CN107670655A - The offline regenerating active carbon purifier of integral type and offline regenerating active carbon cleaning system - Google Patents
The offline regenerating active carbon purifier of integral type and offline regenerating active carbon cleaning system Download PDFInfo
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- CN107670655A CN107670655A CN201710842957.4A CN201710842957A CN107670655A CN 107670655 A CN107670655 A CN 107670655A CN 201710842957 A CN201710842957 A CN 201710842957A CN 107670655 A CN107670655 A CN 107670655A
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- active carbon
- desorption chamber
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 162
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 90
- 230000001172 regenerating effect Effects 0.000 title claims abstract description 90
- 238000004140 cleaning Methods 0.000 title claims description 9
- 238000003795 desorption Methods 0.000 claims abstract description 136
- 230000003197 catalytic effect Effects 0.000 claims abstract description 118
- 238000006555 catalytic reaction Methods 0.000 claims abstract description 37
- 238000000746 purification Methods 0.000 claims abstract description 12
- 238000002485 combustion reaction Methods 0.000 claims description 31
- 238000001179 sorption measurement Methods 0.000 claims description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 26
- 238000010438 heat treatment Methods 0.000 claims description 20
- 238000005485 electric heating Methods 0.000 claims description 10
- 239000007921 spray Substances 0.000 claims description 9
- 238000001514 detection method Methods 0.000 claims description 7
- 230000017525 heat dissipation Effects 0.000 claims description 6
- 238000011069 regeneration method Methods 0.000 abstract description 11
- 230000008929 regeneration Effects 0.000 abstract description 8
- 239000007789 gas Substances 0.000 description 47
- 241000196324 Embryophyta Species 0.000 description 23
- 239000003054 catalyst Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 239000003610 charcoal Substances 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000004880 explosion Methods 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 241001466460 Alveolata Species 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 239000010425 asbestos Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000009418 renovation Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 229910052895 riebeckite Inorganic materials 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000009967 tasteless effect Effects 0.000 description 1
- 230000036413 temperature sense Effects 0.000 description 1
- 238000009279 wet oxidation reaction Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/34—Regenerating or reactivating
- B01J20/3416—Regenerating or reactivating of sorbents or filter aids comprising free carbon, e.g. activated carbon
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/34—Regenerating or reactivating
- B01J20/3483—Regenerating or reactivating by thermal treatment not covered by groups B01J20/3441 - B01J20/3475, e.g. by heating or cooling
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/07—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases in which combustion takes place in the presence of catalytic material
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- Organic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Materials Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
The present invention provides a kind of offline regenerating active carbon purifier of integral type, and it includes integral paralell, desorption chamber, catalytic combustor, main air blower, admission line, outlet pipe and controller；Desorption chamber, catalytic combustor, main air blower are mounted on integral paralell；Desorption chamber is provided with desorption chamber air inlet and desorption chamber gas outlet, and catalytic combustor is provided with catalytic combustor air inlet, catalytic combustor gas outlet；One end connection catalytic combustor gas outlet of admission line, other end connection desorption chamber air inlet；One end connection desorption chamber gas outlet of outlet pipe, the other end connect the inlet end of main air blower, the outlet side connection catalytic combustor air inlet of main air blower；Heater and catalysis burning bed are provided with catalytic combustor.The offline regenerating active carbon purifier of integral type provided in an embodiment of the present invention, desorption and regeneration purification is carried out to activated carbon by the way of offline, it is safer.
Description
Technical field
The present invention relates to regenerating active carbon field, the offline regenerating active carbon purifier of especially a kind of integral type and offline
Regenerating active carbon cleaning system.
Background technology
Activated carbon is nonpoisonous and tasteless because having highly developed pore structure and suitable specific surface area, to organic principle matter
Coloured molecule has very strong adsorption capacity, often as a kind of excellent adsorbent, be widely used in medicine, metallurgy, food,
The every field such as chemical industry, military affairs and environmental protection.In recent years, with the raising of people's social environment consciousness, activated carbon is in environment
Demand in terms of protection is increasing, is widely used in urban water supply purification, pernicious gas absorption, drinking water purification and work
Among industry Sewage advanced treatment.However, because activated carbon is on the high side, the resources of production are more and more in short supply, if will be useless after use
Activated carbon takes the modes such as burning, landfill to dispose, and will certainly cause the serious waste of resource, while also brought necessarily to environment
Influence, significantly limit the application of activated carbon.Therefore, the regeneration of waste active carbon has good development trend.
