CN216093709U - Processing apparatus of high temperature thermal regeneration active carbon - Google Patents

Abstract

The utility model discloses a processing device for high-temperature thermally-regenerated activated carbon, which comprises: the device comprises a feed inlet, a drying section, a carbonization section, an activation section and a discharge outlet which are sequentially communicated from top to bottom, wherein valves are arranged at the communication ends between every two sections, and the active carbon can be automatically transferred from the feed inlet to the discharge outlet; the drying chamber is arranged in the drying section and is used for drying the active carbon; the carbonization chamber is arranged in the carbonization section and is used for carbonizing the active carbon; the activation chamber is communicated with the front section of the activation section to activate the activated carbon; the separation chamber is arranged in the middle section of the activation section to separate activated carbon from steam; the waste gas treatment device comprises a combustion layer and an evaporation layer, the combustion layer is connected with the evaporation layer to evaporate liquid, and the combustion layer is communicated with the drying section; the combustion layer is communicated with the carbonization section; the combustion layer is communicated with the separation chamber; the evaporation layer is communicated with the activation chamber; and the steam treatment device is communicated with the activation chamber to treat redundant steam.

Description

Processing apparatus of high temperature thermal regeneration active carbon

Technical Field

The utility model relates to the field of environment-friendly hazardous waste disposal, in particular to a treatment device for high-temperature thermally-regenerated activated carbon.

Background

The regeneration of the activated carbon is to carry out special treatment on the waste activated carbon which loses activity, so that most of the adsorption capacity of the waste activated carbon is recovered, and the waste activated carbon is reused in the adsorption process. In general, two industrial methods for regenerating activated carbon saturated in adsorption include a chemical regeneration method using an acid or an alkali and a high-temperature thermal regeneration method in which an activation reaction is performed at a high temperature using water gas. The regeneration method of the medicine is used as a method for decolorizing and refining the medicine and regenerating the special activated carbon for decolorizing the fermentation liquor, but because a large amount of waste water is generated in the regeneration process, a device for treating the waste water by neutralization and biological treatment needs to be added at the same time, the implementation of the method has certain difficulty in the region with strict requirements on the quality of the discharged water; in the high-temperature thermal regeneration method, since organic substances adsorbed on activated carbon are decomposed by heating, air pollution is caused if the organic substances are directly discharged, and the high-temperature thermal regeneration method needs to separately provide a heat source, so that energy consumption is large.

SUMMERY OF THE UTILITY MODEL

The present invention is directed to solving at least one of the problems of the prior art. Therefore, the utility model provides a high-temperature thermal regeneration activated carbon treatment device, which can activate activated carbon without waste water, has no air pollution, realizes multi-stage energy utilization and improves the energy utilization rate.

The technical scheme adopted by the embodiment of the utility model is as follows: a treatment device for high-temperature thermally regenerated activated carbon, comprising: the drying section is provided with a drying chamber for drying the activated carbon, a feeding hole is formed in the drying section, and the feeding hole is communicated with the drying chamber; the carbonization section is provided with a carbonization chamber for carbonizing the active carbon, and the carbonization chamber is communicated with the drying chamber; the device comprises an activation section, a carbonization section and a steam separation section, wherein the activation section is provided with an activation chamber for activating activated carbon and a separation chamber for separating the activated carbon from steam, the activation chamber is communicated with the separation chamber, the activation chamber is communicated with the carbonization chamber, the activation section is provided with a discharge hole, and the discharge hole is communicated with the separation chamber; the waste gas treatment device comprises a combustion layer and an evaporation layer, wherein the combustion layer is used for heating the evaporation layer to evaporate liquid, the combustion layer is communicated with the drying chamber and is used for treating dried waste gas generated by drying, the combustion layer is communicated with the carbonization chamber and is used for treating pyrolysis waste gas generated by carbonizing, and the combustion layer is communicated with the separation chamber and is used for treating polluted steam; the evaporation layer is communicated with the activation chamber; a steam treatment device communicated with the activation chamber to treat unreacted steam.

