CN214022589U - Indirect thermal desorption soil remediation device for heat pipe enhanced heat storage - Google Patents
Indirect thermal desorption soil remediation device for heat pipe enhanced heat storage Download PDFInfo
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- CN214022589U CN214022589U CN202022922893.9U CN202022922893U CN214022589U CN 214022589 U CN214022589 U CN 214022589U CN 202022922893 U CN202022922893 U CN 202022922893U CN 214022589 U CN214022589 U CN 214022589U
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- 238000005067 remediation Methods 0.000 title claims description 10
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Abstract
The utility model discloses an indirect thermal desorption soil prosthetic devices of heat accumulation is reinforceed to heat pipe, this prosthetic devices include thermal desorption reactor, dust remover, heated air circulation fan and hot air heater, thermal desorption reactor and dust remover, heated air circulation fan, hot air heater link to each other in proper order and constitute the heated air circulation return circuit, burner links to each other in proper order with hot air heater, chimney and constitutes the flue gas passageway, tail gas purification device links to each other in proper order with draught fan, aiutage and constitutes the tail gas purification passageway. The device utilizes the soil to be heated and volatilizes the thermal desorption gas that self produced as the heat transfer medium, through the mode of circulation heating, has both realized hot-blast and the high-efficient heat transfer of soil contact, and equipment throughput is strong, keeps high temperature flue gas simultaneously again not with soil direct contact, has avoided high temperature flue gas and gaseous state organic pollutant to mix, only has a small amount of unnecessary gas to need purification treatment, and the equipment scale is little.
Description
Technical Field
The utility model belongs to the technical field of pollute place soil restoration, be applicable to the restoration of organic contaminated place soil, concretely relates to heat pipe reinforces indirect thermal desorption soil prosthetic devices of heat accumulation.
Background
The soil is a loose surface layer which has fertility and can grow plants on the surface of the land, when harmful substances discharged into the soil exceed the self-cleaning capacity of the soil, the composition, the structure and the function of the soil are changed, the activity of microorganisms is inhibited, the harmful substances or decomposition products thereof are gradually accumulated in the soil and absorbed by the human body through the soil → the plants → the human body or through the soil → water → the human body indirectly, and the soil pollution is generated to the extent of harming the health of the human body.
The current seriously polluted sites mainly comprise chemical plants, pesticide plants, smelting plants, gas stations, chemical storage tanks and the like, the pollutants of the sites mainly comprise organic pollution, and the sites can be divided into volatile organic compounds, semi-volatile organic compounds, persistent organic compounds, pesticides and the like according to the difference of the melting boiling points of the volatile organic compounds, the semi-volatile organic compounds, the persistent organic compounds and the like. The polluted soil restoration technology comprises incineration (cement kiln cooperative treatment), phytoremediation, bioremediation, chemical remediation, thermal desorption and the like, wherein the thermal desorption technology has the advantages of high treatment efficiency, short restoration period, movable device and the like, is widely applied to restoration of volatile/semi-volatile organic polluted sites, and is one of the main site restoration technologies, wherein the thermal desorption accounts for 20-30% in European and American site restoration cases, as shown by American EPA statistics.
The thermal desorption technology is that high-temperature flue gas generated by combustion is directly or indirectly heated to heat the polluted soil to be higher than a target temperature, and organic pollutants are selectively gasified and volatilized by controlling the system temperature and the material retention time, so that the organic pollutants are separated and removed from soil particles.
The polluted soil is distributed all over the country, and the equipment needs to be frequently disassembled and assembled to replace the use field so as to realize the repeated utilization of the equipment. Considering the installation, transportation and disassembly of equipment, skid-mounted unitized integration is required, and the size of a single structure is generally not more than 3m multiplied by 12 m. Meanwhile, the soil to be repaired in a general polluted site is few thousands of tons and many tens of thousands of tons, and the repaired land is in urgent need of real estate development, so that the repair equipment is required to be high in treatment efficiency and strong in capacity so as to shorten the repair period. Therefore, the more the limited space size is used, the higher the equipment processing capacity is, and the more advantageous the cost reduction and the construction period reduction are. The thermal desorption treatment capacity is limited mainly by the thermal desorption reactor, and the improvement of the heat transfer capacity of the reactor in unit volume has important significance based on the thermal desorption heat transfer characteristic.