Regenerating active carbon, refer to do not destroying activated carbon original structure with the methods of fortune physics, chemistry or biochemistry
Under the premise of, deactivated charcoal after adsorption saturation is handled, recovers its absorption property, reaches the purpose of reuse.It is living
The renovation process of property charcoal has many kinds, such as：Thermal regeneration method, bio-regeneration method, wet oxidation process, solvent regeneration process, electrification
Learn method of reproduction, catalytic wet air oxidation etc..Wherein, thermal regeneration method is to apply at most, industrially most ripe regenerating active carbon
Method.But current thermal reclamation technology there is high energy consumption, efficiency is low, security is poor the problems such as.It is for example, existing online
Formula regenerating active carbon purifier, it is directly to be connected by pipeline with adsorption plant, hot gas is passed through in adsorption plant, to absorption
Activated carbon in equipment is desorbed, then the air after desorption is burnt in catalytic combustor.Fire caused by catalysis burning
Flower, is easily accessible in adsorption plant and its plant tail gas pipeline of connection, triggers fire even explosion accident.
The content of the invention
In view of the shortcomings of the prior art, it is an object of the present invention to provide a kind of offline regenerating active carbon of safer integral type is net
Makeup is put and offline regenerating active carbon cleaning system.
In order to solve the above technical problems, the present invention provides a kind of offline regenerating active carbon purifier of integral type, it includes
Integral paralell, desorption chamber, catalytic combustor, main air blower, admission line, outlet pipe and controller；The desorption chamber, catalysis
Combustion chamber, main air blower are mounted on the integral paralell；The desorption chamber is provided with desorption chamber air inlet and desorption chamber goes out
Gas port, the catalytic combustor are provided with catalytic combustor air inlet, catalytic combustor gas outlet；One end of the admission line
The catalytic combustor gas outlet is connected, the other end connects the desorption chamber air inlet；One end connection institute of the outlet pipe
Desorption chamber gas outlet is stated, the other end connects the inlet end of the main air blower, the outlet side connection catalysis combustion of the main air blower
Burn room air inlet；Heater and catalysis burning bed are provided with the catalytic combustor, the heater and catalysis are burnt
Bed is arranged between the catalytic combustor air inlet and catalytic combustor gas outlet.
Preferably, the air inlet valve group is provided with the admission line, the outlet is provided with the outlet pipe
Valve group, the catalytic combustor gas outlet are provided with discharge duct, and the exhaust valve group is provided with the discharge duct, described
Combustion supervision module is additionally provided with catalytic combustor；The controller is electrically connected with the combustion supervision module and exhaust valve group
Connect, for the opening according to the testing result of the combustion supervision module control exhaust valve group and closing.
Preferably, the combustion supervision module includes the first temperature sensor and second temperature sensor, first temperature
Sensor is spent adjacent to the heater, and second temperature sensor is adjacent to the catalysis burning bed, the second temperature sensor
When the temperature of detection is more than the temperature of first temperature sensor detection, the controller opens the exhaust valve group.
Preferably, the offline regenerating active carbon purifier of the integral type, which also includes, is arranged on the integral paralell
Water tank, the spray head that is arranged in the desorption chamber and is connected with the water tank and be connected to the spray head and the water tank it
Between water pump.
Preferably, the water pump is electrically connected with the controller；It is provided with the desorption chamber air inlet and the control
The three-temperature sensor that device processed is electrically connected with, the 4th be electrically connected with the controller is provided with the desorption chamber gas outlet
Temperature sensor；When the temperature value that the 4th temperature sensor is measured is higher by the temperature value that three-temperature sensor is measured,
The controller control water pump is opened to be sprayed to the desorption chamber.
Preferably, the offline regenerating active carbon purifier of the integral type also includes the alarm being connected with the controller
Device, when the temperature value that the 4th temperature sensor is measured is higher by the temperature value that three-temperature sensor is measured, the control
Device control alarm sends alarm signal.
Preferably, the desorption chamber air inlet is arranged at the top of the desorption chamber, and the desorption chamber gas outlet is arranged at
The bottom of the desorption chamber, the desorption chamber air inlet are diagonally set with desorption chamber gas outlet in the desorption chamber.
