CN112870912A

CN112870912A - Method and system for extinguishing fire and reducing temperature of active carbon in front of adsorption tower

Info

Publication number: CN112870912A
Application number: CN202110045110.XA
Authority: CN
Inventors: 周浩宇; 陈思墨; 刘雁飞; 刘前; 李谦; 王业峰
Original assignee: Zhongye Changtian International Engineering Co Ltd
Current assignee: Zhongye Changtian International Engineering Co Ltd
Priority date: 2021-01-13
Filing date: 2021-01-13
Publication date: 2021-06-01
Anticipated expiration: 2041-01-13
Also published as: CN112870912B

Abstract

A method for extinguishing fire and reducing temperature of an active carbon in a front storage bin of an adsorption tower comprises the following steps: 1) the thermal imaging instrument (1) acquires a thermal imaging image of the material entering the tail imaging area (3) of the vibrating screen (2); 2) judging whether the material entering the imaging area (3) has a high temperature point or not according to the thermal imaging image; if the thermal imaging image is judged to have a high temperature point, recording the found position of the material at the high temperature point in the imaging area (3) at the tail part of the vibrating screen (2); 3) when the materials at the high-temperature point are moved into a storage bin (5) connected with a discharge opening of the conveyor (4), the spontaneous combustion activated carbon extinguishing and cooling device arranged at the top of the storage bin (5) extinguishes corresponding high-temperature materials and cools the corresponding high-temperature materials. According to the invention, the high-temperature activated carbon is detected at the tail part of the vibrating screen and is processed in the flowing falling state of the high-temperature activated carbon falling to the storage bin, so that the problem that the high-temperature activated carbon particles are difficult to detect and treat comprehensively is solved, and the safety of the system is improved.

Description

Method and system for extinguishing fire and reducing temperature of active carbon in front of adsorption tower

Technical Field

The invention relates to detection and treatment of high-temperature active carbon particles in an active carbon flue gas purification device, in particular to a method and a system for extinguishing and cooling by active carbon in a front storage bin of an adsorption tower, and belongs to the technical field of active carbon flue gas purification.

Background

The amount of flue gas generated in the sintering process accounts for about 70 percent of the total flow of steel, and the main pollutant components in the sintering flue gas are dust and SO₂、NO_X(ii) a In addition, there are also small amounts of VOC_sDioxins, heavy metals, etc.; the waste water can be discharged after purification treatment. At present, the technology of treating sintering flue gas by using an activated carbon desulfurization and denitrification device is mature, and the activated carbon desulfurization and denitrification device is popularized and used in China, so that a good effect is achieved.

The working schematic diagram of the activated carbon desulfurization and denitrification device in the prior art is shown in figure 1: raw flue gas (main component of pollutant is SO) generated in sintering process₂) The flue gas is discharged as clean flue gas after passing through an active carbon bed layer of the adsorption tower; adsorbing pollutants (the main component of the pollutants is SO) in the flue gas₂) The activated carbon is sent into an analysis tower through an activated carbon conveyor S1, the activated carbon adsorbed with pollutants in the analysis tower is heated to 400-430 ℃ for analysis and activation, SRG (sulfur-rich) gas released after the analysis and activation is subjected to an acid making process, the activated carbon after the analysis and activation is cooled to 110-130 ℃ and then discharged out of the analysis tower, activated carbon dust is screened out by a vibrating screen, and the activated carbon particles on the screen reenter the adsorption tower through an activated carbon conveyor S2; fresh activated carbon is supplied to the conveyor S1 (activated carbon used in the flue gas purification apparatus is cylindrical activated carbon granules having typical sizes: 9mm in diameter and 11mm in height).

As shown in figure 1, the activated carbon is heated to 400-430 v in the desorption tower, and the ignition temperature of the activated carbon used by the activated carbon flue gas purification device is 420 ℃; the desorption column was of a gas-tight construction and was filled with nitrogen.

The schematic structure of the prior art desorption tower is shown in fig. 2: the active carbon is not contacted with air in the desorption tower so as to ensure that the active carbon is not burnt in the desorption tower; in the process of heating and cooling the activated carbon in the desorption tower, occasionally, a small amount of heated activated carbon particles are not sufficiently cooled in the cooling section, and a small amount of high-temperature activated carbon particles which are not cooled to a safe temperature are discharged from the desorption tower (the amount of activated carbon particles filled in the desorption tower of the sintering flue gas purification device exceeds hundreds of tons, and the processes of flowing, cooling, heating, heat conduction and the like of the activated carbon particles in the desorption tower are complicated). The high-temperature activated carbon particles are discharged from the desorption tower and then contact with air, spontaneous combustion (smoldering and flameless) can occur, a small amount of high-temperature activated carbon particles of the spontaneous combustion can possibly ignite low-temperature activated carbon particles around the high-temperature activated carbon particles, the high-temperature activated carbon particles of the spontaneous combustion can enter each link of the flue gas purification device along with the circulation of the activated carbon, the safe and stable operation of the sintering activated carbon flue gas purification system is threatened, and the sintering activated carbon flue gas purification device has the requirement of detecting and disposing the high-temperature spontaneous combustion activated carbon particles. As shown in fig. 1, the sintered activated carbon flue gas purification device circulates between the desorption tower and the adsorption tower, and all links such as the desorption tower, the adsorption tower, the conveyor, the vibrating screen, the buffer bin and the like are all of airtight structures.

Disclosure of Invention

Aiming at the defects in the prior art, the invention aims to provide a method and a system for extinguishing fire and reducing temperature of an active carbon bin in front of an adsorption tower. According to the invention, a thermal imager is arranged above a cover plate at the tail part of a vibrating screen of the activated carbon flue gas purification device, the thermal imager shoots materials entering an imaging area to obtain thermal imaging images, and then analyzes and judges whether the materials have high temperature points, records the found positions of the materials at the corresponding high temperature points in the imaging area, moves the high temperature materials to a bin connected with a discharge opening of a conveyor, and extinguishes and cools the high temperature materials through a spontaneous combustion activated carbon extinguishing cooling device arranged at the top of the bin. According to the technical scheme provided by the invention, the spontaneous combustion or high-temperature activated carbon is detected at the falling section at the tail part of the vibrating screen, the spontaneous combustion or high-temperature activated carbon is positioned in time, and the fire extinguishing and cooling treatment of the activated carbon is carried out in the storage bin, so that the problem that high-temperature activated carbon particles are difficult to detect and treat comprehensively is solved, and the safety of the system is improved.

According to a first embodiment of the invention, a method for extinguishing fire and reducing temperature of an activated carbon bin in front of an adsorption tower is provided.

A method for extinguishing fire and reducing temperature of an active carbon in a front storage bin of an adsorption tower comprises the following steps:

1) the thermal imaging instrument shoots the material entering the imaging area at the tail part of the vibrating screen in real time to obtain a thermal imaging image;

2) analyzing and judging whether the material entering the imaging area has a high temperature point or not according to the thermal imaging image;

2a) if the thermal imaging image does not have the high temperature point, repeating the step 1);

2b) if the thermal imaging image is judged to have a high temperature point, recording the found position of the material at the high temperature point in the imaging area at the tail part of the vibrating screen;

3) when the materials at the high-temperature point are moved into a storage bin connected with a discharge opening of the conveyor, the spontaneous combustion activated carbon extinguishing and cooling device arranged at the top of the storage bin extinguishes and cools corresponding high-temperature materials.

In the invention, the spontaneous combustion activated carbon extinguishing cooling device is a fire extinguishing gas blowing device. The fire extinguishing gas blowing device is provided with a fire extinguishing gas valve.

Preferably, in step 2b), when it is judged that the thermographic image has a high temperature point, the current time t0 is recorded. The fire extinguishing and cooling treatment in the step 3) specifically comprises the following steps:

3a1) obtain discover the distance XL1 of position to shale shaker discharge opening, the transport distance XL2 of shale shaker discharge opening to conveyer discharge opening, and the transport distance XL3 of conveyer discharge opening to feed bin top, material functioning speed V1 on the combination shale shaker, the functioning speed V2 of material on the conveyer, and the discharge speed V3 of conveyer discharge opening to feed bin, obtain the required time t1 of position of high temperature point department material from discovering the position operation to the gaseous blowing device of putting out a fire:

3a2) starting from the moment t0, after the time t1, opening a fire extinguishing gas valve of the fire extinguishing gas blowing device, and blowing fire extinguishing gas to the high-temperature materials entering the storage bin by the fire extinguishing gas blowing device.

3a3) After the fire extinguishing gas spraying device sprays fire extinguishing gas to the high-temperature material for a duration t2, closing the fire extinguishing gas valve, and enabling the high-temperature material to achieve the effect of extinguishing and cooling; wherein the duration t2 of the fire extinguishing gas blowing satisfies the following relational expression:

wherein: t2 is the duration, s, of the fire extinguishing gas blown by the fire extinguishing gas blowing device. C_hThe specific heat capacity of the activated carbon is kJ/(kg-DEG C). M_hKg is the amount of activated carbon to be cooled. Δ t_hIs the target of active carbon temperature reduction. C_nkJ/(kg. DEG C.) is the specific heat capacity of the fire extinguishing gas. Rho_nDensity of extinguishing gas, kg/m³。Δt_nThe temperature of the fire extinguishing gas is increased after the fire extinguishing gas is extinguished and cooled. S₁Is the sectional area of the spray hole m of the fire extinguishing gas spraying device²。v₁The flow velocity of the fire extinguishing gas sprayed by the fire extinguishing gas spraying and blowing device is m/s. k is a radical of₁The value is 1.5-2.5 for safety factor.

In the invention, a discharge hopper is also arranged between the conveyor and the storage bin. The discharge opening of the conveyor is connected with the inlet of the discharge hopper through a discharge conduit. The outlet of the discharge hopper is connected with the inlet of the storage bin through a feed pipe. Preferably, a plurality of discharge openings are arranged on the conveyor at intervals. A group of discharging guide pipes, a discharging hopper, a feeding pipe and a storage bin are correspondingly arranged below the discharging opening of each conveyor. And the top of each storage bin is provided with a spontaneous combustion activated carbon extinguishing and cooling device. An adsorption tower is correspondingly arranged below each stock bin.

Preferably, the number of the conveyor discharge openings is m, and the conveyor discharge openings are numbered 1,2,3 … … m in sequence according to the conveying direction of the conveyor. When a plurality of discharge openings are formed in the conveyor, the bin needing to be discharged at present is judged according to the detection of the activated carbon level meters in the adsorption towers, and then the corresponding conveyor discharge opening is determined according to the bin needing to be discharged at present. The distance between the central points of the discharge openings of two adjacent conveyors is L. Thus, equation 1 translates to:

wherein: t4 is the time, s, required for the material at the high temperature point to travel from the discovery location to the location of the mth silo.

In the invention, the vibrating screen is provided with the cover plate, and the material entering the vibrating screen moves along the length direction of the vibrating screen. Preferably, the imaging region includes a first imaging region and a second imaging region. At the end of the shaker, the first imaging zone is located upstream of the second imaging zone.

In step 1), the thermal imager shoots the material that gets into in the shale shaker tail portion imaging area in real time, obtains the thermal imaging image, specifically is:

1a) a light shield is arranged on a cover plate at the tail part of the vibrating screen, and a thermal imager is arranged at the top of the light shield;

1b) the connecting position of the thermal imaging camera and the light shield is taken as a base point, and the thermal imaging camera swings back and forth around the base point. The thermal imaging instrument shoots materials entering a first imaging area and/or a second imaging area at the tail part of the vibrating screen in real time to obtain a primary thermal imaging image and/or a secondary thermal imaging image.

In the invention, in step 2), whether the material entering the imaging area has a high temperature point is judged according to the thermal imaging image analysis, specifically:

the thermal imaging instrument shoots the material entering the first imaging area at the tail part of the vibrating screen in real time to obtain a primary thermal imaging image. The maximum temperature value T1 in the primary thermographic image is acquired and compared with the set target temperature T0 by the maximum temperature value T1. And if T1 is not more than T0, judging that the primary thermal imaging image does not have a high temperature point, and repeating the step 1). And if T1 is greater than T0, judging that the primary thermal imaging image has a suspected high-temperature point. Preferably, the value range of T0 is 390-425 ℃, and preferably 400-420 ℃.

When the primary thermal imaging image is judged to have the suspected high-temperature point, the thermal imaging instrument tracks and shoots a secondary thermal imaging image of the material at the suspected high-temperature point entering a second imaging area at the tail part of the vibrating screen, and whether the suspected high-temperature point is the high-temperature point is further judged.

Dividing the secondary thermal imaging image into n areas, obtaining the highest temperature of each of the n areas, selecting the highest temperature value T2 of the n highest temperatures, and comparing the highest temperature value T2 with a set target temperature T0. If T2 is not more than T0, the suspected high temperature point is judged to be a false high temperature point, and the step 1) is repeated. And if T2 is greater than T0, confirming that the suspected high temperature point is the high temperature point. The highest temperature value T2 corresponds to the area on the secondary thermal imaging image, so that the found position of the material on the vibrating screen in the second imaging area at the high temperature point is determined and recorded.

