can Transformatin etc., and the tail gas of guaranteeing to enter tail gas discharge system 5 is up to standard.

Tail gas discharge system 5 comprises exhaust blower 31 and chimney 32, and exhaust blower 31 one end are connected with spray thrower 27 tower top exhaust outlets, and the other end connects chimney 32, and tail gas acts on after tail gas is entered to chimney 32 and enters atmosphere through exhaust blower 31 after tail gas temperature-reduction dust-removal system 4 is processed.

Soil discharge system 6 joins with the inner core kiln head cover 18 lower end discharging opening funnels of Dual-barrel rotary kiln 14, in inner core, soil after treatment enters in biaxial rneader 33 by inner core kiln head cover 18 lower end discharging opening funnels under Action of Gravity Field, biaxial rneader 33 tops are provided with steel dust cap, outside is provided with guard rail, and the personnel of preventing scald; Steel dust cap inner tip is equipped with water jet 34, water jet 34 is provided with some shower nozzles for spraying cooling, in biaxial rneader 33 outsides, be provided with water supply high-tension apparatus 35, by high-pressure spraying, earth material is lowered the temperature, and stir and make earth material water content even, by controlling spray flux, make to be less than 100 ℃ from the soil moisture of the end discharge of biaxial rneader 33, be convenient to soil and enter conveyer belt entrucking, finally be transported to feed bin 36 entruckings, carry out backfill or other processing.

The combustion gas inlet of burner 21 can be by fuel gas supply equipment control, by controlling combustion gas 37 admission velocity control firepower sizes; By controlling the intake velocity of combustion air 38, guaranteeing has enough hot gas for providing thermal current to Dual-barrel rotary kiln 14 in oxygen supply abundance and combustion chamber 19; Temperature sensing device is equipped with in combustion chamber 19, can detect the temperature in combustion chamber 19; Dual-barrel rotary kiln 14 can be by rotating speed control earth material the processing time of staying in kiln; The discharging opening of the inner core kiln head cover 18 of Dual-barrel rotary kiln 14 is provided with Temperature Detector, detects in real time the temperature of discharging earth material; At biaxial rneader 33 afterbodys, earth material Temperature Detector is set, for determining the control of the injection flow rate in biaxial rneader 33; Tail gas discharge system 5 is provided with tail gas checkout equipment, detects in real time tail gas, guarantees tail gas qualified discharge.The detection of above part all connects monitoring system 8, and the running status of the central control system complete monitoring each several part by monitoring system 8 realizes fault alarm and automatically controls.

Silt and silty clay that the polycyclic aromatic hydrocarbon (PAHs) that the utility model device processes main component is naphthalene as utilized pollutes, total concentration is 1700mg/kg, soil moisture content <20%.Because the boiling point of PAHs is generally 200-550 ℃, in rotary kiln soil need to be heated to that their boiling point is above can pollutant, from soil, desorption be out.

First, pending contaminated soil enters feeding bin 9, through classifying screen 10 and disintegrating machine 11, processes soil particle <1cm, then soil, through steady feed bin 12, weighing balance 13, is entered in rotary kiln inner core 14 by the inner core kiln hood 15 upper end charging apertures of Dual-barrel rotary kiln 14.As shown in Figure 2, the thermal current in inner core in soil and urceolus keeps reverse flow, and hot stream temperature is 750 ℃ of left and right, and inner core soil is heated to 500-600 ℃.Soil stops 20min in inner core, can remove more than 97% polycyclic aromatic hydrocarbon.Soil through thermal desorption is entered in biaxial rneader 33 by inner core kiln head cover 18 lower end funnels, by high-pressure water jet 34, to soil, cooling adds wet process, and control and from biaxial rneader 33, give off soil moisture <100 ℃, be convenient to the entrucking transportation backfill of soil etc.