Preferably, the electro-heat equipment is electric heating tube, and the electric heating tube includes S bend pipe body and is arranged at the S types
Spiral heat dissipation piece on body, the spiral heat dissipation piece are made up of multiple spiral elements being integrated that are connected with each other.
Preferably, multiple equally distributed projections are also formed with the spiral element.
Preferably, the electric heating tube includes the S bend pipe body of two or more concatenations.
Preferably, the offline regenerating active carbon purifier of the integral type also includes warm-up cycle pipeline, and the preheating follows
The first end in endless tube road is connected with the inlet end of the main air blower, and the second end of the warm-up cycle pipeline is burnt with the catalysis
Room connects, and air circulation duct is formed between the catalytic combustor and the warm-up cycle pipeline, main air blower, the air follows
Ring passage is through the heater and is catalyzed burning bed, and first circulation valve group is additionally provided with the warm-up cycle pipeline.
Preferably, outlet valve group is provided with the outlet pipe, described in the second end connection of the warm-up cycle pipeline
Admission line, is provided with second circulation valve group on the admission line, and the second end of the warm-up cycle pipeline is positioned at described the
Between two Circulation valves and the catalytic combustor gas outlet, the first end of the warm-up cycle pipeline passes through the outlet pipe
Connected with the inlet end of the main air blower, and between the outlet valve group and the inlet end of the main air blower, in preheating shape
State, the first circulation valve group are opened, and the second circulation valve group and outlet valve group are closed；Followed in detachment status, described second
Ring valve group and outlet valve group are opened, and the first circulation valve group is closed.
Preferably, the offline regenerating active carbon purifier of the integral type also includes the first benefit air-cooler, and described first mends
Air-cooler connects the admission line；And/or also include second and mend air-cooler, described second, which mends air-cooler, connects the escape pipe
Road, and between the desorption chamber gas outlet and the inlet end of the main air blower.
Preferably, the first benefit air-cooler and the second benefit air-cooler electrically connect with the controller, in benefit cold state
When, the main air blower, the first benefit air-cooler and the second benefit air-cooler are run.
Preferably, housing is provided with the integral paralell, workplace is provided with the housing, the desorption chamber is set
In in the housing, and separated by dividing plate and the workplace, the catalytic combustor, main air blower and outlet pipe are respectively provided with
In in the workplace, the admission line is located at the top of the catalytic combustor and desorption chamber.
Preferably, the desorption chamber is provided with the first door body, and the workplace is provided with the second door body.
Preferably, the offline regenerating active carbon purifier of the integral type also includes transporter, and the transporter is used
In the desorption chamber that the activated carbon of outside is transported to the offline regenerating active carbon purifier of the integral type.
Preferably, the transporter is transfer car(buggy).
Preferably, the offline regenerating active carbon purifier of the integral type also includes the rail being engaged with the transfer car(buggy)
Road, one end of the track connect the desorption chamber, the outside adsorption plant of other end connection, and the transfer car(buggy) is arranged at the rail
On road.
Preferably, be provided with the retaining rail being engaged with the transfer car(buggy) in the desorption chamber, the retaining rail with it is described
Track is engaged, and the retaining rail is directed at one end of the track connection desorption chamber.
Preferably, the retaining rail being engaged with the transfer car(buggy) is provided with the desorption chamber.
The embodiment of the present invention also provides a kind of offline regenerating active carbon cleaning system, and it includes adsorption plant and any of the above-described
The offline regenerating active carbon purifier of integral type described in embodiment, the adsorption plant and the offline activated carbon of the integral type are again
Raw purifier interval pre-determined distance, the transporter are used to the activated carbon in the adsorption plant being transported to the one
The desorption chamber of the offline regenerating active carbon purifier of formula.
Compared to online regenerating active carbon purifier, the offline regenerating active carbon of integral type provided in an embodiment of the present invention
Purifier and offline regenerating active carbon cleaning system, desorption and regeneration purification is carried out to activated carbon by the way of offline, therefore
Spark caused by catalysis burning will not be entered in the exhaust system that adsorption plant is connected, so as to avoid the occurrence of fire even
It is the generation of explosion accident, it is safer.