Preferably, the top of the light shield is also provided with a dustproof cooling protective cover. The thermal imaging camera is installed in the dustproof cooling protective cover. The thermal imaging system and the dustproof cooling protective cover are swung back and forth around the base point by taking the connecting position of the dustproof cooling protective cover and the light shield as the base point.

Preferably, a cooling medium is introduced into the dustproof cooling protection cover, and the cooling medium is ejected into the light shield from the dustproof cooling protection cover. Preferably, the cooling medium is one of compressed air, water and nitrogen. Preferably, a black coating is arranged on the inner wall of the light shield.

Preferably, the cover plate of the vibrating screen is provided with an opening. The light shield is positioned on the upper part of the opening. The width of the openings is equal or substantially equal to the width of the shaker.

Preferably, the cover plate of the vibrating screen is further provided with a first dust removal air port and a second dust removal air port. The first dust removal air opening is located at the upstream of the light shield. The second dust removal air opening is located at the downstream of the light shield. Preferably, the second dust removal air opening is obliquely arranged on an end plate at the tail part of the vibrating screen. And the dust removal device removes dust on the materials on the vibrating screen through the first dust removal air opening and/or the second dust removal air opening.

Preferably, the thermal imager is connected with a data processing module, the data processing module is connected with a main process computer control system, and meanwhile, a fire extinguishing gas valve of the fire extinguishing gas blowing device is connected with the main process computer control system. And when the thermal imaging image is judged to have a high-temperature point, the data processing module gives an alarm to the main process computer control system, and the main process computer control system realizes the fire extinguishing and cooling treatment on the corresponding high-temperature material by controlling the operation of the fire extinguishing gas valve.

According to a second embodiment of the invention, a method for extinguishing fire and reducing temperature of an activated carbon bin in front of an adsorption tower is provided.

In the invention, the spontaneous combustion activated carbon extinguishing cooling device is a cooling water spraying device. And a cooling water valve is arranged on the cooling water spraying device.

3b1) obtain discover the distance XL1 of position to shale shaker discharge opening, the transport distance XL2 of shale shaker discharge opening to conveyer discharge opening, and the transport distance XL3 of conveyer discharge opening to feed bin top, material functioning speed V1 on the combination shale shaker, the functioning speed V2 of material on the conveyer, and the discharge speed V3 of conveyer discharge opening to feed bin, obtain the required time t1 of high temperature point department material from discovery position operation to cooling water sprinkler's position:

3b2) and starting from the t0 moment, opening a cooling water valve of the cooling water spraying device after t1 time, and spraying water to the high-temperature materials entering the storage bin by the cooling water spraying device to reduce the temperature.

3b3) After the cooling water spraying device sprays water to the high-temperature material for a duration t3, closing a cooling water valve, and enabling the high-temperature material to achieve an effect of quenching and cooling; wherein the water spray duration t3 satisfies the following relation:

wherein: t2 is the duration of cooling water spray, s. C_hThe specific heat capacity of the activated carbon is kJ/(kg-DEG C). M_hKg is the amount of activated carbon to be cooled. Δ t_hIs the target of active carbon temperature reduction. C_w1kJ/(kg. DEG C.) is the specific heat capacity of water at the evaporation temperature. C_w2The specific heat capacity of water at the initial temperature, kJ/(kg. DEG C.). T is_w1The evaporation temperature of water, DEG C. Rho_wDensity of cooling water, kg/m³。T_w2Is the initial temperature of the water sprayed by the cooling water spraying device. h is_wIs the latent heat of vaporization of water at the evaporation temperature, kJ/kg. S₂Is the cross-sectional area of the spray hole of the cooling water spray device, m²。v₂The flow rate of the water sprayed from the cooling water spray device is m/s. k is a radical of₂The value is 1.2-1.9 for safety factor.

Preferably, the thermal imager is connected with a data processing module, the data processing module is connected with a main process computer control system, and a cooling water valve of the cooling water spraying device is connected with the main process computer control system. And when the thermal imaging image is judged to have a high-temperature point, the data processing module gives an alarm to the main process computer control system, and the main process computer control system realizes the fire extinguishing and cooling treatment on the corresponding high-temperature material by controlling the operation of the cooling water valve.

According to a third embodiment of the invention, a system for extinguishing fire and reducing temperature of an active carbon bin in front of an adsorption tower is provided.

A system for extinguishing fire and cooling active carbon in a front storage bin of an adsorption tower or a system for extinguishing fire and cooling active carbon in a front storage bin of the adsorption tower, which is used for the method in the first embodiment, comprises a thermal imager, a vibrating screen, a conveyor, a storage bin and a spontaneous combustion active carbon extinguishing and cooling device. And a cover plate is arranged on the vibrating screen. The thermal imaging camera is arranged above the cover plate at the tail part of the vibrating screen. The discharge opening of the vibrating screen is connected with the feed opening of the conveyor. The discharge opening of the conveyor is connected with the storage bin. The spontaneous combustion activated carbon extinguishing cooling device is arranged at the top of the storage bin. And an imaging area is arranged at the tail part of the vibrating screen.

In the invention, a discharge hopper is also arranged between the conveyor and the storage bin. The discharge opening of the conveyor is connected with the inlet of the discharge hopper through a discharge conduit. The outlet of the discharge hopper is connected with the inlet of the storage bin through a feed pipe. The feed pipe is arranged at the center of the top of the storage bin.

Preferably, a plurality of discharge openings are arranged on the conveyor at intervals along the conveying direction. A group of discharging guide pipes, a discharging hopper, a feeding pipe and a storage bin are correspondingly arranged below the discharging opening of each conveyor. And the top of each storage bin is provided with a spontaneous combustion activated carbon extinguishing and cooling device. An adsorption tower is correspondingly arranged below each stock bin.

In the invention, the discharge opening of the vibrating screen is connected with the feed opening of the conveyor, and the discharge opening of the conveyor is connected with the discharge guide pipe. Generally, the activated carbon outlet at the end of the vibrating screen includes an oversize activated carbon outlet and an undersize activated carbon outlet. The active carbon particles with the particle size larger than the sieve pore size of the sieve plate of the vibrating sieve flow out of the active carbon outlet on the sieve and enter the conveyer. The active carbon particles with the particle size smaller than the sieve pore size of the sieve plate enter the loss active carbon collecting system through the active carbon outlet under the sieve and do not enter the active carbon smoke purifying device any more. That is, the discharge opening of the vibrating screen in the present invention refers to the outlet of the activated carbon on the screen of the vibrating screen.

In the invention, the spontaneous combustion activated carbon extinguishing cooling device is a fire extinguishing gas blowing device. The fire extinguishing gas blowing device comprises a fire extinguishing gas main pipe and a fire extinguishing gas branch pipe. The fire extinguishing gas main pipe is arranged outside the storage bin. The fire extinguishing gas branch pipe is arranged at the top of the storage bin. One end of the fire extinguishing gas branch pipe is connected with the fire extinguishing gas main pipe, and the other end of the fire extinguishing gas branch pipe extends into the storage bin. And one end of the fire extinguishing gas branch pipe, which is positioned in the storage bin, is provided with a fire extinguishing gas nozzle. Preferably, the fire extinguishing gas main pipe is also provided with a fire extinguishing gas valve.

Preferably, in the fire extinguishing gas spraying apparatus, the fire extinguishing gas branch pipe is obliquely disposed at the top of the storage bin. The number of the fire extinguishing gas branch pipes is multiple, and preferably 2-12. The fire extinguishing gas branch pipes are distributed annularly around the feeding pipe at the top of the storage bin or uniformly along the circumferential direction. And one end of each fire extinguishing gas branch pipe in the storage bin is provided with a fire extinguishing gas nozzle.

Preferably, the system further comprises a light shield. The light shield is arranged on the cover plate at the tail part of the vibrating screen. The thermal imager is disposed on top of the light shield. The imaging region includes a first imaging region and a second imaging region. At the end of the shaker, the first imaging zone is located upstream of the second imaging zone. The connecting position of the thermal imaging camera and the light shield is taken as a base point, and the thermal imaging camera swings back and forth around the base point. The thermal imaging instrument shoots materials entering a first imaging area and/or a second imaging area at the tail part of the vibrating screen in real time to obtain a primary thermal imaging image and/or a secondary thermal imaging image.

Preferably, the top of the light shield is also provided with a dustproof cooling protective cover. The thermal imaging camera is installed in the dustproof cooling protective cover. The thermal imaging system and the dustproof cooling protective cover are swung back and forth around the base point by taking the connecting position of the dustproof cooling protective cover and the light shield as the base point. Preferably, the inner wall of the light shield is provided with a black coating.

Preferably, the cover plate at the tail part of the vibrating screen is provided with an opening. The light shield is positioned on the upper part of the opening. The width of the openings is equal or substantially equal to the width of the shaker.

Preferably, the system further comprises a data processing module and a main process computer control system. The thermal imager is connected with the data processing module, the data processing module is connected with the main process computer control system, and meanwhile, the fire extinguishing gas valve of the fire extinguishing gas blowing device is connected with the main process computer control system. The main process computer control system controls the operation of the data processing module, the thermal imager and the fire extinguishing gas valve.

According to a fourth embodiment of the invention, a system for extinguishing fire and reducing temperature of an activated carbon bin in front of an adsorption tower is provided.

A system for extinguishing fire and cooling active carbon in a front storage bin of an adsorption tower or a system for extinguishing fire and cooling active carbon in a front storage bin of an adsorption tower, which is used for the method in the second embodiment, comprises a thermal imager, a vibrating screen, a conveyor, a storage bin and a spontaneous combustion active carbon extinguishing and cooling device. And a cover plate is arranged on the vibrating screen. The thermal imaging camera is arranged above the cover plate at the tail part of the vibrating screen. The discharge opening of the vibrating screen is connected with the feed opening of the conveyor. The discharge opening of the conveyor is connected with the storage bin. The spontaneous combustion activated carbon extinguishing cooling device is arranged at the top of the storage bin. And an imaging area is arranged at the tail part of the vibrating screen.

In the invention, the spontaneous combustion activated carbon extinguishing cooling device is a cooling water spraying device. The cooling water spraying device comprises a cooling water main pipe, a cooling water branch pipe and an annular water pipe. The cooling water main pipe is arranged outside the storage bin. The cooling water branch pipe is arranged at the top of the storage bin. The annular water pipe is arranged at the top in the storage bin. One end of the cooling water branch pipe is connected with the cooling water main pipe, and the other end of the cooling water branch pipe extends into the storage bin and is connected with the annular water pipe. The annular water pipe is provided with a cooling water nozzle. Preferably, a cooling water valve is further arranged on the cooling water main pipe.

Preferably, in the cooling water spraying apparatus, the cooling water branch pipe is vertically disposed at the top of the bin. The number of the cooling water branch pipes is multiple, and preferably 2-12. The plurality of cooling water branch pipes are distributed annularly around the feeding pipe at the top of the storage bin or uniformly along the circumferential direction. Preferably, a plurality of cooling water nozzles are arranged on the annular water pipe and are uniformly distributed.

Preferably, the system further comprises a data processing module and a main process computer control system. The thermal imager is connected with the data processing module, the data processing module is connected with the main process computer control system, and meanwhile, the cooling water valve of the cooling water spraying device is connected with the main process computer control system. The main process computer control system controls the operation of the data processing module, the thermal imager and the cooling water valve.

As shown in fig. 1, the activated carbon flue gas purification device circulates between the desorption tower and the adsorption tower, all links such as the desorption tower, the adsorption tower, the conveyor and the buffer bin are all airtight structures, and activated carbon is in a large amount of gathering states in the above devices, and occasionally appearing high-temperature activated carbon may be surrounded by a group of normal-temperature activated carbon, so that high-temperature activated carbon particles are difficult to detect comprehensively.

In the activated carbon flue gas purification device, activated carbon circulates between an analysis tower and an adsorption tower, and all the activated carbon needs to be screened out by a vibrating screen in the circulation. The active carbon powder screening is a subsequent process of a desorption tower (a high-temperature heating link), and active carbon particles are in a rolling and flat-spreading state on a vibrating screen. Therefore, the high-temperature activated carbon particles (or the spontaneous combustion activated carbon) are detected in the activated carbon screening link, and the high-temperature activated carbon particles in the activated carbon flue gas purification process can be found more conveniently. And because the active carbon particles at the falling section of the rear end (namely the tail part) of the vibrating screen are in a parabolic shape, the active carbon particles in the falling process are more dispersed than the upper horizontal section of the vibrating screen, and the active carbon particles at the bottom layer are shielded by the active carbon particles at the surface layer to the minimum, so that the active carbon particles are easier to detect and identify by a thermal imaging instrument. Consequently, this application sets up thermal imaging system in the top of shale shaker afterbody apron, arranges here that thermal imaging system more can detect all active carbon particles comprehensively, avoids lou examining.

After the thermal imaging system detects the spontaneous combustion activated carbon particles, namely high temperature points, the relatively safe disposal mode mainly comprises: 1. discharging the spontaneous combustion activated carbon; the exhausted spontaneous combustion activated carbon often increases the loss of an activated carbon flue gas purification system, and exhausted spontaneous combustion activated carbon particles need further treatment; 2. extinguishing and cooling the spontaneous combustion activated carbon; after the spontaneous combustion activated carbon particles are extinguished, if the high-temperature state above the spontaneous combustion point is continuously maintained, spontaneous combustion can occur when the spontaneous combustion activated carbon particles meet air, so that the spontaneous combustion activated carbon particles need to be extinguished and cooled for safe disposal.