The dusty gas that Dual-barrel rotary kiln 14 inner core soil desorptions go out is imported in burner 21 by air exhauster 22, the burning in combustion chamber 19 that coexists of combustion gas 37, combustion air 38 and dusty gas one, combustion flame temperature is 1000-1300 ℃, PAHs is time of staying >2s at this temperature, and its clearance reaches 99.9%.High-temperature flue gas (1000 ℃ of left and right) in combustion chamber 19 first adjusts the temperature to 700-800 ℃ through flue gas temperature controlling instruments 23, then by high-temperature pipe, is delivered to the urceolus kiln head cover 17 of Dual-barrel rotary kiln 14, as the thermal source of soil heating in inner core.In Dual-barrel rotary kiln 14 urceolus, high-temperature flue gas is discharged from urceolus kiln hood 16, enters tail gas temperature-reduction dust-removal system 4 and processes, and after detection vent gas treatment is qualified, enters atmosphere.

If whole system sealing is good, soil can all be recycled, and treating capacity is 10t/h, and the clearance of PAHs is between 97-99.9%.

Above-described embodiment is described preferred embodiment of the present utility model; not scope of the present utility model is limited; do not departing under the prerequisite of the utility model design spirit; various distortion and improvement that those of ordinary skills make the technical solution of the utility model, all should fall in the definite protection domain of the utility model claims.

Claims (10)

1. the organic polluted soil thermal desorption restoration processing system of environmental protection and energy saving, it is characterized in that: comprise feed system, thermal desorption system, soil discharge system, burning and exhaust treatment system, flue gas temperature-controlling system, tail gas temperature-reduction dust-removal system and tail gas discharge system, described feed system leads to described thermal desorption system, described thermal desorption system is led to respectively soil discharge system and described burning and exhaust treatment system, described burning and exhaust treatment system lead to described flue gas temperature-controlling system, described flue gas temperature-controlling system leads to described thermal desorption system, described thermal desorption system is led to tail gas temperature-reduction dust-removal system, described tail gas temperature-reduction dust-removal system leads to tail gas discharge system.
2. the organic polluted soil thermal desorption restoration processing system of environmental protection and energy saving according to claim 1, it is characterized in that: described feed system leads to described thermal desorption system afterbody entrance, described soil discharge system and described burning and exhaust treatment system are led to respectively in described thermal desorption system head outlet, described flue gas temperature-controlling system leads to described thermal desorption system head entrance, described tail gas temperature-reduction dust-removal system is led in described thermal desorption system afterbody outlet, and described tail gas temperature-reduction dust-removal system leads to tail gas discharge system.
3. the organic polluted soil thermal desorption restoration processing system of environmental protection and energy saving according to claim 2, it is characterized in that: described thermal desorption system comprises Dual-barrel rotary kiln, described Dual-barrel rotary kiln is the double-barrel structure of inner/outer tube, described Dual-barrel rotary kiln is provided with inner core kiln head cover, inner core kiln hood, urceolus kiln head cover, urceolus kiln hood, described feed system leads to described inner core kiln hood, described soil discharge system is led in described inner core kiln head cover lower end, and described burning and exhaust treatment system are led in described inner core kiln head cover upper end; Described flue gas temperature-controlling system leads to described urceolus kiln head cover, and described urceolus kiln hood leads to described tail gas temperature-reduction dust-removal system, and described tail gas temperature-reduction dust-removal system leads to tail gas discharge system.
4. the organic polluted soil thermal desorption restoration processing system of environmental protection and energy saving according to claim 3, is characterized in that: described Dual-barrel rotary kiln inner core inwall is provided with lifting blade, and outer tube inner wall is built alumina firebrick, and outer drum outer wall is laid one layer of heat preservation material.
5. the organic polluted soil thermal desorption restoration processing system of environmental protection and energy saving according to claim 1, it is characterized in that: also comprise monitoring system, described monitoring system is connected with described feed system, described thermal desorption system, described burning and exhaust treatment system, described flue gas temperature-controlling system, described tail gas temperature-reduction dust-removal system, described tail gas discharge system and described soil discharge system respectively, for monitoring inner each equipment running status.
6. the organic polluted soil thermal desorption restoration processing system of environmental protection and energy saving according to claim 1, it is characterized in that: described feed system comprises feeding bin, disintegrating machine, conveyer belt, steady feed bin and weighing balance, in described feeding bin, classifying screen is set, disintegrating machine is led in described feeding bin outlet, described conveyer belt is positioned at described classifying screen and described disintegrating machine below, described steady feed bin is set under described conveyer belt discharge end, described steady feed bin has weighing balance, and described weighing balance discharge end leads to described thermal desorption system.
7. the organic polluted soil thermal desorption restoration processing system of environmental protection and energy saving according to claim 1, is characterized in that: described burning and exhaust treatment system comprise burner and combustion chamber, described burner is connected with combustion chamber; Described burner is led in described thermal desorption system head outlet, and described combustor exit leads to described flue gas temperature-controlling system.
8. the organic polluted soil thermal desorption restoration processing system of environmental protection and energy saving according to claim 3, it is characterized in that: described soil discharge system comprises biaxial rneader, high-pressure spraying humidification apparatus and feed bin, described inner core kiln head cover leads to described biaxial rneader entrance, described high-pressure spraying humidifier is positioned at described biaxial rneader top, and described feed bin is led in described biaxial rneader outlet.
9. the organic polluted soil thermal desorption restoration processing system of environmental protection and energy saving according to claim 1, it is characterized in that: described tail gas temperature-reduction dust-removal system comprises cyclone dust collectors and spraying cooling cleaner, described thermal desorption system connects described cyclone dust collectors entrance, described cyclone dust collectors outlet connects described spraying cooling cleaner, and described spraying cooling cleaner connects described tail gas discharge system.
10. the organic polluted soil thermal desorption restoration processing system of environmental protection and energy saving according to claim 5, it is characterized in that: also comprise the high temperature wireway of high-temperature resistant thermal insulating material, described high temperature wireway is for being connected of thermal desorption system and described burning and exhaust treatment system, flue gas temperature-controlling system, tail gas temperature-reduction dust-removal system and being connected of burning and exhaust treatment system and described flue gas temperature-controlling system.
CN201320687239.1U 2013-11-01 2013-11-01 Environment-friendly energy-saving organic polluted soil thermal desorption recovery treatment system CN203578349U (en)