The processing device for the high-temperature thermally regenerated activated carbon provided by the embodiment of the utility model at least has the following beneficial effects:

1. through a feeding hole, a drying section, a carbonization section, an activation section and a discharging hole which are communicated in sequence from top to bottom, the active carbon can sequentially pass through the device or the working section under the action of gravity, so that the automatic transfer of the active carbon is realized, and the use is more convenient;

2. the drying waste gas of the drying section and the pyrolysis waste gas of the carbonization section are introduced into the combustion layer, so that harmful substances are further calcined in the combustion layer, and meanwhile, energy is provided for the evaporation layer to provide steam, and further, the activation of the activated carbon is realized by utilizing the steam, the energy is recycled, and the utilization efficiency is high;

3. the separation chamber separates the steam in the activated carbon from the activated carbon, the steam is introduced into the combustion layer and is further calcined to remove harmful substances, and meanwhile, the energy is provided for the evaporation layer, the energy is recycled, and the utilization efficiency is high;

4. through a high-temperature thermal regeneration method, no waste water is generated after activated, the generated waste gas is recycled and combusted for multiple times, the pollution-free emission is realized, meanwhile, the energy is recycled for multiple times, and the energy utilization efficiency is higher;

5. the steam is treated by the steam treatment device, so that pollution-free discharge of the steam is realized.

According to some embodiments of the utility model, further comprising a primary utilization conduit communicating a middle portion of the activation chamber and the combustion layer.

According to some embodiments of the utility model, the device further comprises a secondary utilization pipeline, wherein the secondary utilization pipeline is arranged outside the carbonization chamber to insulate the carbonization chamber and is communicated with the bottom of the activation chamber and the waste gas treatment device.

According to some embodiments of the present invention, the exhaust gas treatment device further comprises a tertiary utilization pipe disposed outside the drying chamber to keep the drying chamber warm, the tertiary utilization pipe is communicated with the secondary utilization pipe and/or the bottom of the activation chamber, and the tertiary utilization pipe is communicated with the exhaust gas treatment device.

According to some embodiments of the utility model, the activation chamber comprises an activation layer and a heat preservation layer, the heat preservation layer is arranged around the activation layer to preserve heat of the activation layer, the top parts of the activation layer and the activation layer are communicated, the discharge end of the carbonization section is arranged in the activation layer, the gas outlet end of the evaporation layer is arranged in the activation layer, is positioned below the discharge end and is arranged towards the discharge end, the bottom part of the activation layer is communicated with the separation chamber, the middle part of the heat preservation layer is communicated with the combustion layer, and the bottom part of the heat preservation layer is communicated with the steam treatment device.

According to some embodiments of the utility model, the device further comprises a cooling device, which is arranged at the end section of the activation section and is communicated with the separation chamber and the discharge hole to cool the activated carbon.

According to some embodiments of the utility model, the cooling device comprises a cooling pipe, a circulation pipe and a water pump, the cooling pipe is communicated with the separation chamber and the discharge hole, the circulation pipe is arranged around the outer side of the cooling pipe, and the circulation pipe is communicated with the water pump to form a closed cooling water circulation.

According to some embodiments of the utility model, the steam treatment device comprises a quenching deacidification tower, a bag-type dust remover, an air-entraining fan and a chimney which are communicated in sequence, wherein the quenching deacidification tower is communicated with the activation chamber.

According to some embodiments of the utility model, the exhaust gas treatment device comprises a boiler, a combustion-supporting gas pipe, a gas pipe and a water inlet pipe, wherein the combustion-supporting gas pipe, the gas pipe and the water inlet pipe are all communicated with the boiler, and the boiler is communicated with the drying section and the carbonization section and is communicated with the activation chamber through a cylinder.

According to some embodiments of the utility model, the feed inlet, the drying section, the carbonization section, the activation section and the discharge outlet are sequentially communicated from top to bottom, and the communication ends between every two sections are respectively provided with a valve, the drying chamber and the carbonization chamber are both horizontally arranged, and the interior of the drying chamber and the carbonization chamber is respectively provided with a pushing device so as to push the interior activated carbon into the next working section.

According to some embodiments of the utility model, the pushing device is a screw.

According to some embodiments of the utility model, the valve is a two-stage knife gate valve.

Additional aspects and advantages of the utility model will be set forth in part in the description which follows and, in part, will be obvious from the description, or may be learned by practice of the utility model.

Drawings

The above and/or additional aspects and advantages of the present invention will become apparent and readily appreciated from the following description of the embodiments, taken in conjunction with the accompanying drawings of which:

FIG. 1 is a schematic view of a processing apparatus for thermally regenerating activated carbon at a high temperature according to an embodiment of the present invention.