The application provides a method for extinguishing fire and reducing temperature of an active carbon front storage bin of an adsorption tower, wherein in the method, a thermal imager firstly shoots materials in an imaging area at the tail of a vibrating screen in real time to obtain a thermal imaging image; and analyzing and judging whether the material entering the imaging area has a high temperature point or not according to the thermal imaging image. And if the thermal imaging image does not have the high temperature point, the thermal imager continues to monitor the material entering the imaging area at the tail part of the vibrating screen. When the thermal imaging image is judged to have a high temperature point, recording the found position of the material at the high temperature point in the imaging area; treat that corresponding high temperature material removes to the feed bin of being connected with the conveyer discharge opening in, extinguish cooling device through the spontaneous combustion active carbon who sets up at the feed bin top and put out a fire the cooling and handle corresponding high temperature material to the realization is to the extinguishing and the cooling of high temperature material.

In the invention, the method for extinguishing fire and reducing temperature of the active carbon in the front storage bin of the adsorption tower comprises two embodiments. In a first embodiment, the spontaneous combustion activated carbon quenching cooling device is an extinguishing gas blowing device. The scheme adopts nitrogen and CO₂Inert gases and the like can insulate oxygen to extinguish fire, on one hand, the extinguishing gas can insulate oxygen to prevent high temperature and smoldering active carbon from burning to play a role in extinguishing fire, and can bring away part of heat to play a role in cooling; on the other hand, the desorption tower needs to use a large amount of nitrogen, and a nitrogen gas generating and storing device is arranged nearby, so that the fire extinguishing and cooling system can be directly used; correspondingly, there is CO nearby₂Gas-generating and gas-storing apparatus, e.g. CO produced during high-temperature calcination of limestone (or dolomite)₂Then the use of CO is also contemplated₂Used as a cooling medium to extinguish fire and reduce temperature.

In a first embodiment, the fire suppressing gas blowing means is provided at the top of the silo connected to the discharge opening of the conveyor. The fire extinguishing gas nozzle is arranged at the position of the platform at the top of the storage bin, and the activated carbon particles entering the storage bin from the feeding pipe cannot contact the position. Unloading to the feed bin in by the conveyer when the high temperature activated carbon particle that detects, high temperature activated carbon particle is in the whereabouts state, and the activated carbon particle of whereabouts state is more dispersed than other states, and each layer activated carbon particle is less to sheltering from each other, arranges the gaseous jetting device of putting out a fire promptly here, the gaseous contact of going out a fire that the gaseous jetting device of going out a fire can be more even more abundant with high temperature activated carbon particle and cladding or be full of around high temperature activated carbon particle, thereby can realize extinguishing and cooling of high temperature activated carbon particle more fast. In addition, the jetting direction of gas nozzle of putting out a fire intersects with the axis of inlet pipe, and a plurality of gas nozzles of putting out a fire are cyclic annular evenly distributed at feed bin top platform, also are favorable to realizing the temperature regulation or the accuse temperature to high temperature active carbon particle more.

In this embodiment, the time at which the high temperature activated carbon particles are found in the imaging zone at the rear of the vibrating screen is set to t 0. The time required by the high-temperature activated carbon particles to move from the found position to the storage bin is calculated according to the formula 1, namely the time when the fire extinguishing gas blowing device starts to work (namely the time when the fire extinguishing gas valve is opened), and then the time when the fire extinguishing gas blowing device stops working (namely the time when the fire extinguishing gas valve is closed) is calculated according to the heat balance between the activated carbon and the fire extinguishing gas and the formula 2. Wherein, formula 1 and formula 2 are as follows:

that is, after the time t1 elapses from the time t0, the fire extinguishing gas valve is opened, and the fire extinguishing gas blowing device starts blowing the fire extinguishing gas to the high-temperature material. And after the fire extinguishing gas spraying device sprays fire extinguishing gas to the high-temperature material for a duration t2, closing the fire extinguishing gas valve, and enabling the high-temperature material to achieve the effect of extinguishing and cooling.

Generally, the average temperature of the cooled activated carbon particles discharged from the desorption tower is about 120 to 140 ℃, the temperature of the activated carbon is lowered to a predetermined target temperature T0 or less, and the amount of the fire extinguishing gas is considered to be, for example, a temperature of 20 to 50 ℃ for the cooled activated carbon (for example, the temperature is lowered toΔt_h30 ℃ below zero. Ideally, the fire suppressing gas is heated to an average temperature of all the activated carbon particles, e.g., 125 ℃, during the heat exchange process; if the initial temperature of the extinguishing gas is 25 ℃, at this time, Δ t_n125-25-100 ℃. In formula 2, the duration t2 of the fire extinguishing and cooling of the fire extinguishing gas blowing device means that the high-temperature activated carbon particles falling from the storage bin can be fully coated with the fire extinguishing gas, oxygen is isolated, and partial heat is taken away, so that the purposes of reducing the temperature of the high-temperature and smoldering activated carbon particles and extinguishing the smoldering activated carbon particles are achieved. The duration t2 of the fire extinguishing and cooling indicates that the using amount of the fire extinguishing gas is accurately controlled, so that the technical scheme of the invention can extinguish and cool the spontaneous combustion activated carbon particles and can control the use cost of the fire extinguishing gas.

In a second embodiment, the spontaneous combustion activated carbon quenching cooling device is a cooling water spraying device. According to the scheme, water is selected as a cooling medium for extinguishing fire and reducing temperature by using active carbon. On one hand, the specific heat ratio of water to nitrogen and CO₂When the specific heat capacity of the gas is large, the temperature reduction range of water with the same volume is larger, and the required water quantity is smaller; on the other hand, the water spraying amount is less, water vapor generated after water absorbs heat when meeting the high-temperature activated carbon is less, in the application scene of the invention, spontaneous combustion or high-temperature activated carbon particles are local high-temperature points in all activated carbon particles, the volume and the range of the activated carbon particles at the high-temperature points are very small, the activated carbon particles can be rapidly cooled when meeting water, and the water vapor reaction can not occur between a small amount of water vapor and the activated carbon at a lower temperature. In addition, in view of the low cost and ready availability of water, water is used as the cooling medium in the second embodiment of the present invention.

In a second embodiment, the cooling water spray device is arranged on top of a silo connected to the discharge opening of the conveyor. A cooling water nozzle (or a water mist nozzle) is arranged at the position of the platform at the top of the storage bin, and activated carbon particles entering the storage bin from the feeding pipe cannot contact the position. In the cooling water spraying device, a cooling water branch pipe is connected with an annular water pipe suspended in a storage bin, a plurality of water mist nozzles are arranged in the annular water pipe, and water mist sprayed out of the water mist nozzles is sprayed out in a conical mode in the horizontal direction. The water mist nozzles are uniformly distributed in an annular shape, so that the active carbon particles falling into the storage bin can be fully contacted with the water mist, and the fire is extinguished and the temperature is reduced.

It should be noted that, because the feed bin is directly connected with the activated carbon inlet of the adsorption tower, the spontaneous combustion activated carbon extinguishing and cooling device is arranged at the top of the feed bin, so that the temperature of the activated carbon entering the adsorption tower can be ensured to be within a reasonable range.

In this embodiment, the time at which the high temperature activated carbon particles are found in the imaging zone at the rear of the vibrating screen is set to t 0. The time required by the high-temperature activated carbon particles to move from the found position to the storage bin is calculated according to the formula 1, namely the time when the cooling water spraying device starts to work (namely the time when the cooling water valve is opened), and then the time when the cooling water spraying device stops working (namely the time when the cooling water valve is closed) is calculated according to the heat balance between the activated carbon and the cooling water according to the formula 3. Wherein, formula 1 and formula 3 are as follows:

namely, from the time t0, after the time t1 elapses, the cooling water valve is opened, and the cooling water spraying device starts spraying water to the high-temperature material. And after the cooling water spraying device continuously sprays water for the high-temperature material for t3, closing the cooling water valve, and enabling the high-temperature material to achieve the effect of extinguishing and cooling.

Generally, the average temperature of the cooled activated carbon particles discharged from the desorption tower is about 120 to 140 ℃, the temperature of the activated carbon is lowered to a predetermined target temperature T0 or less, and the amount of cooling water is, for example, considered to reduce the temperature of the activated carbon by 15 to 20 ℃ (Δ T, for example)_h20 c) to ensure that the cooling water is completely converted to water vapour during the cooling process, i.e. liquid water is not carried into the chain bucket, when the cooling water is warmed during the heat exchange process to a water evaporation temperature at the local atmospheric pressure, e.g. 100 c. Water as described hereinThe evaporation temperature refers to the temperature of water when it evaporates rapidly in bulk. In formula 3, the duration t3 of the cooling water spraying device for extinguishing fire and reducing temperature means that the high-temperature activated carbon particles falling from the storage bin can be in uniform and sufficient contact with water mist, partial heat of the high-temperature and smoldering activated carbon is taken away, the purposes of reducing the temperature of the high-temperature and smoldering activated carbon particles and extinguishing the smoldering activated carbon particles are achieved, and meanwhile, the water mist is converted into water vapor through heat exchange. The duration t3 of the fire extinguishing and temperature reduction shows that the invention avoids the liquid water from being fed into the bin and even the whole flue gas purification device by accurately controlling the water spraying amount of the cooling water spraying device, thereby avoiding the active carbon powder from being adhered to the conveying equipment caused by the liquid water in the conveying system, and simultaneously avoiding the incompletely resolved SO in the liquid water and the active carbon₂Reaction to form H₂5O₄And corrodes the transport equipment. The invention adopts water which is low in cost and easy to obtain as a medium for extinguishing and cooling the activated carbon, reduces the use cost and avoids common technical problems which may occur when the water is used as the extinguishing and cooling medium.

In the invention, a discharge hopper is also arranged between the conveyor and the storage bin. The discharge opening of the conveyor is connected with the inlet of the discharge hopper through a discharge conduit. The outlet of the discharge hopper is connected with the inlet of the storage bin through a feed pipe. A plurality of discharge openings are arranged on the conveyor at intervals. A group of discharging guide pipes, a discharging hopper, a feeding pipe and a storage bin are correspondingly arranged below the discharging opening of each conveyor. And the top of each storage bin is provided with a spontaneous combustion activated carbon extinguishing and cooling device. An adsorption tower is correspondingly arranged below each stock bin. The number of the discharge openings of the conveyor is m, and the discharge openings of the conveyor are numbered as 1,2 and 3 … … m in sequence according to the conveying direction of the conveyor. When a plurality of discharge openings are formed in the conveyor, the bin needing to be discharged at present is judged according to the detection of the activated carbon level meters in the adsorption towers, and then the corresponding conveyor discharge opening is determined according to the bin needing to be discharged at present. The distance between the central points of the discharge openings of two adjacent conveyors is L. Thus, equation 1 translates to:

When the active carbon level meter in the adsorption tower corresponding to a certain bin detects that the active carbon level is too low, the conveyer is controlled to feed the bin. And the main control obtains the information of the number m of the discharge opening of the conveyor corresponding to the current feeding bin and transmits the information to the spontaneous combustion activated carbon extinguishing and cooling device. When the ash discharge valve on the corresponding bin is opened, the main control transmits opening information to the spontaneous combustion activated carbon extinguishing cooling device corresponding to the bin, and the spontaneous combustion activated carbon extinguishing cooling device opens the valve to extinguish fire and cool the activated carbon particles falling to the bin.

Further, in the above equations 2 and 3, M_hKg is the amount of activated carbon to be cooled. As can be seen from fig. 4, the high-temperature activated carbon particles passing through the spontaneous combustion activated carbon extinguishing and cooling device at the top of the storage bin come from a discharge device (such as a roller feeder) of the desorption tower, the amount of activated carbon to be cooled at present is the same as the flow rate of the discharge device of the desorption tower at a certain past moment, and the time length t in the middle is:

t-t 1+ t5 … … … … (equation 5).

Wherein: t1 is the time length of waiting for the fire extinguishing gas valve or cooling water valve to open the valve after the thermal imager detects the high-temperature activated carbon particles, which is unit s; t5 is a constant and represents the length of time in s that the activated carbon particles travel from the stripper discharge to the point of discovery of the high temperature activated carbon particles. Therefore, the time t0 is pushed forward for time t5, and the amount of the activated carbon to be cooled can be obtained by measuring the blanking flow of the activated carbon of the discharging device of the desorption tower at that time.

In addition, as shown in fig. 5 and 8, the conveyor is driven by a motor M, and when the motor M works, the rotating speed of the motor M is adjusted by a frequency converter VF (other speed adjusting modes are available, and the speed adjusting effect similar to that of the frequency converter can be achieved). The frequency converter VF is monitored by the master. The relationship among the running speed V2 of the material on the conveyor, the rotating speed RV of the motor M and the frequency f1 of the frequency converter VF is as follows:

v2 ═ k3 ═ k3 ═ k4 ═ f1 … … … … (formula 6);

wherein: k3 is a constant and is related to the transformation ratio of the speed reducer and the radius of the star wheel; k4 is a constant, and is related to the number of poles of the motor and the slip of the motor. By substituting equation 6 into equation 1, the delay time t1 can be determined according to the given frequency f1 of the conveyor in production.