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CN103962374A (en) * 2013-11-01 2014-08-06 中科华南(厦门)环保有限公司 Environment-friendly and energy-saving thermal-desorption remediation treatment system for organic contaminated soil
CN104226681A (en) * 2014-09-17 2014-12-24 杭州大地环保工程有限公司 Device and method for indirect thermal desorption disposal of persistent organic pollutant contaminated soil
CN104307864A (en) * 2014-11-11 2015-01-28 常州宝利环保科技有限公司 Remediation method of organic contaminated soil
CN104438311A (en) * 2014-11-11 2015-03-25 武汉都市环保工程技术股份有限公司 Thermal-sensitivity contaminant contaminated soil thermal drive desorption repair system
CN104438313A (en) * 2014-11-21 2015-03-25 中冶赛迪工程技术股份有限公司 Contaminated soil thermal desorption system capable of efficiently recycling waste heat and method adopting contaminated soil thermal desorption system
CN104607455A (en) * 2015-02-06 2015-05-13 中国科学院武汉岩土力学研究所 Multi-stage thermal desorption remediation system for organic polluted soil
CN104646409A (en) * 2015-02-03 2015-05-27 郭华 Two-section type rotary kiln indirect heat desorption device
CN104741372A (en) * 2015-03-18 2015-07-01 中国环境科学研究院 Novel thermal desorption restoring system and novel thermal desorption restoring method for treating POPs (persistent organic pollutants) polluted soil
CN104785515A (en) * 2015-04-27 2015-07-22 沈逍江 Two-section auger indirect thermal desorption device
CN104785512A (en) * 2015-03-26 2015-07-22 重庆太湖锅炉股份有限公司 Contaminated soil remediation system
CN105080958A (en) * 2015-10-10 2015-11-25 中石化炼化工程(集团)股份有限公司 Classified thermal desorption repair system and technology of organic contaminated soil
CN105363770A (en) * 2015-12-17 2016-03-02 上海康恒环境股份有限公司 Sectional type heating and modular thermal desorption equipment for restoring organic contaminated soil and method
CN106077066A (en) * 2015-11-24 2016-11-09 江苏安琪尔废气净化有限公司 The system and method for flow-type energy-conservation LTTD RCO renovation of organic pollution soil
CN109539288A (en) * 2018-11-13 2019-03-29 西安文理学院 A kind of prosthetic device and restorative procedure of oil pollution alkaline land soil
CN111069262A (en) * 2019-12-27 2020-04-28 天津大学 Phase change heat transfer soil thermal remediation system
WO2020168875A1 (en) * 2019-02-22 2020-08-27 杰瑞环保科技有限公司 Rotary indirect thermal desorption device and system