Reference numerals:

100-a feed inlet;

200-a drying section; 210-a drying chamber;

300-carbonization section; 310-a carbonization chamber;

400-an activation section; 410-an activation chamber; 411-an active layer; 412-an insulating layer; 420-a separation chamber; 430-a cooling device; 431-cooling tubes; 432-a recycle conduit;

500-discharge hole;

600-an exhaust gas treatment device; 610-a boiler; 620-combustion assisting gas pipe; 630-gas pipe; 640-a water inlet pipe;

700-steam treatment device; 710-quench deacidification tower; 720-bag dust collector; 730-a bleed air blower; 740-a chimney;

800-a valve; 900-first-stage utilization pipeline; 1000-second stage utilization pipeline; 1100-three stage utilization of pipelines.

Detailed Description

Reference will now be made in detail to embodiments of the present invention, examples of which are illustrated in the accompanying drawings, wherein like or similar reference numerals refer to the same or similar elements or elements having the same or similar function throughout. The embodiments described below with reference to the accompanying drawings are illustrative only for the purpose of explaining the present invention, and are not to be construed as limiting the present invention.

In the description of the present invention, it should be understood that the orientation or positional relationship referred to in the description of the orientation, such as the upper, lower, front, rear, left, right, etc., is based on the orientation or positional relationship shown in the drawings, and is only for convenience of description and simplification of description, and does not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and thus, should not be construed as limiting the present invention.

In the description of the present invention, the meaning of a plurality of means is one or more, the meaning of a plurality of means is two or more, and larger, smaller, larger, etc. are understood as excluding the number, and larger, smaller, inner, etc. are understood as including the number. If the first and second are described for the purpose of distinguishing technical features, they are not to be understood as indicating or implying relative importance or implicitly indicating the number of technical features indicated or implicitly indicating the precedence of the technical features indicated.

In the description of the present invention, unless otherwise explicitly limited, terms such as arrangement, installation, connection and the like should be understood in a broad sense, and those skilled in the art can reasonably determine the specific meanings of the above terms in the present invention in combination with the specific contents of the technical solutions.

In addition, the technical solutions in the embodiments of the present invention may be combined with each other, but it must be based on the realization of those skilled in the art, and when the technical solutions are contradictory or cannot be realized, such a combination of technical solutions should not be considered to exist, and is not within the protection scope of the present invention.

Referring to fig. 1, in some embodiments of the present invention, a processing apparatus for high temperature thermal regeneration of activated carbon includes:

the drying section 200, the drying section 200 is provided with a drying chamber 210 for drying the activated carbon, the drying section 200 is provided with a feed inlet 100, and the feed inlet 100 is communicated with the drying chamber 210;

a carbonization section 300, wherein the carbonization section 300 is provided with a carbonization chamber 310 for carbonizing the active carbon, and the carbonization chamber 310 is communicated with the drying chamber 210;

the device comprises an activation section 400, wherein the activation section 400 is provided with an activation chamber 410 for activating activated carbon and a separation chamber 420 for separating the activated carbon from steam, the activation chamber 410 is communicated with the separation chamber 420, the activation chamber 410 is communicated with a carbonization chamber 310, the activation section 400 is provided with a discharge hole 500, and the discharge hole 500 is communicated with the separation chamber 420;

the waste gas treatment device 600 comprises a combustion layer and an evaporation layer, wherein the combustion layer is used for heating the evaporation layer to evaporate liquid, the combustion layer is communicated with the drying chamber 210 and is used for treating dried waste gas generated by drying, the combustion layer is communicated with the carbonization chamber 310 and is used for treating pyrolysis waste gas generated by carbonization, and the combustion layer is communicated with the separation chamber 420 and is used for treating polluted steam; the evaporation layer is communicated with the activation chamber 410;

a steam treatment device 700 communicated with the activation chamber 410 to treat the unreacted steam.

Specifically, the drying waste gas of the drying section 200 and the pyrolysis waste gas of the carbonization section 300 are introduced into the combustion layer, so that harmful substances are further calcined in the combustion layer, and meanwhile, energy is provided for the evaporation layer to provide steam, and further, the activated carbon is activated by utilizing the steam, the energy is recycled, and the utilization efficiency is high; the separation chamber 420 separates the steam in the activated carbon from the activated carbon, the steam is introduced into the combustion layer and is further calcined to remove harmful substances, and meanwhile, the energy is provided for the evaporation layer, so that the energy is recycled, and the utilization efficiency is high.