Preferably, the specific high-temperature detection process in the method of the present invention is as follows: firstly, shooting a material entering a first imaging area at the tail part of the vibrating screen by a thermal imaging instrument to obtain a primary thermal imaging image; analyzing and judging whether the material entering the first imaging area has a suspected high-temperature point or not according to the primary thermal imaging image; tracking and shooting the material with the suspected high-temperature point in the primary thermal imaging image, and acquiring a secondary thermal imaging image of the material at the suspected high-temperature point entering the second imaging area; and analyzing and judging whether the suspected high-temperature point is a high-temperature point or not according to the secondary thermal imaging image. And when the suspected high-temperature point is confirmed to be the high-temperature point, recording the found position of the high-temperature point material in the second imaging area and giving an alarm.

In the invention, the thermal imaging image (i.e. the primary thermal imaging image or the secondary thermal imaging image) is an infrared image with temperature information, and the temperature information of the material at each point in the imaging area can be read from the thermal imaging image. Comparing the highest temperature value T1 in the primary thermographic image with the target temperature T0, it can be determined whether there is a high temperature point in the primary thermographic image. And if the T1 is not more than T0, judging that the primary thermal imaging image does not have a high-temperature point, and continuously carrying out high-temperature monitoring on the material subsequently entering the first imaging area by the thermal imaging instrument. If T1 is greater than T0, the primary thermal imaging image is judged to have a suspected high temperature point; the thermal imager further shoots the material at the suspected high-temperature point to obtain a secondary thermal imaging image of the material in the second imaging area. Dividing the secondary thermal imaging image into n regions (for example, into nine-square grids), acquiring a highest temperature value T2 in the n regions, and comparing the T2 with a target temperature T0 to determine whether the suspected high temperature point is a high temperature point. If T2 is not more than T0, the suspected high temperature point is judged to be a false high temperature point, and the thermal imager continues to monitor the high temperature of the material entering the first imaging area subsequently. If T2 is greater than T0, the suspected high temperature point is confirmed to be a high temperature point, the highest temperature value T2 corresponds to the area on the secondary thermal imaging image, and therefore the found position of the material at the high temperature point in the second imaging area is determined and an alarm is given to a main control (namely a main process computer control system). In order to further embody the accuracy or precision of the high-temperature detection, the secondary thermal imaging image can be a plurality of continuously shot pictures, and the temperature information of the material at the suspected high-temperature point in the plurality of continuously shot pictures is compared, so that more accurate judgment is made on whether the suspected high-temperature point is the high-temperature point.

In the transportation process of high-temperature materials, when the temperature of the materials reaches a certain value, oxidation exothermic reaction can occur in the materials, so that the temperature of the materials is further increased; but the vibration or the relative change of the internal position exists between the materials in the transportation process, so that the condition of the oxidation exothermic reaction of the materials can be destroyed, and the temperature of the materials is reduced. If the situation that the material is high in temperature or spontaneously combusted is directly judged through a primary thermal imaging image after a primary high-temperature point is detected, the found position of the material at the high-temperature point is marked and subjected to alarm processing, and the situation that processing is improper due to inaccurate detection is inevitable. According to the technical scheme, the process of identifying the high-temperature point materials is divided into preliminary judgment of suspected high-temperature points, tracking judgment is carried out on the suspected high-temperature points, and therefore accurate judgment data of the high-temperature points are obtained. The accurate judgment of the high temperature point of the material is also beneficial to the subsequent further processing of the material aiming at the high temperature point.

It should be noted that, in the transportation process of the material by the vibrating screen or the conveyer, local relative displacement occurs between material particles on the conveyer due to the vibration of the conveyer, so that the material which may be self-burning releases heat, and the initial suspected high temperature point is determined as the false high temperature point.

Generally speaking, the main body of the vibrating screen is a sealing structure, active carbon moves in the vibrating screen, and conventional detection modes such as a thermocouple arranged in the existing vibrating screen are difficult to capture high-temperature active carbon particles passing through rapidly. The thermal imaging camera is arranged in the vibrating screen, so that the problems of insufficient space and severe working environment (vibration and dust) exist. Therefore, the existing vibrating screen needs to be modified to meet the requirement of a thermal imaging camera on detecting high-temperature activated carbon particles.

In this application, the thermal imaging camera is disposed above the shaker tail cover plate (i.e., the thermal imaging camera is disposed independently of the shaker). Be equipped with the trompil with the shale shaker width on the apron of shale shaker afterbody, the imaging area of thermal imaging system covers the trompil width, covers the active carbon particle and the active carbon particle of a small segment horizontal segment of shale shaker rear end whereabouts section, and the thermal imaging system passes through the active carbon that the trompil flowed through on to the shale shaker sieve carries out real-time supervision. Preferably, the thermal imaging camera is arranged on the top of a light shield, and the light shield is arranged on the upper part of the opening at the tail part of the vibrating screen. The light shield is provided with a black coating to prevent light reflection. The lens hood can play the purpose of shielding external light, eliminates the interference of external light to the thermal imager. In the invention, the connecting position of the thermal imaging camera and the light shield is taken as a base point, and the thermal imaging camera performs reciprocating swing around the base point; the thermal imaging instrument shoots materials entering a first imaging area and/or a second imaging area at the tail part of the vibrating screen in real time to obtain a primary thermal imaging image and/or a secondary thermal imaging image.

Further preferably, the thermal imaging camera is mounted in a dustproof cooling protective cover, and the dustproof cooling protective cover is arranged at the top of the light shield. The tail part of the dustproof cooling protective cover (namely one end of the dustproof cooling protective cover positioned outside the light shield) is introduced with a cooling medium, the cooling medium is sprayed out from the front end of the dustproof cooling protective cover (namely one end of the dustproof cooling protective cover positioned in the light shield), and the cooling medium is used for cooling the thermal imager and ensuring that the working temperature of the thermal imager is not higher than 60 ℃. Meanwhile, the cooling medium can prevent dust from entering the thermal imager to cause instrument failure. The cooling medium of dustproof cooling safety cover's front end spun still plays clean guard action to thermal imaging system's camera lens and safety cover high definition protection lens, prevents the dust gathering, pollutes camera lens and safety cover high definition protection lens. In addition, the cooling medium sprayed out of the dustproof cooling protective cover can maintain positive pressure in the light shield, prevent external dust from entering the light shield, and prevent individual activated carbon particles from jumping out of the vibrating screen from the opening of the light shield to damage a thermal imager. The cooling medium is not particularly limited and may perform the above-described functions, and for example, the cooling medium is one of compressed air, water, and nitrogen. In the present invention, the thermal imaging system and the dust-proof cooling protective cover are reciprocated about a base point at a connecting position of the dust-proof cooling protective cover and the light shield.

In the invention, the cover plate of the vibrating screen is also provided with a first dust removal air port and a second dust removal air port. The first dust removal air opening is located at the upstream of the light shield. The second dust removal air opening is located at the downstream of the light shield. The second dust removal air port is obliquely arranged on an end plate at the tail part of the vibrating screen, and the oblique design at the position can ensure that the individual activated carbon particles entering the second dust removal air port can fall back to the vibrating screen by means of gravity. The cooling medium sprayed out of the front end of the dustproof cooling protective cover and the negative pressure of the dust removal air port remove dust in the space of the thermal imaging range, and are beneficial to improving the accuracy of thermal imaging and providing a good working environment for a thermal imager.

In the invention, the installation height, the lens and the like of the thermal imager are adjusted according to the actual situation on site. Thermal imaging system, dustproof cooling safety cover, lens hood are a whole, and this whole is independent of the shale shaker, is located the top of shale shaker afterbody apron, and is higher 1 ~ 2cm than shale shaker apron position.

In the present invention, one or more thermal imagers may be provided on top of the light shield. In specific implementation, can set up a plurality of thermal imaging cameras, shoot the material that gets into in the formation of image district through controlling a plurality of independent thermal imaging cameras and acquire the thermal imaging image to guarantee not to omit the material among the high temperature testing process, solved the problem that is difficult to detect comprehensively among the prior art. Simultaneously, the thermal imaging system does reciprocating swing around the basic point, and the position of thermal imaging system can swing along with the transport of material on the shale shaker promptly, and to the material of suspected high temperature point, the thermal imaging system can further track and judge to make and detect more accurately, also more be favorable to realizing the comprehensiveness that detects.

In the invention, the system for extinguishing fire and reducing temperature by using the active carbon on the vibrating screen further comprises a main process computer control system (for short, master control) and a data processing module. The method comprises the steps that after a thermal imager acquires a thermal imaging image of a material in an imaging area, whether a high-temperature point exists in the corresponding material or not is judged according to the thermal imaging image, data information judged as the high-temperature point is transmitted to a data processing module, the data processing module is connected with a main control, an alarm is sent to the main control, and the main control enters the next processing flow.

In the present application, the material refers to activated carbon, and is generally fresh activated carbon after being desorbed by an desorption tower.

In the present application, the terms "upstream" and "downstream" refer to the relative concepts of the flow direction of the activated carbon particles on the conveying devices such as vibrating screens, conveyors, discharge ducts, discharge hoppers, feed pipes, silos, etc., i.e., the position where the activated carbon particles pass first on the conveying device is upstream and the position where the activated carbon particles pass later is downstream.

Compared with the prior art, the invention has the following beneficial effects:

1. according to the invention, the thermal imaging system is arranged above the vibrating screen tail cover plate, and because the active carbon particles at the tail part of the vibrating screen are in a parabolic falling state, the active carbon particles are more dispersed when falling than other positions, the active carbon particles at the bottom layer are shielded by the active carbon particles at the surface layer to the minimum, and are easier to detect and identify by the thermal imaging system, namely, the thermal imaging system is arranged at the position to detect all the active carbon particles more comprehensively, and the omission is avoided.

2. According to the invention, the spontaneous combustion activated carbon extinguishing cooling device is arranged at the top of the storage bin connected with the discharge opening of the conveyor, the activated carbon particles entering the storage bin are in a falling state, the activated carbon particles in the falling state are more dispersed than other states, and the shielding among the activated carbon particles in each layer is less, so that a cooling medium sprayed by the spontaneous combustion activated carbon extinguishing cooling device can be more uniformly and more sufficiently contacted with the high-temperature activated carbon particles and covers or is filled around the high-temperature activated carbon particles, and the extinguishing and cooling of the high-temperature activated carbon particles can be more rapidly realized.

3. According to the invention, a high-temperature detection mode of the thermal imager is adopted, and accurate judgment data of the high-temperature point is obtained by preliminarily judging the suspected high-temperature point and tracking and judging the suspected high-temperature point, so that the detection accuracy is improved.

4. According to the technical scheme provided by the invention, under the condition that the materials in the imaging area at the tail part of the vibrating screen are identified to have high temperature points, the fire extinguishing gas injection amount of the fire extinguishing gas injection device can be accurately controlled, and the use cost of the fire extinguishing gas can be controlled while the high temperature materials are extinguished and cooled.

5. According to the technical scheme provided by the invention, under the condition that the materials in the imaging area at the tail part of the vibrating screen are identified to have high temperature points, the water spraying amount of the cooling water spraying device can be accurately controlled, the high-temperature materials are extinguished and cooled, meanwhile, the liquid water is prevented from being brought into a conveying system, and the safety of the system is improved.

6. The arrangement of the light shield can play a role in shielding external light and eliminate the interference of the external light on the thermal imager; meanwhile, due to the arrangement of the dustproof cooling protective cover and the introduction of a cooling medium into the dustproof cooling protective cover, the thermal imager can be cooled, dust is prevented from being accumulated, and a lens of the thermal imager and a high-definition protective lens of the protective cover are cleaned and protected.

Drawings

FIG. 1 is a schematic diagram of an activated carbon desulfurization and denitrification apparatus in the prior art;

FIG. 2 is a schematic diagram of a prior art desorption tower;

FIG. 3 is a flow chart of a method for extinguishing fire and reducing temperature of an active carbon bin in front of an adsorption tower according to the invention;

FIG. 4 is a first structural schematic diagram of a system for extinguishing a fire and cooling by using activated carbon in a front storage bin of an adsorption tower, according to the invention;

FIG. 5 is a structural schematic diagram II of a system for extinguishing fire and reducing temperature of an active carbon in a front storage bin of an adsorption tower;

FIG. 6 is a schematic structural view of the fire extinguishing gas blowing apparatus and the storage bin according to the present invention;

FIG. 7 is a top view of the fire suppressing gas blowing apparatus and the storage bin according to the present invention;

FIG. 8 is a schematic structural diagram of another system for extinguishing fire and cooling by using activated carbon in a front storage bin of an adsorption tower;

FIG. 9 is a schematic structural view of a cooling water spraying device and a storage bin according to the present invention;

FIG. 10 is a top view of the cooling water spray device and the storage bin of the present invention;

FIG. 11 is a schematic view of the present invention with multiple conveyor discharge openings and bins;

FIG. 12 is a schematic view of a thermal imager acquiring a single thermal image of the material in the first imaging region in accordance with the present invention;

FIG. 13 is a schematic diagram of a thermal imager of the present invention acquiring a second thermographic image of the material in the second imaging zone;

FIG. 14 is a diagram showing the relationship between a thermal imager, a data processing module, and a master control in the present invention;

fig. 15 is a data processing flow chart of the thermal imager of the present invention;

FIG. 16 is a logic diagram of a high temperature activated carbon particle process flow of the present invention;

FIG. 17 is a logic diagram of another high temperature activated carbon particle treatment process of the present invention.