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103962374A (en) * 2013-11-01 2014-08-06 中科华南(厦门)环保有限公司 Environment-friendly and energy-saving thermal-desorption remediation treatment system for organic contaminated soil
CN104226681A (en) * 2014-09-17 2014-12-24 杭州大地环保工程有限公司 Device and method for indirect thermal desorption disposal of persistent organic pollutant contaminated soil
CN104307864A (en) * 2014-11-11 2015-01-28 常州宝利环保科技有限公司 Remediation method of organic contaminated soil
CN104438311A (en) * 2014-11-11 2015-03-25 武汉都市环保工程技术股份有限公司 Thermal-sensitivity contaminant contaminated soil thermal drive desorption repair system
CN104438313A (en) * 2014-11-21 2015-03-25 中冶赛迪工程技术股份有限公司 Contaminated soil thermal desorption system capable of efficiently recycling waste heat and method adopting contaminated soil thermal desorption system
CN104646409A (en) * 2015-02-03 2015-05-27 郭华 Two-section type rotary kiln indirect heat desorption device
CN104607455A (en) * 2015-02-06 2015-05-13 中国科学院武汉岩土力学研究所 Multi-stage thermal desorption remediation system for organic polluted soil
CN104607455B (en) * 2015-02-06 2016-11-16 中国科学院武汉岩土力学研究所 A kind of organic polluted soil Multi-stage heat desorption repair system
CN104741372A (en) * 2015-03-18 2015-07-01 中国环境科学研究院 Novel thermal desorption restoring system and novel thermal desorption restoring method for treating POPs (persistent organic pollutants) polluted soil
CN104785512A (en) * 2015-03-26 2015-07-22 重庆太湖锅炉股份有限公司 Contaminated soil remediation system
WO2016173448A1 (en) * 2015-04-27 2016-11-03 沈逍江 Two-section auger indirect thermal desorption device
CN104785515A (en) * 2015-04-27 2015-07-22 沈逍江 Two-section auger indirect thermal desorption device
CN105080958A (en) * 2015-10-10 2015-11-25 中石化炼化工程(集团)股份有限公司 Classified thermal desorption repair system and technology of organic contaminated soil
CN106077066A (en) * 2015-11-24 2016-11-09 江苏安琪尔废气净化有限公司 The system and method for flow-type energy-conservation LTTD RCO renovation of organic pollution soil
CN105363770A (en) * 2015-12-17 2016-03-02 上海康恒环境股份有限公司 Sectional type heating and modular thermal desorption equipment for restoring organic contaminated soil and method
CN109539288A (en) * 2018-11-13 2019-03-29 西安文理学院 A kind of prosthetic device and restorative procedure of oil pollution alkaline land soil
WO2020168875A1 (en) * 2019-02-22 2020-08-27 杰瑞环保科技有限公司 Rotary indirect thermal desorption device and system
CN111069262A (en) * 2019-12-27 2020-04-28 天津大学 Phase change heat transfer soil thermal remediation system

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