Through a high-temperature thermal regeneration method, no waste water is generated after the activated carbon is activated, and the generated waste gas is recycled and combusted for multiple times, so that the energy is recycled while pollution-free emission is realized, and the energy utilization efficiency is higher; the steam is treated by the steam treatment device 700, and pollution-free discharge of the steam is realized.

The specific process is as follows:

in this embodiment, the valve 800 is a two-stage knife gate valve; drying chamber 210 is a screw dryer; the carbonization chamber 310 is a spiral pyrolysis cylinder; the combustion layer and the evaporation layer are both arranged in the boiler 610; the activation chamber 410 is a steam activation tower; the separation chamber 420 is a cyclone.

Step 1: the crushed powdery waste activated carbon is fed from the feed inlet 100, uniformly fed into a spiral dryer through a valve 800, nitrogen is introduced into the spiral dryer, the temperature of the spiral dryer is controlled to be 120-130 ℃, the drying time is controlled to be about 15 minutes, and the dried waste gas is introduced into a combustion layer in a boiler 610 for combustion.

Step 2: the material dried by the dryer is uniformly fed into the spiral pyrolysis cylinder through the secondary knife switch valve, nitrogen is introduced into the pyrolysis cylinder, the temperature is controlled to be 450-650 ℃, the carbonization time is controlled to be 15-20 minutes, organic substances adsorbed by the waste activated carbon are carbonized, and pyrolysis waste gas is introduced into the combustion layer to be combusted.

And step 3: the carbonized active carbon is conveyed into a steam activation tower, the temperature in the tower is controlled to be 700-850 ℃, high-temperature steam is provided to the steam activation tower by an evaporation layer in the boiler 610, the high-temperature steam is fully contacted with the powdered active carbon in the tower, the generated fixed carbon is reacted, the aperture of the active carbon is reopened, and the adsorption performance of the active carbon is recovered.

And 4, step 4: the activated carbon powder enters a cyclone separator, the activated carbon powder is separated from steam, the steam is led to other working sections for secondary utilization or enters a steam treatment device 700, and the activated carbon powder enters the next working section.

In the above process, the drying exhaust gas mainly contains volatile components on the activated carbon; the pyrolysis waste gas mainly contains organic matters which are adsorbed on the activated carbon and can be partially boiled and vaporized for desorption, and also contains micromolecular hydrocarbon which is generated by decomposition reaction of a part of the organic matters; the high-temperature steam mainly contains CO, CO2, H2 and other hydrocarbon gases. Above-mentioned gas all needs to carry out the postcombustion to realize the complete reaction, in order to obtain the gas that can discharge into in the air, and the energy when this application will above gas postcombustion drops into the evaporation process to the evaporation blanket, realizes the reuse of the energy, has improved energy utilization efficiency.

Referring to fig. 1, in some embodiments of the present invention, a stage utilization pipe 900 is further included, and the stage utilization pipe 900 communicates the middle portion of the activation chamber 410 and the combustion layer.

Specifically, the air in the activation chamber 410 is transferred from the middle of the activation chamber 410 to the combustion layer of the exhaust gas treatment device 600 through the primary utilization pipe 900, so that the high-temperature steam is subjected to secondary combustion or even multiple combustion, so that CO, H2 and the like which are generated by insufficient combustion and contained in the high-temperature steam are sufficiently combusted to generate CO2 and water, and finally the CO2 is discharged along the steam treatment device 700, and the water is continuously converted into water vapor to activate the activated carbon, thereby realizing multiple recycling of energy and improving the utilization efficiency of the energy.

In addition, the temperature in the activation chamber 410 can reach 700-.

Referring to fig. 1, in some embodiments of the present invention, a secondary utilization pipe 1000 is further included, and the secondary utilization pipe 1000 is disposed outside the carbonization chamber 310 to insulate the carbonization chamber 310, and is communicated with the bottom of the activation chamber 410 and the exhaust gas treatment device 600.

Specifically, because the density of the hot air is lower than that of the cold air, the hot air is lighter and is easy to rise, the temperature of the steam at the bottom of the activation chamber 410 is lower, the steam at the lower temperature enters the secondary utilization pipeline 1000 at about 700 ℃, because the secondary utilization pipeline 1000 is located outside the carbonization chamber 310, the temperature of the carbonization section 300 needs to be controlled between 450-650 ℃, and the temperature of the carbonization section 300 is kept at 450-650 ℃ by introducing the steam into the secondary utilization pipeline 1000, so that the temperature of the carbonization section 300 is always kept between 450-650 ℃, and the gradient application of the heat energy contained in the steam is realized, the utilization efficiency of the heat energy is higher, and the use is more convenient.