Reference numerals:

1: a thermal imager; 2: vibrating screen; 201: a cover plate; 3: an imaging area; 301: a first imaging region; 302: a second imaging area; 4: a conveyor; 5: a storage bin; 6: a fire extinguishing gas blowing device; 601: a fire suppressing gas valve; 602: a main fire extinguishing gas pipe; 603: a fire extinguishing gas branch pipe; 604: a fire extinguishing gas nozzle; 7: a cooling water spray device; 701: a cooling water valve; 702: a cooling water main pipe; 703: cooling water branch pipes; 704: an annular water pipe; 705: a cooling water nozzle; 8: a discharge hopper; 9: a discharge conduit; 10: a feed pipe; 11: a light shield; 12: a dust-proof cooling protective cover; 13: a first dust removal tuyere; 14: a second dust removal tuyere; a1: a data processing module; a2: a main process computer control system.

Detailed Description

A system for extinguishing fire and cooling active carbon in a front storage bin of an adsorption tower or a system for extinguishing fire and cooling active carbon in a front storage bin of the adsorption tower, which is used for the method in the first embodiment, comprises a thermal imager 1, a vibrating screen 2, a conveyor 4, a storage bin 5 and a spontaneous combustion active carbon extinguishing and cooling device. And a cover plate 201 is arranged on the vibrating screen 2. The thermal imaging camera 1 is disposed above a cover plate 201 at the rear of the vibrating screen 2. The discharge opening of the vibrating screen 2 is connected with the feed opening of the conveyor 4. The discharge opening of the conveyor 4 is connected with a silo 5. The spontaneous combustion active carbon extinguishing cooling device is arranged at the top of the storage bin 5. And an imaging area 3 is arranged at the tail part of the vibrating screen 2.

In the invention, a discharge hopper 8 is also arranged between the conveyor 4 and the storage bin 5. The discharge opening of the conveyor 4 is connected to the inlet of a discharge hopper 8 via a discharge conduit 9. The outlet of the discharge hopper 8 is connected with the inlet of the storage bin 5 through a feeding pipe 10. The feed pipe 10 is arranged in a central position at the top of the silo 5.

Preferably, a plurality of discharge openings are arranged on the conveyor 4 at intervals along the conveying direction. A group of discharge conduits 9, a discharge hopper 8, a feed pipe 10 and a storage bin 5 are correspondingly arranged below the discharge opening of each conveyor 4. The top of each bin 5 is provided with a spontaneous combustion activated carbon extinguishing cooling device. An adsorption tower is correspondingly arranged below each bin 5.

In the invention, the spontaneous combustion active carbon extinguishing and cooling device is a fire extinguishing gas blowing device 6. The fire extinguishing gas blowing device 6 includes a main fire extinguishing gas pipe 602 and fire extinguishing gas branch pipes 603. The main fire extinguishing gas pipe 602 is disposed outside the silo 5. A fire extinguishing gas branch 603 is provided at the top of the silo 5. One end of the fire extinguishing gas branch pipe 603 is connected with the fire extinguishing gas main pipe 602, and the other end of the fire extinguishing gas branch pipe 603 extends into the storage bin 5. The fire extinguishing gas branch pipe 603 is provided with a fire extinguishing gas nozzle 604 at one end located in the silo 5. Preferably, a fire extinguishing gas valve 601 is further disposed on the fire extinguishing gas main pipe 602.

Preferably, in the fire extinguishing gas blowing device 6, the fire extinguishing gas branch pipes 603 are obliquely disposed at the top of the silo 5. The number of the fire extinguishing gas branch pipes 603 is plural, preferably 2 to 12. The plurality of fire suppressing gas branch pipes 603 are distributed annularly or uniformly in the circumferential direction centering on the feed pipe 10 at the top of the silo 5. Each fire suppressing gas branch pipe 603 is provided with a fire suppressing gas nozzle 604 at one end located in the storage bin 5.

Preferably, the system further comprises a light shield 11. The light shield 11 is arranged on a cover plate 201 at the tail part of the vibrating screen 2. The thermal imaging camera 1 is disposed on top of the light shield 11. The imaging zone 3 comprises a first imaging zone 301 and a second imaging zone 302. At the rear of the shaker 2, the first imaging zone 301 is located upstream of the second imaging zone 302. The thermal imaging system 1 swings back and forth around the base point of the connection position of the thermal imaging system 1 and the light shield 11. The thermal imaging camera 1 shoots materials entering a first imaging area 301 and/or a second imaging area 302 at the tail part of the vibrating screen 2 in real time to obtain a primary thermal imaging image and/or a secondary thermal imaging image.

Preferably, the top of the light shield 11 is further provided with a dustproof cooling protective cover 12. The thermal imaging camera 1 is mounted within a dust-tight cooled protective cover 12. With the connecting position of the dust-proof cooling protective cover 12 and the light shield 11 as a base point, the thermal imaging system 1 and the dust-proof cooling protective cover 12 are swung back and forth around the base point. Preferably, a black coating is provided on the inner wall of the light shield 11.

Preferably, the cover plate 201 at the rear of the vibrating screen 2 is provided with an opening. A light shield 11 is located above the aperture. The width of the openings is equal or substantially equal to the width of the vibrating screen 2.

Preferably, the cover plate 201 of the vibrating screen 2 is further provided with a first dust-removing air opening 13 and a second dust-removing air opening 14. The first dust removal tuyere 13 is located upstream of the light shield 11. The second dust removal tuyere 14 is located downstream of the light shield 11. Preferably, the second dust removal tuyere 14 is obliquely arranged on an end plate at the rear of the vibrating screen 2. The dust removing device removes dust on the materials on the vibrating screen 2 through the first dust removing air opening 13 and/or the second dust removing air opening 14.

Preferably, the system further includes a data processing module A1 and a main process computer control system A2. The thermal imaging system 1 is connected with a data processing module A1, the data processing module A1 is connected with a main process computer control system A2, and meanwhile, a fire-extinguishing gas valve 601 of the fire-extinguishing gas blowing device 6 is connected with a main process computer control system A2. The main process computer control system a2 controls the operation of the data processing module a1, the thermal imager 1, and the fire suppressing gas valve 601.

A system for extinguishing fire and reducing temperature of active carbon in a front storage bin of an adsorption tower or a system for extinguishing fire and reducing temperature of the active carbon in the front storage bin of the adsorption tower in the method of the second embodiment comprises a thermal imager 1, a vibrating screen 2, a conveyor 4, a storage bin 5 and a spontaneous combustion active carbon extinguishing and cooling device. And a cover plate 201 is arranged on the vibrating screen 2. The thermal imaging camera 1 is disposed above a cover plate 201 at the rear of the vibrating screen 2. The discharge opening of the vibrating screen 2 is connected with the feed opening of the conveyor 4. The discharge opening of the conveyor 4 is connected with a silo 5. The spontaneous combustion active carbon extinguishing cooling device is arranged at the top of the storage bin 5. And an imaging area 3 is arranged at the tail part of the vibrating screen 2.

In the invention, the spontaneous combustion activated carbon extinguishing cooling device is a cooling water spraying device 7. The cooling water spray device 7 includes a cooling water main pipe 702, a cooling water branch pipe 703, and an annular water pipe 704. The cooling water main pipe 702 is disposed outside the silo 5. A cooling water branch pipe 703 is provided at the top of the silo 5. An annular water pipe 704 is provided at the top inside the silo 5. One end of the cooling water branch pipe 703 is connected to the cooling water main pipe 702, and the other end of the cooling water branch pipe 703 extends into the silo 5 and is connected to the annular water pipe 704. The annular water pipe 704 is provided with a cooling water nozzle 705. Preferably, a cooling water valve 701 is further disposed on the cooling water main pipe 702.

Preferably, in the cooling water spray device 7, the cooling water branch pipe 703 is vertically provided at the top of the hopper 5. The number of the cooling water branch pipes 703 is plural, preferably 2 to 12. The cooling water branch pipes 703 are distributed annularly or uniformly in the circumferential direction around the feed pipe 10 at the top of the silo 5. Preferably, a plurality of cooling water nozzles 705 are arranged on the annular water pipe 704, and the plurality of cooling water nozzles 705 are uniformly distributed.

Preferably, the system further includes a data processing module A1 and a main process computer control system A2. The thermal imager 1 is connected with a data processing module A1, the data processing module A1 is connected with a main process computer control system A2, and meanwhile, a cooling water valve 701 of the cooling water spraying device 7 is connected with a main process computer control system A2. The main process computer control system a2 controls the operation of the data processing module a1, the thermal imager 1, and the cooling water valve 701.

Example 1

The utility model provides a system for feed bin active carbon extinguishment cooling before adsorption tower, this system includes that thermal imaging system 1, shale shaker 2, conveyer 4, feed bin 5, spontaneous combustion active carbon extinguish cooling device. And a cover plate 201 is arranged on the vibrating screen 2. The thermal imaging camera 1 is disposed above a cover plate 201 at the rear of the vibrating screen 2. The discharge opening of the vibrating screen 2 is connected with the feed opening of the conveyor 4. The discharge opening of the conveyor 4 is connected with a silo 5. The spontaneous combustion active carbon extinguishing cooling device is arranged at the top of the storage bin 5. And an imaging area 3 is arranged at the tail part of the vibrating screen 2.

Example 2

As shown in fig. 11, example 1 is repeated, except that a discharge hopper 8 is further provided between the conveyor 4 and the silo 5. The discharge opening of the conveyor 4 is connected to the inlet of a discharge hopper 8 via a discharge conduit 9. The outlet of the discharge hopper 8 is connected with the inlet of the storage bin 5 through a feeding pipe 10. The feed pipe 10 is arranged in a central position at the top of the silo 5. And a plurality of discharge openings are arranged on the conveyor 4 at intervals along the conveying direction. A group of discharge conduits 9, a discharge hopper 8, a feed pipe 10 and a storage bin 5 are correspondingly arranged below the discharge opening of each conveyor 4. The top of each bin 5 is provided with a spontaneous combustion activated carbon extinguishing cooling device. An adsorption tower is correspondingly arranged below each bin 5.

Example 3

As shown in fig. 12 and 13, embodiment 2 is repeated except that the system further comprises a light shield 11. The light shield 11 is arranged on a cover plate 201 at the tail part of the vibrating screen 2. The thermal imaging camera 1 is disposed on top of the light shield 11. The imaging zone 3 comprises a first imaging zone 301 and a second imaging zone 302. At the rear of the shaker 2, the first imaging zone 301 is located upstream of the second imaging zone 302. The thermal imaging system 1 swings back and forth around the base point of the connection position of the thermal imaging system 1 and the light shield 11. The thermal imaging system 1 shoots materials entering a first imaging area 301 and a second imaging area 302 at the tail part of the vibrating screen 2 in real time to obtain a primary thermal imaging image and a secondary thermal imaging image.

Example 4

Example 3 is repeated except that the top of the light shield 11 is also provided with a dust-proof cooling protective cover 12. The thermal imaging camera 1 is mounted within a dust-tight cooled protective cover 12. With the connecting position of the dust-proof cooling protective cover 12 and the light shield 11 as a base point, the thermal imaging system 1 and the dust-proof cooling protective cover 12 are swung back and forth around the base point. And a black coating is arranged on the inner wall of the light shield 11.

Example 5

Example 4 is repeated except that the cover plate 201 at the rear of the vibrating screen 2 is provided with openings. A light shield 11 is located above the aperture. The width of the opening is equal to the width of the vibrating screen 2.

Example 6

Example 5 was repeated except that the cover plate 201 of the vibrating screen 2 was further provided with a first dust-removing tuyere 13 and a second dust-removing tuyere 14. The first dust removal tuyere 13 is located upstream of the light shield 11. The second dust removal tuyere 14 is located downstream of the light shield 11. The second dust removal tuyere 14 is obliquely arranged on an end plate at the rear of the vibrating screen 2. The dust removing device removes dust on the materials on the vibrating screen 2 through the first dust removing air opening 13 and the second dust removing air opening 14.

Example 7

As shown in fig. 4, 6 and 7, example 6 was repeated except that the spontaneous combustion activated carbon quenching cooling device was a fire extinguishing gas blowing device 6. The fire extinguishing gas blowing device 6 includes a main fire extinguishing gas pipe 602 and fire extinguishing gas branch pipes 603. The main fire extinguishing gas pipe 602 is disposed outside the silo 5. A fire extinguishing gas branch 603 is provided at the top of the silo 5. One end of the fire extinguishing gas branch pipe 603 is connected with the fire extinguishing gas main pipe 602, and the other end of the fire extinguishing gas branch pipe 603 extends into the storage bin 5. The fire extinguishing gas branch pipe 603 is provided with a fire extinguishing gas nozzle 604 at one end located in the silo 5. The fire extinguishing gas main pipe 602 is also provided with a fire extinguishing gas valve 601.