At present, the heating mode of high-temperature flue gas and soil is different, and the technology is divided into two technologies of direct thermal desorption and indirect thermal desorption.
Application number is CN201010598161.7 reverse thermal desorption system of organic matter contaminated soil drum-type, including soil charge-in system, heat source system links to each other with reverse thermal desorption system, reverse thermal desorption system in proper order with dust pelletizing system, a cooling system, activated carbon adsorption system links to each other, above-mentioned subsystem control end and control system are connected, make the reverse thermal desorption cylinder of hot-air entering through ignition system, contaminated soil gets into reverse thermal desorption cylinder through soil conveyor, hot-air and the reverse contact of soil, heat its organic pollutant who contains, make it volatilize. The rotary thermal desorption kiln, the device and the process for thermal desorption of organic contaminated soil with the application number of CN201910814270.9 comprise a thermal desorption cavity for containing and thermally desorbing the organic contaminated soil and a combustion chamber for burning organic gas generated by thermal desorption, wherein the thermal desorption cavity and the combustion chamber are independently separated chambers in the thermal desorption rotary thermal desorption kiln; and a gas channel is communicated between the heat desorption cavity and the combustion chamber and penetrates through the kiln head cover and the kiln tail cover. These two patents disclose a typical direct thermal desorption structure system, in which although the hot gas and the contaminated soil are in reverse contact in the thermal desorption drum, only one way of contact heat transfer is provided, the heat transfer channel is single, and the heat transfer capacity per unit volume of the reactor is not high. The high-temperature flue gas and the gas generated by heating the soil are mixed together, the amount of tail gas to be purified is very large, and a large amount of tail gas needs to be treated at the high temperature of 1100-1200 ℃ through a secondary combustion chamber, so that the treatment process is long, the equipment scale is large, the energy consumption is high, and the investment cost and the use cost are very high.
Application number is CN201920224738.4 indirect thermal desorption device of rotation and system, including kiln head, kiln tail, gyration barrel, burning chamber, feed inlet, discharge gate, chimney, kiln head, gyration barrel, kiln tail connect gradually, and the burning chamber cover is established on gyration barrel, and the chimney is established on burning chamber, and the feed inlet is established on the kiln head, and the discharge gate is established on the kiln tail, still is equipped with the gas vent on the kiln head, and the bottom in burning chamber is equipped with a plurality of combustors. Application number is CN201721044803.2 external heating formula thermal desorption rotary kiln, including mutual airtight isolated boiler tube and furnace, boiler tube one end is the feed end, and the other end is the discharge end, the furnace cladding is in outside between the both ends of boiler tube, to the boiler tube provides the heat. Application number is CN201510207851.8 indirect thermal desorption device of two segmentation auger, including last sledge and the lower sledge of arranging from top to bottom, upward be equipped with upper strata thermal desorption room in the sledge, the feeder hopper, the feeding air locker, the air preheater, the air-blower, first rapid cooling spray column, second rapid cooling spray column, defogging tower and draught fan, be equipped with lower floor's thermal desorption room in the sledge down, the active carbon filters the jar, the combustion chamber, go out hopper and ejection of compact air locker, be equipped with first auger in the upper strata thermal desorption room, upper strata thermal desorption room outside cover has upper flue gas to press from both sides the cover, be equipped with the second auger in the lower floor's thermal desorption room, lower floor's thermal desorption room outside cover has lower floor's flue gas to press from both sides the cover. These three patents disclose typical indirect thermal desorption systems and reactor configurations, which, although a skid-mounted unitized integration is achieved, only transfer heat from the high temperature flue gas to the contaminated soil through the reactor shell, and the heat transfer capacity per unit volume of the reactor is low. Particularly, the heat transfer area is small and the heat transfer efficiency is low due to the limitation of an indirect heat transfer principle and the equipment scale, and the treatment capacity of the equipment is only about 3 to 4 tons per hour generally.