Moreover, the secondary utilization pipe 1000 is communicated with the exhaust gas treatment device 600, so that the steam in the secondary utilization pipe 1000 can flow back again to enter the combustion layer of the exhaust gas treatment device 600 for repeated combustion, and when the secondary utilization pipe 1000 is communicated with the exhaust gas treatment device 600 through the primary utilization pipe 900, the steam in the activation chamber 410 can enter the secondary utilization pipe 1000 through the primary utilization pipe 900, so that the use is more convenient.

Referring to fig. 1, in some embodiments of the present invention, a tertiary utilization duct 1100 is further included, the tertiary utilization duct 1100 is disposed outside the drying chamber 210 to insulate the drying chamber 210, the tertiary utilization duct 1100 is communicated with the secondary utilization duct 1000 and/or the bottom of the activation chamber 410, and the tertiary utilization duct 1100 is communicated with the exhaust gas treatment device 600.

Specifically, the principle of the tertiary utilization pipeline 1100 is the same as that of the secondary utilization pipeline 1000, and the heat preservation of the drying chamber 210 by the tertiary utilization pipeline 1100 is realized by introducing steam at a certain temperature into the tertiary utilization pipeline 1100, while the temperature required to be maintained in the drying section 200 is between 120 ℃ and 130 ℃ and lower than that of the steam in the secondary utilization pipeline 1000, so that the steam can be directly led out from the activation chamber 410 into the tertiary utilization pipeline 1100, the steam in the secondary utilization pipeline 1000 can be directly led out into the tertiary utilization pipeline 1100, or both the steam and the steam exist, the gradient application of steam heat energy is realized, and the energy utilization efficiency is higher.

Referring to fig. 1, in some embodiments of the present invention, the activation chamber 410 includes an activation layer 411 and an insulation layer 412, the insulation layer 412 is disposed around the activation layer 411 to insulate the activation layer 411, top portions of the activation layer 411 and the insulation layer are connected, a discharge end of the carbonization section 300 is disposed in the activation layer 411, an air outlet end of the evaporation layer is disposed in the activation layer 411, below the discharge end, and toward the discharge end, a bottom portion of the activation layer 411 is connected to the separation chamber 420, a middle portion of the insulation layer 412 is connected to the combustion layer, and a bottom portion thereof is connected to the steam processing apparatus 700.

Specifically, in the activation layer 411, the activated carbon falls towards the air outlet, the activated carbon is fully contacted with high-temperature steam to fully activate and recover the performance of the activated carbon, so that high-quality activated carbon is obtained, the steam escaping from the air outlet end of the evaporation layer enters the heat insulation layer 412 through the top of the activation layer 411, the steam can be communicated with the combustion layer of the waste gas treatment device 600 through the middle of the heat insulation layer 412, secondary or multiple combustion of the steam is realized, so that air pollution is prevented, meanwhile, the energy is repeatedly utilized for multiple times, and the energy utilization efficiency is higher; the steam with too low temperature is connected with the steam treatment device 700 through the bottom of the heat insulation layer 412 for subsequent treatment, or enters the secondary utilization pipeline 1000 or the tertiary utilization pipeline 1100, so that the heat energy is recycled, and the use is more convenient.

Referring to fig. 1, in some embodiments of the present invention, a cooling device 430 is further included and is disposed at the end of the activation section 400 to communicate the separation chamber 420 with the discharge port 500 to cool the activated carbon.

Specifically, the activated carbon from which steam is separated is cooled by the cooling device 430, so that the temperature of the activated carbon is reduced and the activated carbon is collected more conveniently, and the activated carbon can be directly subjected to subsequent packaging treatment, and meanwhile, the activated carbon is difficult to adsorb moisture in the air at normal temperature, so that the activated carbon is damped, and the quality of the activated carbon is improved more favorably.

Referring to fig. 1, in some embodiments of the present invention, the cooling device 430 includes a cooling pipe 431, a circulation pipe 432, and a water pump, the cooling pipe 431 communicates the separation chamber 420 with the discharge hole 500, the circulation pipe 432 is disposed around the outside of the cooling pipe 431, and the circulation pipe 432 communicates with the water pump to form a closed cooling water circulation.