Example 8

Example 7 was repeated except that in the fire extinguishing gas blowing device 6, the fire extinguishing gas branch pipes 603 were disposed obliquely at the top of the silo 5. The number of fire suppressing gas branch pipes 603 is 4. The 4 fire extinguishing gas branch pipes 603 are distributed annularly centering on the feeding pipe 10 at the top of the silo 5. Each fire suppressing gas branch pipe 603 is provided with a fire suppressing gas nozzle 604 at one end located in the storage bin 5.

Example 9

As shown in FIG. 5, example 8 was repeated except that the system further included a data processing module A1 and a main process computer control system A2. The thermal imaging system 1 is connected with a data processing module A1, the data processing module A1 is connected with a main process computer control system A2, and meanwhile, a fire-extinguishing gas valve 601 of the fire-extinguishing gas blowing device 6 is connected with a main process computer control system A2. The main process computer control system a2 controls the operation of the data processing module a1, the thermal imager 1, and the fire suppressing gas valve 601.

Example 10

As shown in fig. 8 to 10, example 6 was repeated except that the spontaneous combustion activated carbon quenching cooling device was a cooling water spraying device 7. The cooling water spray device 7 includes a cooling water main pipe 702, a cooling water branch pipe 703, and an annular water pipe 704. The cooling water main pipe 702 is disposed outside the silo 5. A cooling water branch pipe 703 is provided at the top of the silo 5. An annular water pipe 704 is provided at the top inside the silo 5. One end of the cooling water branch pipe 703 is connected to the cooling water main pipe 702, and the other end of the cooling water branch pipe 703 extends into the silo 5 and is connected to the annular water pipe 704. The annular water pipe 704 is provided with a cooling water nozzle 705. A cooling water valve 701 is further arranged on the cooling water main pipe 702.

Example 11

Example 10 was repeated except that in the cooling water spray device 7, the cooling water branch pipes 703 were vertically disposed at the top of the silo 5. The number of the cooling water branch pipes 703 is 4. The 4 cooling water branch pipes 703 are annularly distributed centering on the feeding pipe 10 at the top of the storage bin 5. The annular water pipe 704 is provided with a plurality of cooling water nozzles 705, and the plurality of cooling water nozzles 705 are uniformly distributed.

Example 12

As shown in FIG. 14, example 11 was repeated except that the system further included a data processing module A1 and a main process computer control system A2. The thermal imager 1 is connected with a data processing module A1, the data processing module A1 is connected with a main process computer control system A2, and meanwhile, a cooling water valve 701 of the cooling water spraying device 7 is connected with a main process computer control system A2. The main process computer control system a2 controls the operation of the data processing module a1, the thermal imager 1, and the cooling water valve 701.

Example 13

As shown in fig. 3, a method for extinguishing fire and reducing temperature by using activated carbon in a front storage bin of an adsorption tower comprises the following steps:

1) the thermal imaging instrument 1 shoots the material entering the imaging area 3 at the tail part of the vibrating screen 2 in real time to obtain a thermal imaging image;

2) analyzing and judging whether the material entering the imaging area 3 has a high temperature point or not according to the thermal imaging image;

2b) if the thermal imaging image is judged to have a high temperature point, recording the found position of the material at the high temperature point in the imaging area 3 at the tail part of the vibrating screen 2;

3) when the material at the high temperature point moves to the bin 5 connected with the discharge opening of the conveyor 4, the spontaneous combustion activated carbon extinguishing and cooling device arranged at the top of the bin 5 extinguishes corresponding high-temperature materials and cools the corresponding high-temperature materials.

Example 14

Example 13 is repeated except that the vibrating screen 2 is provided with a cover plate 201, and the material entering the vibrating screen 2 moves along the length direction of the vibrating screen 2. The imaging zone 3 comprises a first imaging zone 301 and a second imaging zone 302. At the rear of the shaker 2, the first imaging zone 301 is located upstream of the second imaging zone 302.

In step 1), the thermal imaging instrument 1 shoots the material entering the vibrating screen 2 tail imaging area 3 in real time to obtain a thermal imaging image, which specifically comprises:

1a) a light shield 11 is arranged on a cover plate 201 at the tail part of the vibrating screen 2, and the thermal imaging camera 1 is arranged at the top of the light shield 11;

1b) the thermal imaging system 1 swings back and forth around the base point of the connection position of the thermal imaging system 1 and the light shield 11. The thermal imaging system 1 shoots materials entering a first imaging area 301 and a second imaging area 302 at the tail part of the vibrating screen 2 in real time to obtain a primary thermal imaging image and a secondary thermal imaging image.

Example 15

As shown in fig. 15, the embodiment 14 is repeated, except that in step 2), whether the material entering the imaging area 3 has a high temperature point is judged according to the thermal imaging image analysis, specifically:

the thermal imaging instrument 1 shoots the material entering the first imaging area 301 at the tail part of the vibrating screen 2 in real time to obtain a primary thermal imaging image. The maximum temperature value T1 in the primary thermographic image is acquired and compared with the set target temperature T0 by the maximum temperature value T1. And if T1 is not more than T0, judging that the primary thermal imaging image does not have a high temperature point, and repeating the step 1). And if T1 is greater than T0, judging that the primary thermal imaging image has a suspected high-temperature point. T0 has a value of 415 ℃.

When the primary thermal imaging image is judged to have the suspected high-temperature point, the thermal imaging instrument 1 tracks and shoots a secondary thermal imaging image of the material at the suspected high-temperature point entering the second imaging area 302 at the tail part of the vibrating screen 2, and further judges whether the suspected high-temperature point is the high-temperature point.

Dividing the secondary thermal imaging image into 9 areas of the nine-square grid, obtaining the highest temperature of each of the 9 areas, selecting the highest temperature value T2 of the 9 highest temperatures, and comparing the highest temperature value T2 with a set target temperature T0. If T2 is not more than T0, the suspected high temperature point is judged to be a false high temperature point, and the step 1) is repeated. And if T2 is greater than T0, confirming that the suspected high temperature point is the high temperature point. The highest temperature value T2 is used to correspond to the area on the secondary thermal image, so as to determine and record the found position of the material on the vibrating screen 2 in the second imaging area 302.

Example 16

Example 15 was repeated except that the top of the light shield 11 was also provided with a dust-proof cooling protective cover 12. The thermal imaging camera 1 is mounted within a dust-tight cooled protective cover 12. With the connecting position of the dust-proof cooling protective cover 12 and the light shield 11 as a base point, the thermal imaging system 1 and the dust-proof cooling protective cover 12 are swung back and forth around the base point. And a cooling medium is introduced into the dustproof cooling protective cover 12, and is sprayed out of the dustproof cooling protective cover 12 into the light shield 11. The cooling medium is compressed air. And a black coating is arranged on the inner wall of the light shield 11.

Example 17

Example 16 is repeated except that the cover plate 201 of the vibrating screen 2 is provided with openings. A light shield 11 is located above the aperture. The width of the opening is equal to the width of the vibrating screen 2.

Example 18

Example 17 was repeated except that the cover plate 201 of the vibrating screen 2 was further provided with a first dust-removing tuyere 13 and a second dust-removing tuyere 14. The first dust removal tuyere 13 is located upstream of the light shield 11. The second dust removal tuyere 14 is located downstream of the light shield 11. The second dust removal tuyere 14 is obliquely arranged on an end plate at the rear of the vibrating screen 2. The dust removing device removes dust on the materials on the vibrating screen 2 through the first dust removing air opening 13 and the second dust removing air opening 14.

Example 19

Example 18 was repeated except that the spontaneous combustion activated carbon quenching cooling device was the fire extinguishing gas blowing device 6. The fire extinguishing gas blowing device 6 is provided with a fire extinguishing gas valve 601. The fire extinguishing gas is nitrogen.

As shown in fig. 16, in step 2b), when it is judged that the thermographic image has a high temperature point, the current time t0 is recorded. The fire extinguishing and cooling treatment in the step 3) specifically comprises the following steps:

3a1) obtain the distance XL1 of discovery position to shale shaker 2 discharge opening, the transport distance XL2 of shale shaker 2 discharge opening to 4 discharge openings of conveyer, and the transport distance XL3 of 4 discharge openings of conveyer to 5 tops of feed bin, material functioning speed V1 on the combination shale shaker 2, functioning speed V2 of material on the conveyer 4, and the discharge speed V3 of 4 discharge openings of conveyer to 5 feed bin, obtain the required time t1 of position of high temperature point department material from discovery position operation to the gaseous device of jetting of fire extinguishing 6:

3a2) starting from the time t0, after the time t1 elapses, the fire extinguishing gas valve 601 of the fire extinguishing gas blowing device 6 is opened, and the fire extinguishing gas blowing device 6 blows fire extinguishing gas to the high-temperature material entering the silo 5.

3a3) After the fire extinguishing gas blowing device 6 blows the fire extinguishing gas to the high-temperature material for the duration time t2, the fire extinguishing gas valve 601 is closed, and the high-temperature material achieves the effect of extinguishing and cooling. Wherein the duration t2 of the fire extinguishing gas blowing satisfies the following relational expression:

wherein: t2 is the duration, s, of the fire extinguishing gas blown by the fire extinguishing gas blowing device. C_hThe specific heat capacity of the activated carbon is kJ/(kg-DEG C). M_hKg is the amount of activated carbon to be cooled. Delta th is the active carbon cooling target, DEG C. Cn is the specific heat capacity of the fire extinguishing gas, kJ/(kg-DEG C). Rho_nDensity of extinguishing gas, kg/m³。Δt_nThe temperature of the fire extinguishing gas is increased after the fire extinguishing gas is extinguished and cooled. S₁Is the sectional area of the spray hole m of the fire extinguishing gas spraying device²。v₁The flow velocity of the fire extinguishing gas sprayed by the fire extinguishing gas spraying and blowing device is m/s. k is a radical of₁The value is 1.5-2.5 for safety factor.

Example 20

Example 19 was repeated except that the thermal imaging camera 1 was connected to a data processing module a1, the data processing module a1 was connected to the main process computer control system a2, and the fire suppressing gas valve 601 of the fire suppressing gas spraying apparatus 6 was connected to the main process computer control system a 2. When the thermal imaging image is judged to have a high temperature point, the data processing module A1 gives an alarm to the main process computer control system A2, and the main process computer control system A2 realizes the fire extinguishing and temperature reducing treatment on the corresponding high-temperature material by controlling the operation of the fire extinguishing gas valve 601.

Example 21

Example 18 was repeated except that the spontaneous combustion activated carbon quenching cooling device was the cooling water spraying device 7. A cooling water valve 701 is provided on the cooling water spraying device 7.

As shown in fig. 17, in step 2b), when it is judged that the thermographic image has a high temperature point, the current time t0 is recorded. The fire extinguishing and cooling treatment in the step 3) specifically comprises the following steps:

3b1) obtain the distance XL1 of discovery position to shale shaker 2 discharge opening, the transport distance XL2 of shale shaker 2 discharge opening to 4 discharge openings of conveyer, and the transport distance XL3 of 4 discharge openings of conveyer to 5 tops of feed bin, material functioning speed V1 on the combination shale shaker 2, functioning speed V2 of material on the conveyer 4, and the discharge speed V3 of 4 discharge openings of conveyer to 5 feed bin, obtain the required time t1 of the position of high temperature point department material from discovery position operation to cooling water sprinkler 7:

3b2) starting from the time t0, after the time t1 elapses, the cooling water valve 701 of the cooling water spraying device 7 is opened, and the cooling water spraying device 7 sprays water to the high-temperature material entering the storage bin 5 to reduce the temperature.

3b3) After the cooling water spraying device 7 sprays water to the high-temperature material for a duration t3, closing the cooling water valve 701, and enabling the high-temperature material to achieve an effect of extinguishing and cooling; wherein the water spray duration t3 satisfies the following relation:

wherein: t2 is the duration of cooling water spray, s. C_hThe specific heat capacity of the activated carbon is kJ/(kg-DEG C). M_hKg is the amount of activated carbon to be cooled. Δ t_hIs the target of active carbon temperature reduction. C_w1To the evaporation temperatureThe specific heat capacity of water, kJ/(kg. DEG C.). C_w2The specific heat capacity of water at the initial temperature, kJ/(kg. DEG C.). T is_w1The evaporation temperature of water, DEG C. Rho_wDensity of cooling water, kg/m³。T_w2Is the initial temperature of the water sprayed by the cooling water spraying device. h is_wIs the latent heat of vaporization of water at the evaporation temperature, kJ/kg. S₂Is the cross-sectional area of the spray hole of the cooling water spray device, m²。v₂The flow rate of the water sprayed from the cooling water spray device is m/s. k is a radical of₂The value is 1.2-1.9 for safety factor.