SUMMERY OF THE UTILITY MODEL
The utility model provides an indirect thermal desorption soil restoration device and method for heat pipe enhanced heat storage aiming at the defects existing in the prior art.
The purpose of the utility model can be realized by the following technical scheme:
the utility model provides an indirect thermal desorption soil prosthetic devices of heat pipe intensive heat accumulation, this prosthetic devices includes thermal desorption reactor, dust remover, heated air circulation fan and hot air heater, thermal desorption reactor and dust remover, heated air circulation fan, hot air heater link to each other in proper order and constitute the heated air circulation return circuit, burner links to each other in proper order with hot air heater, chimney and constitutes the flue gas passageway, tail gas purification device links to each other in proper order with draught fan, aiutage and constitutes the tail gas purification passageway.
In the above apparatus: thermal desorption reactor include feed arrangement, the fixed cover of feed end, the rotary drum, the fixed cover of discharge end, wherein feed arrangement, the rotary drum, the fixed cover of discharge end communicates in proper order and constitutes the soil passageway, the fixed cover of feed end, the fixed cover of rotary drum discharge end communicates in proper order and constitutes the hot air duct in the reactor, hot air duct communicates with the soil passageway in the rotary drum, the last former soil import that is equipped with of feed arrangement, the fixed cover of feed end is equipped with the hot air circulation export, the fixed cover of discharge end is equipped with the hot air circulation import and handles the back soil export, the rotary drum is rotary motion around the central axis, all the other parts are fixed motionless.
In the above apparatus: the rotary drum barrel axis and horizontal plane contained angle be 1~6, just the rotary drum include outer insulating layer, the heat accumulator of inlayer and the heat pipe of part insertion heat accumulator, the inside cylindrical cavity that constitutes of heat accumulator is the space that hot air circulation and soil heat transfer and take place thermal desorption reaction, the heat pipe is along barrel circumference and axial equipartition, the distance of two adjacent heat pipes is greater than the maximum particle size of soil.
In the above apparatus: the diameter of the inner cavity of the drum body of the rotary drum is 1.5-2 m, and the length of the inner cavity of the drum body is 8-12 m; wherein: the thickness of the heat insulation layer is 80-120 mm, the thickness of the heat accumulator is 20-30 cm, the diameter of the heat pipe is 2-5 cm, the length of the heat pipe is 45-55 cm, and the distance between the heat pipes is 1-15 cm; preferably: the heat accumulator comprises alumina ceramic, silicon nitride ceramic or silicon carbide ceramic.
In some preferred embodiments: 1/3-2/3 of the length of the heat pipe is vertically inserted into the heat accumulator.
In some specific embodiments: the heat pipe shell is made of austenitic stainless steel, the working solution is mercury, and the internal negative pressure is (0.5-1.5) × 10-4Pa, working temperature of 250-650 ℃.
The method is characterized in that the polluted soil is conveyed to the feeding end of a rotary drum by a feeding device and is heated by two modes; firstly, hot air at 550-650 ℃ from an outlet of a hot air heater enters a rotary drum from a circulating hot air inlet of a discharge end fixing cover, and is in direct countercurrent contact with contaminated soil for heat transfer to heat the contaminated soil; secondly, the heat accumulator at the bottom of the rotary drum releases heat through a heat pipe to heat the polluted soil; the temperature of the polluted soil is gradually increased to about 300-500 ℃, water and organic pollutants in the soil are volatilized to be gaseous and carry dust to become thermal desorption tail gas, the thermal desorption tail gas is separated from solid soil, and the treated soil is discharged from a treated soil outlet of the discharge end fixing cover.