Specifically, water cooling is performed, so that the water in the cooling pipe 431, after being heated and heated, can be used as the evaporated liquid in the exhaust gas treatment device 600 to be vaporized, the heat energy can be repeatedly utilized, and the energy utilization efficiency is higher.

Referring to fig. 1, in some embodiments of the utility model, a steam treatment plant 700 includes a quench deacidification tower 710, a bag-type dust collector 720, an air-entraining fan 730 and a stack 740 in sequential communication, the quench deacidification tower 710 being in communication with an activation chamber 410.

Specifically, steam enters a quenching deacidification tower 710 to be quenched to a temperature below 200 ℃, is subjected to deacidification treatment, then enters a bag-type dust collector 720, is subjected to fly ash collection by the bag-type dust collector 720, and is finally discharged into the atmosphere by an induced draft fan and a chimney 740.

Referring to fig. 1, in some embodiments of the present invention, the exhaust gas treatment device 600 includes a boiler 610, a combustion-supporting gas pipe 620, a gas pipe 630, and a water inlet pipe 640, the combustion-supporting gas pipe 620, the gas pipe 630, and the water inlet pipe 640 are all disposed to communicate with the boiler 610, and the boiler 610 communicates with the drying section 200 and the carbonization section 300 and communicates with the activation chamber 410 through a cylinder.

Specifically, the combustion-supporting gas pipe 620 conveys combustion-supporting gas, and the gas pipe 630 conveys gas to burn in the boiler 610, and water is delivered through the water inlet pipe 640, so that evaporation is more convenient.

Referring to fig. 1, in some embodiments of the present invention, the feeding inlet 100, the drying section 200, the carbonization section 300, the activation section 400, and the discharging outlet 500 are sequentially communicated from top to bottom, and the communicating ends between each two are provided with valves 800, and the drying chamber 210 and the carbonization chamber 310 are horizontally arranged and are internally provided with pushing devices to push the activated carbon inside into the next working section.

Specifically, the feeding hole 100, the drying section 200, the carbonization section 300, the activation section 400 and the discharging hole 500 which are communicated in sequence from top to bottom enable the activated carbon to enter the valve 800 under the action of gravity when entering the next working section and then enter the next working section through the valve 800; and promote the active carbon through thrust unit and remove in the workshop section for the motion of active carbon is more controllable, and it is more convenient to use, and the drying chamber 210 and the carbomorphism room 310 of level setting will save the space of vertical direction more, and the design is more reasonable. The pushing device is a spiral propeller. The spiral propeller saves more space and is more convenient to use.

Referring to fig. 1, in some embodiments of the utility model, the valve 800 is a two-stage knife gate valve.

Particularly, continuous blanking is carried out through a secondary knife switch valve, the blanking process is more controllable and safer, and the detailed blanking steps can be found in the 'sheet block material sealing feeding method' in the Chinese invention patent with the patent number of CN 202011496165.4.

The present invention is not limited to the above-described embodiments, and those skilled in the art can make equivalent modifications or substitutions without departing from the spirit of the present invention, and such equivalent modifications or substitutions are included in the scope defined by the claims of the present application.

Claims (10)

1. A treatment device for high-temperature thermally regenerated activated carbon is characterized by comprising:

the drying section (200) is provided with a drying chamber (210) for drying the activated carbon, the drying section (200) is provided with a feeding hole (100), and the feeding hole (100) is communicated with the drying chamber (210);

the carbonization section (300) is provided with a carbonization chamber (310) for carbonizing the active carbon, and the carbonization chamber (310) is communicated with the drying chamber (210);

the device comprises an activation section (400), wherein the activation section (400) is provided with an activation chamber (410) for activating activated carbon and a separation chamber (420) for separating the activated carbon from steam, the activation chamber (410) is communicated with the separation chamber (420), the activation chamber (410) is communicated with a carbonization chamber (310), the activation section (400) is provided with a discharge hole (500), and the discharge hole (500) is communicated with the separation chamber (420);

the waste gas treatment device (600) comprises a combustion layer and an evaporation layer, the combustion layer is used for heating the evaporation layer to evaporate liquid, the combustion layer is communicated with the drying chamber (210) and is used for treating dry waste gas generated by drying, the combustion layer is communicated with the carbonization chamber (310) and is used for treating pyrolysis waste gas generated by carbonization, and the combustion layer is communicated with the separation chamber (420) and is used for treating polluted steam; the evaporation layer is communicated with the activation chamber (410);

a steam treatment device (700) in communication with the activation chamber (410) to treat unreacted steam.