Example 22

Example 21 is repeated except that the thermal imager 1 is connected to a data processing module a1, the data processing module a1 is connected to the main process computer control system a2, and the cooling water valve 701 of the cooling water spraying device 7 is connected to the main process computer control system a 2. When the thermal imaging image is judged to have a high temperature point, the data processing module A1 gives an alarm to the main process computer control system A2, and the main process computer control system A2 realizes the fire extinguishing and temperature reduction treatment on the corresponding high-temperature material by controlling the operation of the cooling water valve 701.

Example 23

Example 22 is repeated, except that a discharge hopper 8 is also provided between the conveyor 4 and the silo 5. The discharge opening of the conveyor 4 is connected to the inlet of a discharge hopper 8 via a discharge conduit 9. The outlet of the discharge hopper 8 is connected with the inlet of the storage bin 5 through a feeding pipe 10. A plurality of discharge openings are arranged on the conveyor 4 at intervals. A group of discharge conduits 9, a discharge hopper 8, a feed pipe 10 and a storage bin 5 are correspondingly arranged below the discharge opening of each conveyor 4. The top of each bin 5 is provided with a spontaneous combustion activated carbon extinguishing cooling device. An adsorption tower is correspondingly arranged below each bin 5.

The number of the discharge openings of the conveyor 4 is m, and the discharge openings of the conveyor 4 are numbered as 1,2 and 3 … … m in sequence according to the conveying direction of the conveyor 4. When a plurality of discharge openings are formed in the conveyor 4, the bin 5 which needs to be discharged at present is judged according to the detection of the activated carbon level meters in the adsorption towers, and the corresponding discharge opening of the conveyor 4 is determined according to the bin 5 which needs to be discharged at present. The distance between the central points of the discharge openings of two adjacent conveyors 4 is L. Thus, equation 1 translates to:

Application example 1

A method for extinguishing fire and reducing temperature of an activated carbon bin in front of an adsorption tower by using the system in the embodiment 9 comprises the following steps:

1) the thermal imaging instrument 1 shoots materials entering a first imaging area 301 at the tail part of the vibrating screen 2 in real time to obtain a primary thermal imaging image;

2) and analyzing and judging whether the material entering the imaging area 3 has a high temperature point according to the primary thermal imaging image:

the maximum temperature value T1 in the primary thermal imaging image is acquired as 200 ℃, and the maximum temperature value T1 is compared with the set target temperature T0. T0 has a value of 390 ℃. Since T1 < T0, the primary thermographic image was judged not to have a high temperature point. Repeat step 1).

Application example 2

the maximum temperature value T1 in the primary thermal imaging image is obtained as 422 ℃, and the maximum temperature value T1 is compared with the set target temperature T0. T0 has a value of 415 ℃. Since T1 > T0, the primary thermographic image is judged to have a suspected high temperature point.

The thermal imaging system 1 tracks and shoots a secondary thermal imaging image of the material at the suspected high-temperature point entering the second imaging area 302 at the tail part of the vibrating screen 2, and further judges whether the suspected high-temperature point is a high-temperature point:

dividing the secondary thermal imaging image into nine-grid squares, obtaining the highest temperature of each of the 9 areas, selecting the highest temperature value T2 of the 9 highest temperatures as 424 ℃, and comparing the highest temperature value T2 with a set target temperature T0. Since T2 > T0, the suspected high temperature point was confirmed to be a high temperature point. The highest temperature value T2 corresponds to the area on the secondary thermal imaging image, so that the found position of the material at the high temperature point in the second imaging area 302 at the tail part of the vibrating screen 2 is determined and recorded.

The spontaneous combustion active carbon extinguishing cooling device is a fire extinguishing gas blowing device 6. The fire extinguishing gas is nitrogen. When it is judged that the thermal imaging image has a high temperature point, the current time t0 is recorded. The fire extinguishing and cooling treatment in the step 3) specifically comprises the following steps:

3a1) acquiring a distance XL1 between the discovery position and a discharge opening of the vibrating screen 2 to be 2.5m, a conveying distance XL2 between the discharge opening of the vibrating screen 2 and a discharge opening of the conveyor 4 to be 100m, and a conveying distance XL3 between the discharge opening of the conveyor 4 and the top of the storage bin 5 to be 3.5m, and acquiring a time t1 required by the material at the high temperature point to run from the discovery position to the position of the fire extinguishing gas spraying device 6 in combination with a material running speed V1 on the vibrating screen 2 to be 50mm/s, a material running speed V2 on the conveyor 4 to be 200mm/s, and a material discharging speed V3 between the discharge opening of the conveyor 4 and the storage bin 5 to be 350 mm/s:

wherein: t2 is the duration, s, of the fire extinguishing gas blown by the fire extinguishing gas blowing device. C_hIs the specific heat capacity of activated carbon, C_h＝0.84kJ/(kg·℃)。M_hAmount of activated carbon to be cooled, M_h＝1kg。Δt_hFor activated carbon cooling target, Δ t_h＝50℃。C_nSpecific heat capacity of extinguishing gas, C_n＝1.30kJ/(kg·℃)。ρ_nDensity of extinguishing gas, p_n＝1.25kg/m³。Δt_nFor the temperature, delta t, of the extinguishing gas after being cooled down for extinguishing a fire_n＝35℃。S₁Is the sectional area of the spray hole S of the fire extinguishing gas spraying device₁＝3.6×10^-3m²。v₁Velocity of flow v of extinguishing gas to be sprayed out of the extinguishing gas spraying device₁100 m/s. The fire extinguishing gas is nitrogen, the nozzle is 3 double-sided air knives with the length of 0.3m, the hole width of 2mm and the k₁For safety factor, the value is 1.7.

Application example 3

A method for extinguishing fire and reducing temperature of an activated carbon bin in front of an adsorption tower by using the system in the embodiment 12, comprising the following steps of:

the maximum temperature value T1 in the primary thermal imaging image is obtained as 419 ℃, and this maximum temperature value T1 is compared with the set target temperature T0. T0 has a value of 415 ℃. Since T1 > T0, the primary thermographic image is judged to have a suspected high temperature point.

dividing the secondary thermal imaging image into nine-grid squares, obtaining the highest temperature of each of the 9 areas, selecting the highest temperature value T2 of the 9 highest temperatures as 420 ℃, and comparing the highest temperature value T2 with a set target temperature T0. Since T2 > T0, the suspected high temperature point was confirmed to be a high temperature point. The highest temperature value T2 corresponds to the area on the secondary thermal imaging image, so that the found position of the material at the high temperature point in the second imaging area 302 at the tail part of the vibrating screen 2 is determined and recorded.

The spontaneous combustion active carbon extinguishment cooling device is a cooling water spraying device 7. A cooling water valve 701 is provided on the cooling water spraying device 7. When it is judged that the thermal imaging image has a high temperature point, the current time t0 is recorded. The fire extinguishing and cooling treatment in the step 3) specifically comprises the following steps:

3b1) acquiring a distance XL1 between the discovery position and a discharge opening of the vibrating screen 2 to be 2.5m, a conveying distance XL2 between the discharge opening of the vibrating screen 2 and a discharge opening of the conveyor 4 to be 100m, and a conveying distance XL3 between the discharge opening of the conveyor 4 and the top of the storage bin 5 to be 3.5m, and acquiring a time t1 required by the material at the high temperature point to run from the discovery position to the position of the cooling water spraying device 7 in combination with a material running speed V1 on the vibrating screen 2 to be 50mm/s, a material running speed V2 on the conveyor 4 to be 200mm/s, and a material discharging speed V3 between the discharge opening of the conveyor 4 and the storage bin 5 to be 350 mm/s:

wherein: t2 is the duration of cooling water spray, s. C_hIs the specific heat capacity of activated carbon, C_h＝0.84kJ/(kg·℃)。M_hAmount of activated carbon to be cooled, M_h＝0.5kg。Δt_hFor activated carbon cooling target, Δ t_h＝80℃。C_w1Specific heat capacity of water at evaporation temperature, C_w1＝4.22kJ/(kg·℃)。C_w2Specific heat capacity of water at initial temperature, C_w2＝4.191kJ/(kg·℃)。T_w1Is the evaporation temperature of water, T_w1At 100 ℃. ρ w is the density of the cooling water, ρ_w，＝999.7kg/m³。T_w2Initial temperature, T, of water sprayed for cooling water spray device_w2＝10℃。h_wThe latent heat of vaporization of water at the evaporation temperature, h_w＝2256.6kJ/kg。S₂Is the cross-sectional area of the spray hole of the cooling water spray device, S₂＝1.77×10^-6m²。v₂Flow rate of water sprayed to cooling water spray device, v₂8 m/s. The nozzles are 1 atomizing nozzle with the diameter of the spray hole of 1.5mm, k₂For safety factor, the value is 1.5.

Claims

1. A method for extinguishing fire and reducing temperature of an active carbon in a front storage bin of an adsorption tower comprises the following steps:

1) the thermal imaging instrument (1) shoots materials entering the tail imaging area (3) of the vibrating screen (2) in real time to obtain a thermal imaging image;

2) analyzing and judging whether the material entering the imaging area (3) has a high temperature point or not according to the thermal imaging image;

2b) if the thermal imaging image is judged to have a high temperature point, recording the found position of the material at the high temperature point in the imaging area (3) at the tail part of the vibrating screen (2);

3) when the materials at the high-temperature point are moved into a storage bin (5) connected with a discharge opening of the conveyor (4), the spontaneous combustion activated carbon extinguishing and cooling device arranged at the top of the storage bin (5) extinguishes corresponding high-temperature materials and cools the corresponding high-temperature materials.

2. The method of claim 1, wherein: the spontaneous combustion active carbon extinguishing cooling device is a fire extinguishing gas blowing device (6); the fire extinguishing gas blowing device (6) is provided with a fire extinguishing gas valve (601);

preferably, in step 2b), when the thermographic image is judged to have a high temperature point, recording the current time t 0; the fire extinguishing and cooling treatment in the step 3) specifically comprises the following steps:

3a1) obtain discover the distance XL1 of position to shale shaker (2) discharge opening, conveying distance XL2 of shale shaker (2) discharge opening to conveyer (4) discharge opening, and the conveying distance XL3 of conveyer (4) discharge opening to feed bin (5) top, material functioning speed V1 on combination shale shaker (2), functioning speed V2 of material on conveyer (4), and the discharge speed V3 of conveyer (4) discharge opening to feed bin (5), obtain the required time t1 of position that the high temperature point department material moved to the fire extinguishing gas blowing device (6) from discovering the position:

3a2) starting from the moment t0, after the time t1, opening a fire extinguishing gas valve (601) of the fire extinguishing gas blowing device (6), wherein the fire extinguishing gas blowing device (6) blows fire extinguishing gas to high-temperature materials entering a storage bin (5);

3a3) after the fire extinguishing gas spraying and blowing device (6) sprays fire extinguishing gas to the high-temperature material for a duration t2, closing the fire extinguishing gas valve (601), and enabling the high-temperature material to achieve the effect of extinguishing and cooling; wherein the duration t2 of the fire extinguishing gas blowing satisfies the following relational expression:

wherein: t2 is the duration, s, of the fire extinguishing gas blown by the fire extinguishing gas blowing device; c_hThe specific heat capacity of the activated carbon is kJ/(kg DEG C); m_hKg of the amount of activated carbon to be cooled; Δ t_hThe temperature of the active carbon is reduced to the target value of DEG C; c_nkJ/(kg. DEG C) which is the specific heat capacity of the fire extinguishing gas; rho_nDensity of extinguishing gas, kg/m³；Δt_nThe temperature of the fire extinguishing gas is increased after the fire extinguishing gas is extinguished and cooled; s₁Is the sectional area of the spray hole m of the fire extinguishing gas spraying device²；v₁The flow speed of the fire extinguishing gas sprayed out by the fire extinguishing gas spraying and blowing device is m/s; k is a radical of₁The value is 1.5-2.5 for safety factor.

3. The method of claim 1, wherein: the spontaneous combustion activated carbon extinguishing cooling device is a cooling water spraying device (7); a cooling water valve (701) is arranged on the cooling water spraying device (7);

3b1) obtaining a distance XL1 from a discovery position to a discharge opening of a vibrating screen (2), a conveying distance XL2 from the discharge opening of the vibrating screen (2) to a discharge opening of a conveyor (4), and a conveying distance XL3 from the discharge opening of the conveyor (4) to the top of a storage bin (5), combining a material running speed V1 on the vibrating screen (2), a running speed V2 of a material on the conveyor (4), and a discharging speed V3 from the discharge opening of the conveyor (4) to the storage bin (5), and obtaining a time t1 required by the material at the high temperature point to run from the discovery position to the position of the cooling water spraying device (7):

3b2) starting from the time t0, after the time t1, opening a cooling water valve (701) of the cooling water spraying device (7), and spraying water to the high-temperature material entering the storage bin (5) by the cooling water spraying device (7) for cooling;

3b3) after the cooling water spraying device (7) sprays water to the high-temperature materials for a duration t3, closing a cooling water valve (701), and enabling the high-temperature materials to achieve the effect of quenching; wherein the water spray duration t3 satisfies the following relation:

wherein: t2 is the duration of time, s, for which the cooling water spray device sprays water; c_hThe specific heat capacity of the activated carbon is kJ/(kg DEG C); m_hKg of the amount of activated carbon to be cooled; Δ t_hThe temperature of the active carbon is reduced to the target value of DEG C; c_w1The specific heat capacity of water at the evaporation temperature, kJ/(kg. DEG C); c_w2The specific heat capacity of water at the initial temperature, kJ/(kg. DEG C); t is_w1The evaporation temperature of water, DEG C; rho_wDensity of cooling water, kg/m³；T_w2The initial temperature of the water sprayed by the cooling water spraying device is DEG C; h is_wIs the latent heat of vaporization of water at the evaporation temperature, kJ/kg; s₂Is the cross-sectional area of the spray hole of the cooling water spray device, m²；v₂The flow speed of water sprayed by the cooling water spraying device is m/s; k is a radical of₂The value is 1.2-1.9 for safety factor.