The above method may alternatively be capable of: the section of the rotary drum is divided into a heat release area and a heat storage area according to the horizontal line as a reference, the temperature of a heat storage body positioned at the bottom heat release area is higher than the temperature of soil, heat is transferred to the soil through a heat pipe, and the temperature is reduced to be close to the temperature of the soil; the temperature of the heat accumulator positioned in the top heat accumulation area is lower than that of hot air, the heat pipe transmits the heat of the hot air to the heat accumulator, and the temperature of the heat accumulator rises to be close to that of the hot air; along with the rotary motion of the rotary drum around the central axis, the heat accumulator performs heat accumulation and heat release circulation through the heat pipe, and the heat of the hot air is transferred to the soil.
The method comprises the following steps: the thermal desorption tail gas generated by heating the polluted soil in the rotary drum of the thermal desorption reactor is used as an initial source of circulating hot air, the hot air is subjected to dust removal treatment from a circulating hot air outlet of the feed end fixing cover to the dust remover and is driven by a hot air circulating fan, most of the hot air is heated to 550-650 ℃ through indirect heat exchange of a hot air heater, and then the hot air returns to the interior of the rotary drum from a circulating hot air inlet of the discharge end fixing cover, is directly contacted with the polluted soil for heat transfer, and simultaneously heats a heat accumulator through a heat pipe, the temperature is reduced to 200-300 ℃, and carries thermal desorption gas generated by heating the polluted soil, part of the thermal desorption tail gas is continuously recycled in a hot air circulating loop, and the rest of the thermal desorption tail gas is discharged after purification treatment.
The method comprises the following steps: the fuel is combusted in the combustion device to generate 950-1050 ℃ high-temperature flue gas, the high-temperature flue gas and the circulating hot air are subjected to indirect heat exchange through the hot air heater, the temperature is reduced to about 300 ℃, then the flue gas is discharged to the atmosphere from a chimney, and the high-temperature flue gas is not directly contacted with the circulating hot air.
The method comprises the following steps: along with the continuous processing of soil, constantly produce thermal desorption tail gas, the hot blast circulation has carried thermal desorption tail gas and mixes with it, and the gas volume becomes more, and 60 ~ 90% gas in the rotary drum is as hot blast circulation, recycles, and remaining gas is followed heated air circulation fan outlet branch, discharges after tail gas cleanup unit purification treatment.
Summarizing the above methods: the rotating speed is 0.4-10 r/min, and the filling coefficient of the soil in the cylinder body is not more than 0.25.
The utility model discloses among the technical scheme: the heat pipe consists of pipe shell, working liquid, liquid absorbing core and end cover, and is filled with proper amount of working liquid after negative pressure is pumped inside the pipe.
The utility model has the advantages that:
the utility model discloses a heat pipe ceramic heat accumulating type indirect thermal desorption soil remediation system and method, on one hand, the thermal desorption gas generated by the heated and volatilized soil is used as a heat transfer medium, through a circulating heating mode, not only the contact type high-efficiency heat transfer between hot air and the soil is realized, the processing capacity of the equipment is strong, but also the high-temperature flue gas is kept not to be in direct contact with the soil, the mixing of the high-temperature flue gas and gaseous organic pollutants is avoided, only a small amount of redundant gas needs to be purified, and the equipment scale is small; on the other hand, a second soil heating channel is provided by loading the heat pipe and the ceramic heat accumulator on the reactor, the heat transfer capacity of the reactor in unit volume is improved, and the treatment efficiency is remarkably improved on the same scale.
Drawings
Fig. 1 is a flow chart of a heat pipe ceramic heat accumulating type indirect thermal desorption soil remediation system.
Fig. 2 is a schematic structural view of a thermal desorption reactor.
FIG. 3 is a schematic cross-sectional view of the drum.