2. The apparatus for treating high-temperature thermally regenerated activated carbon as claimed in claim 1, wherein: the device also comprises a first-stage utilization pipeline (900), wherein the first-stage utilization pipeline (900) is communicated with the middle part of the activation chamber (410) and the combustion layer.

3. The apparatus for treating high-temperature thermally regenerated activated carbon as claimed in claim 1, wherein: the device is characterized by further comprising a secondary utilization pipeline (1000), wherein the secondary utilization pipeline (1000) is arranged on the outer side of the carbonization chamber (310) to keep the carbonization chamber (310) warm and is communicated with the bottom of the activation chamber (410) and the waste gas treatment device (600).

4. The apparatus for treating high-temperature thermally regenerated activated carbon as claimed in claim 3, wherein: the device is characterized by further comprising a third-stage utilization pipeline (1100), wherein the third-stage utilization pipeline (1100) is arranged on the outer side of the drying chamber (210) to keep the drying chamber (210) warm, the third-stage utilization pipeline (1100) is communicated with the bottom of the second-stage utilization pipeline (1000) and/or the activation chamber (410), and the third-stage utilization pipeline (1100) is communicated with the waste gas treatment device (600).

5. The apparatus for treating high-temperature thermally regenerated activated carbon as claimed in claim 1, wherein: the activation chamber (410) comprises an activation layer (411) and a heat preservation layer (412), the heat preservation layer (412) surrounds the activation layer (411) to preserve heat of the activation layer (411), the tops of the activation layer and the activation layer are communicated, the discharge end of the carbonization section (300) is arranged in the activation layer (411), the air outlet end of the evaporation layer is arranged in the activation layer (411) and is positioned below the discharge end and faces the discharge end, the bottom of the activation layer (411) is communicated with the separation chamber (420), the middle of the heat preservation layer (412) is communicated with the combustion layer, and the bottom of the heat preservation layer is communicated with the steam treatment device (700).

6. A high temperature thermally regenerated activated carbon treatment apparatus according to any one of claims 1 to 5, characterized in that: the device also comprises a cooling device (430) which is arranged at the tail section of the activation section (400) and is communicated with the separation chamber (420) and the discharge hole (500) so as to cool the activated carbon.

7. The apparatus for treating high-temperature thermally regenerated activated carbon as claimed in claim 6, wherein: the cooling device (430) comprises a cooling pipe (431), a circulating pipeline (432) and a water pump, wherein the cooling pipe (431) is communicated with the separation chamber (420) and the discharge hole (500), the circulating pipeline (432) is arranged around the outer side of the cooling pipe (431), and the circulating pipeline (432) is communicated with the water pump to form closed cooling water circulation.

8. A high temperature thermally regenerated activated carbon treatment apparatus according to any one of claims 1 to 5, characterized in that: the steam treatment device (700) comprises a quenching deacidification tower (710), a bag-type dust remover (720), an air-entraining fan (730) and a chimney (740), which are sequentially communicated, wherein the quenching deacidification tower (710) is communicated with the activation chamber (410).

9. A high temperature thermally regenerated activated carbon treatment apparatus according to any one of claims 1 to 5, characterized in that: waste gas processing apparatus (600) includes boiler (610), combustion-supporting gas pipe (620), gas pipe (630) and inlet tube (640), the combustion layer with the evaporation blanket all set up in boiler (610), combustion-supporting gas pipe (620) gas pipe (630) with the combustion layer is linked together, inlet tube (640) with the evaporation blanket is linked together, the evaporation blanket pass through the cylinder with activation chamber (410) is linked together.

10. A high temperature thermally regenerated activated carbon treatment apparatus according to any one of claims 1 to 5, characterized in that: feed inlet (100) drying section (200) carbomorphism section (300) activation section (400) with discharge gate (500) are linked together by high to end in proper order, and the end of communicating between two liang all is equipped with valve (800), the equal level setting of drying chamber (210) and carbomorphism room (310), and inside all is equipped with thrust unit to in pushing into next workshop section with inside active carbon.

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