4. A method according to claim 2 or 3, characterized in that: a discharge hopper (8) is also arranged between the conveyor (4) and the storage bin (5); the discharge opening of the conveyor (4) is connected with the inlet of a discharge hopper (8) through a discharge conduit (9); the outlet of the discharge hopper (8) is connected with the inlet of the storage bin (5) through a feed pipe (10); preferably, a plurality of discharge openings are arranged on the conveyor (4) at intervals; a group of discharging conduits (9), a discharging hopper (8), a feeding pipe (10) and a storage bin (5) are correspondingly arranged below the discharging opening of each conveyor (4); the top of each bin (5) is provided with a spontaneous combustion activated carbon extinguishing cooling device; an adsorption tower is correspondingly arranged below each stock bin (5);

preferably, the number of the discharge openings of the conveyor (4) is m, and the discharge openings of the conveyor (4) are numbered as 1,2 and 3 … … m in sequence according to the conveying direction of the conveyor (4); when the conveyor (4) is provided with a plurality of discharge openings, judging the bin (5) needing to be discharged at present according to the detection of the activated carbon level indicator in each adsorption tower, and determining the corresponding discharge opening of the conveyor (4) according to the bin (5) needing to be discharged at present; the distance between the central points of the discharge openings of the two adjacent conveyors (4) is L; thus, equation 1 translates to:

5. The method according to any one of claims 1-4, wherein: a cover plate (201) is arranged on the vibrating screen (2), and materials entering the vibrating screen (2) move along the length direction of the vibrating screen (2); preferably, the imaging zone (3) comprises a first imaging zone (301) and a second imaging zone (302); at the end of the shaker (2), the first imaging zone (301) is located upstream of the second imaging zone (302);

in step 1), the thermal imaging instrument (1) shoots the material entering the vibrating screen (2) tail imaging area (3) in real time to obtain a thermal imaging image, which specifically comprises the following steps:

1a) a light shield (11) is arranged on a cover plate (201) at the tail part of the vibrating screen (2), and the thermal imager (1) is arranged at the top of the light shield (11);

1b) taking the connecting position of the thermal imaging camera (1) and the light shield (11) as a base point, and reciprocating swinging the thermal imaging camera (1) around the base point; the thermal imaging system (1) shoots materials entering a first imaging area (301) and/or a second imaging area (302) at the tail of the vibrating screen (2) in real time to obtain a primary thermal imaging image and/or a secondary thermal imaging image.

6. The method of claim 5, wherein: in the step 2), whether the material entering the imaging area (3) has a high temperature point is judged according to the thermal imaging image analysis, and the method specifically comprises the following steps:

the thermal imaging instrument (1) shoots materials entering a first imaging area (301) at the tail part of the vibrating screen (2) in real time to obtain a primary thermal imaging image; acquiring a highest temperature value T1 in a primary thermal imaging image, and comparing the highest temperature value T1 with a set target temperature T0; if T1 is not more than T0, judging that the primary thermal imaging image does not have a high temperature point, and repeating the step 1); if T1 is greater than T0, the primary thermal imaging image is judged to have a suspected high temperature point; preferably, the value range of T0 is 390-425 ℃, and preferably 400-420 ℃;

when the suspected high-temperature point is found in the primary thermal imaging image, the thermal imaging instrument (1) tracks and shoots a secondary thermal imaging image of the material at the suspected high-temperature point entering a second imaging area (302) at the tail of the vibrating screen (2), and further judges whether the suspected high-temperature point is the high-temperature point;

dividing the secondary thermal imaging image into n areas, obtaining the highest temperature of each of the n areas, selecting the highest temperature value T2 of the n highest temperatures, and comparing the highest temperature value T2 with a set target temperature T0; if T2 is not more than T0, judging the suspected high temperature point as a false high temperature point, and repeating the step 1); if T2 is greater than T0, confirming that the suspected high temperature point is a high temperature point; the highest temperature value T2 corresponds to the area on the secondary thermal imaging image, so that the found position of the material at the high temperature point in the second imaging area (302) on the vibrating screen (2) is determined and recorded.

7. The method according to claim 5 or 6, characterized in that: the top of the light shield (11) is also provided with a dustproof cooling protective cover (12); the thermal imaging camera (1) is arranged in the dustproof cooling protective cover (12); taking the connecting position of the dustproof cooling protective cover (12) and the light shield (11) as a base point, and reciprocating swinging the thermal imaging system (1) and the dustproof cooling protective cover (12) around the base point;

preferably, a cooling medium is introduced into the dustproof cooling protective cover (12), and the cooling medium is sprayed out of the dustproof cooling protective cover (12) into the light shield (11); preferably, the cooling medium is one of compressed air, water and nitrogen; preferably, a black coating is arranged on the inner wall of the light shield (11).

8. The method according to any one of claims 5-7, wherein: a cover plate (201) of the vibrating screen (2) is provided with an opening; the light shield (11) is positioned at the upper part of the opening; the width of the opening is equal or basically equal to the width of the vibrating screen (2); and/or

A first dust removal air port (13) and a second dust removal air port (14) are further formed in the cover plate (201) of the vibrating screen (2); the first dust removal air port (13) is positioned at the upstream of the light shield (11); the second dust removal air port (14) is positioned at the downstream of the light shield (11); preferably, the second dust removal air port (14) is obliquely arranged on an end plate at the tail part of the vibrating screen (2); the dust removal device removes dust on the materials on the vibrating screen (2) through the first dust removal air opening (13) and/or the second dust removal air opening (14).

9. The method according to any one of claims 1-8, wherein: the thermal imager (1) is connected with a data processing module (A1), the data processing module (A1) is connected with a main process computer control system (A2), and meanwhile, a fire extinguishing gas valve (601) of a fire extinguishing gas blowing device (6) or a cooling water valve (701) of a cooling water spraying device (7) is connected with the main process computer control system (A2); when the thermal imaging image is judged to have a high-temperature point, the data processing module (A1) gives an alarm to the main process computer control system (A2), and the main process computer control system (A2) realizes the fire extinguishing and temperature reduction treatment on the corresponding high-temperature material by controlling the operation of the fire extinguishing gas valve (601) or the cooling water valve (701).

10. A system for extinguishing fire and cooling active carbon in a storage bin in front of an adsorption tower or a system for extinguishing fire and cooling active carbon in a storage bin in front of an adsorption tower, which is used for the method in any one of claims 1 to 9, and comprises a thermal imaging camera (1), a vibrating screen (2), a conveyor (4), a storage bin (5) and a spontaneous combustion active carbon extinguishing cooling device; a cover plate (201) is arranged on the vibrating screen (2); the thermal imaging system (1) is arranged above a cover plate (201) at the tail part of the vibrating screen (2); the discharge opening of the vibrating screen (2) is connected with the feed opening of the conveyor (4); the discharge opening of the conveyor (4) is connected with the stock bin (5); the spontaneous combustion activated carbon extinguishing cooling device is arranged at the top of the storage bin (5); and an imaging area (3) is arranged at the tail part of the vibrating screen (2).

11. The system of claim 10, wherein: a discharge hopper (8) is also arranged between the conveyor (4) and the storage bin (5); the discharge opening of the conveyor (4) is connected with the inlet of a discharge hopper (8) through a discharge conduit (9); the outlet of the discharge hopper (8) is connected with the inlet of the storage bin (5) through a feed pipe (10); the feeding pipe (10) is arranged at the center of the top of the storage bin (5);

preferably, a plurality of discharge openings are arranged on the conveyor (4) at intervals along the conveying direction; a group of discharging conduits (9), a discharging hopper (8), a feeding pipe (10) and a storage bin (5) are correspondingly arranged below the discharging opening of each conveyor (4); the top of each bin (5) is provided with a spontaneous combustion activated carbon extinguishing cooling device; an adsorption tower is correspondingly arranged below each stock bin (5).

12. The system according to claim 10 or 11, characterized in that: the spontaneous combustion active carbon extinguishing cooling device is a fire extinguishing gas blowing device (6); the fire extinguishing gas blowing device (6) comprises a fire extinguishing gas main pipe (602) and a fire extinguishing gas branch pipe (603); the fire extinguishing gas main pipe (602) is arranged outside the storage bin (5); the fire extinguishing gas branch pipe (603) is arranged at the top of the storage bin (5); one end of the fire extinguishing gas branch pipe (603) is connected with the fire extinguishing gas main pipe (602), and the other end of the fire extinguishing gas branch pipe (603) extends into the storage bin (5); one end of the fire extinguishing gas branch pipe (603) positioned in the storage bin (5) is provided with a fire extinguishing gas nozzle (604); preferably, the fire extinguishing gas main pipe (602) is also provided with a fire extinguishing gas valve (601);

preferably, in the fire extinguishing gas blowing device (6), the fire extinguishing gas branch pipe (603) is obliquely arranged at the top of the storage bin (5); the number of the fire extinguishing gas branch pipes (603) is multiple, preferably 2-12; a plurality of fire extinguishing gas branch pipes (603) are annularly distributed or uniformly distributed along the circumferential direction by taking a feeding pipe (10) at the top of the storage bin (5) as a center; and one end of each fire extinguishing gas branch pipe (603) positioned in the storage bin (5) is provided with a fire extinguishing gas nozzle (604).

13. The system according to claim 10 or 11, characterized in that: the spontaneous combustion activated carbon extinguishing cooling device is a cooling water spraying device (7); the cooling water spraying device (7) comprises a cooling water main pipe (702), a cooling water branch pipe (703) and an annular water pipe (704); the cooling water main pipe (702) is arranged outside the storage bin (5); the cooling water branch pipe (703) is arranged at the top of the storage bin (5); the annular water pipe (704) is arranged at the top in the storage bin (5); one end of the cooling water branch pipe (703) is connected with the cooling water main pipe (702), and the other end of the cooling water branch pipe (703) extends into the storage bin (5) and is connected with the annular water pipe (704); a cooling water nozzle (705) is arranged on the annular water pipe (704); preferably, a cooling water valve (701) is further arranged on the cooling water main pipe (702);

preferably, in the cooling water spraying device (7), the cooling water branch pipe (703) is vertically arranged at the top of the storage bin (5); the number of the cooling water branch pipes (703) is multiple, preferably 2-12; a plurality of cooling water branch pipes (703) are annularly distributed or uniformly distributed along the circumferential direction by taking a feeding pipe (10) at the top of the storage bin (5) as a center; preferably, a plurality of cooling water nozzles (705) are arranged on the annular water pipe (704), and the plurality of cooling water nozzles (705) are uniformly distributed.

14. The system according to any one of claims 10-13, wherein: the system further comprises a light shield (11); the light shield (11) is arranged on a cover plate (201) at the tail part of the vibrating screen (2); the thermal imaging camera (1) is arranged on the top of the light shield (11); the imaging zone (3) comprises a first imaging zone (301) and a second imaging zone (302); at the end of the shaker (2), the first imaging zone (301) is located upstream of the second imaging zone (302); taking the connecting position of the thermal imaging camera (1) and the light shield (11) as a base point, and reciprocating swinging the thermal imaging camera (1) around the base point; the thermal imaging instrument (1) shoots materials entering a first imaging area (301) and/or a second imaging area (302) at the tail of the vibrating screen (2) in real time to obtain a primary thermal imaging image and/or a secondary thermal imaging image;

preferably, the top of the light shield (11) is also provided with a dustproof cooling protective cover (12); the thermal imaging camera (1) is arranged in the dustproof cooling protective cover (12); taking the connecting position of the dustproof cooling protective cover (12) and the light shield (11) as a base point, and reciprocating swinging the thermal imaging system (1) and the dustproof cooling protective cover (12) around the base point; preferably, a black coating is arranged on the inner wall of the light shield (11).

15. The system of claim 14, wherein: a cover plate (201) at the tail part of the vibrating screen (2) is provided with an opening; the light shield (11) is positioned at the upper part of the opening; the width of the opening is equal or basically equal to the width of the vibrating screen (2); and/or

16. The system according to any one of claims 10-15, wherein: the system also includes a data processing module (A1) and a main process computer control system (A2); the thermal imager (1) is connected with a data processing module (A1), the data processing module (A1) is connected with a main process computer control system (A2), and meanwhile, a fire extinguishing gas valve (601) of a fire extinguishing gas blowing device (6) or a cooling water valve (701) of a cooling water spraying device (7) is connected with the main process computer control system (A2); the main process computer control system (A2) controls the operation of the data processing module (A1), the thermal imager (1), the fire extinguishing gas valve (601) and the cooling water valve (701).