Wherein: the device comprises a thermal desorption reactor 1, a dust remover 2, a hot air circulating fan 3, a hot air heater 4, a combustion device 5, a chimney 6, a tail gas purification device 7, an induced draft fan 8, an exhaust funnel 9, a feeding device 10, a feeding end fixing cover 11, a rotary drum 12, a discharge end fixing cover 13, a heat pipe 14, a ceramic heat accumulator 15 and a heat insulation layer 16.
Detailed Description
The present invention will be further explained with reference to the following embodiments, but the scope of the present invention is not limited thereto:
example 1
As shown in fig. 1-3, an indirect thermal desorption soil remediation device for heat pipe enhanced heat storage comprises a thermal desorption reactor (1), a dust remover (2), a hot air circulating fan (3) and a hot air heater (4), wherein the thermal desorption reactor (1) is sequentially connected with the dust remover (2), the hot air circulating fan (3) and the hot air heater (4) to form a hot air circulating loop, a combustion device (5) is sequentially connected with the hot air heater (4) and a chimney (6) to form a flue gas passage, and a tail gas purification device (7) is sequentially connected with an induced draft fan (8) and an exhaust funnel (9) to form a tail gas purification passage.
Thermal desorption reactor (1) include feed arrangement (10), feed end fixed cover (11), rotary drum (12), discharge end fixed cover (13), wherein feed arrangement (10), rotary drum (12), discharge end fixed cover (13) communicate in proper order and constitute the soil passageway, feed end fixed cover (11), rotary drum (12) discharge end fixed cover (13) communicate in proper order and constitute the hot air duct in the reactor, hot air duct communicates with the soil passageway in rotary drum (12), be equipped with former soil import on feed arrangement (10), be equipped with the hot air circulating outlet on feed end fixed cover (11), be equipped with hot air circulating inlet and handle back soil outlet on discharge end fixed cover (13), rotary drum (12) are rotary motion around the central axis, all the other parts are fixed motionless.
The rotary drum (12) barrel axis be 1~6 with the horizontal plane contained angle, just rotary drum (12) include outer insulating layer (16), heat accumulator (15) and the heat pipe (14) of part insertion heat accumulator (15) of inlayer, the inside cylindrical cavity that constitutes of heat accumulator is the space that circulation hot-blast and soil heat transfer and take place the thermal desorption reaction, barrel circumference and axial equipartition are followed in heat pipe (14), the distance of two adjacent heat pipes is greater than the maximum particle size of soil.
The diameter of the inner cavity of the drum body of the rotary drum (12) is 1.5-2 m, and the length is 8-12 m; wherein: the thickness of the heat insulation layer is 80-120 mm, the thickness of the heat accumulator is 20-30 cm, the diameter of the heat pipe (14) is 2-5 cm, the length of the heat pipe is 45-55 cm, and the distance between the heat pipe and the heat pipe is 1-15 cm; the heat accumulator is made of alumina ceramic.
The heat pipe (14) is composed of a pipe shell, working liquid, a liquid absorbing core and an end cover, wherein a proper amount of working liquid is filled in the pipe after the pipe is pumped into negative pressure, the pipe is acted by gravity, the lower end of the pipe is an evaporation heat absorption section, the upper end of the pipe is a condensation heat release section, the functions of the two ends can be exchanged along with the upside-down position, the heat pipe utilizes the heat conduction principle and the phase change rapid heat transfer property of the working liquid, is a heat transfer element with the heat conduction capability exceeding that of any known metal, the pipe shell adopts austenitic stainless steel, the working liquid is mercury, and the working temperature is 250-.
The application case is as follows:
by adopting the system structure, the diameter of the inner cavity of the reactor cylinder is 2m, the length of the inner cavity is 12m, the thickness of the heat insulation layer outside the cylinder is 100mm, the thickness of the ceramic heat accumulator is 25cm, the diameter of the heat pipe is 3.2cm, the length of the heat pipe is 50cm, and the distance between the heat pipes is 10 cm. The heat pipe shell is made of austenitic stainless steel, the working liquid is mercury, and the working temperature is 250-650 ℃.
The temperature settings were: high-temperature flue gas generated by combustion is subjected to indirect heat exchange with circulating hot air at 1000 ℃ through a hot air heater, and the temperature is reduced to 300 ℃. The temperature of hot air at the inlet of the hot air heater is 250 ℃, and the temperature of hot air at the outlet of the hot air heater is 600 ℃; the final heating temperature of the contaminated soil is 350 ℃.
A method for realizing indirect thermal desorption soil remediation of heat pipe enhanced heat storage by using the device is characterized in that polluted soil is conveyed to the feeding end of a rotary drum by a feeding device and is heated by two modes; firstly, hot air with the temperature of 600 ℃ from an outlet of a hot air heater enters a rotary drum from a circulating hot air inlet of a discharge end fixing cover, and is in direct countercurrent contact with polluted soil for heat transfer to heat the polluted soil; secondly, the ceramic heat accumulator at the bottom of the rotary drum releases heat through a heat pipe to heat the polluted soil; the temperature of the polluted soil is gradually increased to about 350 ℃, water and organic pollutants in the soil are volatilized to be gaseous and carry dust to become thermal desorption tail gas which is separated from solid soil, and the treated soil is discharged from a treated soil outlet of the discharge end fixing cover.
The section of the rotary drum is divided into a heat release area and a heat storage area according to the horizontal line as a reference, the temperature of a ceramic heat storage body positioned at the heat release area at the bottom is higher than the temperature of soil, heat is transferred to the soil through a heat pipe, and the temperature is reduced to be close to the temperature of the soil; the temperature of the ceramic heat accumulator in the top heat accumulation area is lower than that of hot air, the heat pipe transfers the heat of the hot air to the ceramic heat accumulator, and the temperature of the heat accumulator rises to be close to that of the hot air; along with the rotary motion of the rotary drum around the central axis, the ceramic heat accumulator performs heat accumulation and heat release circulation through the heat pipe, and the heat of the hot air is transferred to the soil, namely the second heating mode.
The thermal desorption tail gas generated by heating the polluted soil in the rotary drum of the thermal desorption reactor is used as an initial source of circulating hot air, the hot air is subjected to dust removal treatment from a circulating hot air outlet of a feed end fixing cover to a dust remover and is driven by a hot air circulating fan, most of the hot air is heated to 600 ℃ through indirect heat exchange of a hot air heater, then the hot air is returned to the interior of the rotary drum from a circulating hot air inlet of a discharge end fixing cover, is directly contacted with the polluted soil for heat transfer, and simultaneously heats a ceramic heat accumulator through a heat pipe, the temperature is reduced to 200-300 ℃, the thermal desorption tail gas is carried with the polluted soil, part of the thermal desorption tail gas is continuously recycled in a hot air circulating loop, and the rest of the thermal desorption tail gas is discharged after being purified.
The method comprises the following steps: the fuel is combusted in the combustion device to generate high-temperature flue gas at 1000 ℃, the high-temperature flue gas and the circulating hot air are subjected to indirect heat exchange through the hot air heater, the temperature is reduced to 300 ℃, then the high-temperature flue gas is discharged to the atmosphere from a chimney, and the high-temperature flue gas is not directly contacted with the circulating hot air.
The method comprises the following steps: along with the continuous treatment of soil, the thermal desorption tail gas is continuously generated, the circulating hot air carries the thermal desorption tail gas and is mixed with the thermal desorption tail gas, the gas quantity is increased, 80 percent of gas in the rotary drum (12) is used as circulating hot air for recycling, and the rest gas is branched from the outlet of the hot air circulating fan and is discharged after being purified by a tail gas purification device.
The method comprises the following steps: the rotating speed of the rotating drum is 5r/min, and the soil filling coefficient in the cylinder body is 0.2.
The realized effects are as follows: the polluted soil is restored by 20 tons per hour, and the removal rate of the organic pollutants is more than 99 percent.
Comparative example 1:
the structure was the same as that of example 1 except for the heat pipe and the ceramic heat storage, wherein the inner cavity of the reactor cylinder had a diameter of 2m and a length of 12m, and the thickness of the heat insulating layer outside the cylinder was 100 mm.
The temperature settings were: high-temperature flue gas generated by combustion is subjected to indirect heat exchange with circulating hot air at 1000 ℃ through a hot air heater, and the temperature is reduced to 300 ℃. The temperature of hot air at the inlet of the hot air heater is 250 ℃, and the temperature of hot air at the outlet of the hot air heater is 600 ℃; the final heating temperature of the contaminated soil is 350 ℃.
The realized effects are as follows: the polluted soil is restored by 12 tons per hour, and the removal rate of the organic pollutants is more than 99 percent.
Comparison results
Treatment effects of examples and comparative examples
Claims (4)
1. The utility model provides an indirect thermal desorption soil prosthetic devices of heat pipe intensive heat storage which characterized in that: this prosthetic devices includes thermal desorption reactor (1), dust remover (2), heated air circulation fan (3) and hot air heater (4), thermal desorption reactor (1) link to each other in proper order and constitute the heated air circulation return circuit with dust remover (2), heated air circulation fan (3), hot air heater (4), burner (5) link to each other in proper order with hot air heater (4), chimney (6) and constitute the flue gas passageway, tail gas purification device (7) link to each other in proper order with draught fan (8), aiutage (9) and constitute the tail gas purification passageway.
2. The indirect thermal desorption soil remediation device with heat pipe for enhanced heat storage according to claim 1, wherein: thermal desorption reactor (1) include feed arrangement (10), feed end fixed cover (11), rotary drum (12), discharge end fixed cover (13), wherein feed arrangement (10), rotary drum (12), discharge end fixed cover (13) communicate in proper order and constitute the soil passageway, feed end fixed cover (11), rotary drum (12) discharge end fixed cover (13) communicate in proper order and constitute the hot air duct in the reactor, hot air duct communicates with the soil passageway in rotary drum (12), be equipped with former soil import on feed arrangement (10), be equipped with the hot air circulating outlet on feed end fixed cover (11), be equipped with hot air circulating inlet and handle back soil outlet on discharge end fixed cover (13), rotary drum (12) are rotary motion around the central axis, all the other parts are fixed motionless.
3. The indirect thermal desorption soil remediation device with heat pipe for enhanced heat storage according to claim 2, wherein: the rotary drum (12) barrel axis be 1~6 with the horizontal plane contained angle, just rotary drum (12) include outer insulating layer (16), heat accumulator (15) and the heat pipe (14) of part insertion heat accumulator (15) of inlayer, the inside cylindrical cavity that constitutes of heat accumulator is the space that circulation hot-blast and soil heat transfer and take place the thermal desorption reaction, barrel circumference and axial equipartition are followed in heat pipe (14), the distance of two adjacent heat pipes is greater than the maximum particle size of soil.
4. The indirect thermal desorption soil remediation device with heat pipe for enhanced heat storage according to claim 3, wherein: the diameter of the inner cavity of the drum body of the rotary drum (12) is 1.5-2 m, and the length is 8-12 m; wherein: the thickness of the heat insulation layer is 80-120 mm, the thickness of the heat accumulator is 20-30 cm, the diameter of the heat pipe (14) is 2-5 cm, the length of the heat pipe is 45-55 cm, and the distance between the heat pipe and the heat pipe is 1-15 cm; preferably: the heat accumulator comprises alumina ceramic, silicon nitride ceramic or silicon carbide ceramic.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114904903A (en) * | 2022-05-27 | 2022-08-16 | 江苏省环境科学研究院 | Quick emergency thermal desorption device for petroleum hydrocarbon leakage contaminated soil |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114904903A (en) * | 2022-05-27 | 2022-08-16 | 江苏省环境科学研究院 | Quick emergency thermal desorption device for petroleum hydrocarbon leakage contaminated soil |
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