Brief description of the drawings
Fig. 1 is the structural representation of the offline regenerating active carbon purifier of integral type provided by the invention.
Fig. 2 is the structural representation for the offline regenerating active carbon purifier of integral type that another embodiment of the present invention provides.
Fig. 3 is the stereochemical structure front schematic view of Fig. 1 offline regenerating active carbon purifier of integral type.
Fig. 4 is the stereochemical structure schematic rear view of Fig. 1 offline regenerating active carbon purifier of integral type.
Fig. 5 is the structural representation of the heater in Fig. 1.
Fig. 6 is the structural representation of the spiral element in Fig. 5.
Fig. 7 is the structural representation of offline regenerating active carbon cleaning system provided by the invention.
Fig. 8 is the structural representation of catalytic combustor in another embodiment.
Embodiment
Technical solution of the present invention is described in further detail with specific embodiment below in conjunction with the accompanying drawings, so that this area
Technical staff can be better understood from the present invention and can be practiced, but illustrated embodiment is not as a limitation of the invention.
Referring to figs. 1 to Fig. 8, the embodiment of the present invention provides a kind of offline regenerating active carbon purifier of integral type, and it includes
Catalytic combustor 2, catalytic combustor 2 are provided with catalytic combustor air inlet 23, catalytic combustor gas outlet 24, heater
222 and catalysis burning bed 221.Catalytic combustor air inlet 23 can be arranged in the side wall of catalytic combustor 2, catalytic combustor
Gas outlet 24 may be disposed at the top of catalytic combustor 2.Heater 222 is used to carry out the air for entering catalytic combustor 2
Heating.The catalyst for the organic principle in air be catalyzed burning, catalysis combustion can be placed on catalysis burning bed 221
Loose structure can be had by burning bed 221, and air passes through the loose structure, can obtain preferable catalytic effect.
The offline regenerating active carbon purifier of the integral type also includes warm-up cycle pipeline 10, and the of warm-up cycle pipeline 10
One end connects with the inlet end of main air blower 3, and the outlet side of main air blower 3 connects with catalytic combustor 2, and the of warm-up cycle pipeline 10
Two ends are connected with catalytic combustor 2, and air circulation is formed between catalytic combustor 2 and warm-up cycle pipeline 10, main air blower 3 and is led to
Road, air circulation duct is through heater 222 and is catalyzed burning bed 221, from the point of view of the path of air circulation, heater
222 and catalysis burning bed 221 be arranged between catalytic combustor air inlet 23 and catalytic combustor gas outlet 24.Warm-up cycle pipe
First circulation valve group 7 is additionally provided with road 10, for opening or closing warm-up cycle pipeline 10.In the present embodiment, first follow
Ring valve group 7 is the combining structure of hand-operated valve and motor-driven valve, and in other embodiments, first circulation valve group 7 can be hand-operated valve,
It can be motor-driven valve.
Because the catalyst placed on catalysis burning bed 221 is needed after reaching certain temperature, there could be preferably catalysis
Effect, therefore before air output is desorbed to activated carbon, first can be preheated air.During preheating, control the
One Circulation valve 7, opens warm-up cycle pipeline 10, then starts heater 222 and main air blower 3, air are roused by main air blower 3
Enter in catalytic combustor 2, then heated by heater 222, the air after heating fires catalysis through catalysis burning bed 221
The catalyst heating on bed 221 is burnt, then air enters warm-up cycle pipeline 10, in main air blower further out catalytic combustor 2
Under 3 drive, and blasted in catalytic combustor 2, so circulation, catalyst is heated.
With reference to figure 1, Fig. 3 and Fig. 4, in a preferred embodiment, the offline regenerating active carbon purifier of the integral type also includes
Desorption chamber 1, admission line 13, outlet pipe 14, discharge duct 6, outlet valve group 16 and exhaust valve group 61.Desorption chamber 1 is used to put
The activated carbon of purification to be regenerated is put, desorption chamber 1 is provided with desorption chamber air inlet 11 and desorption chamber gas outlet 12.Desorption chamber air inlet
11 can be arranged at the top of desorption chamber 1, and desorption chamber gas outlet 12 can be arranged at the bottom of desorption chamber 1.Admission line 13
One end connection catalytic combustor gas outlet 24, other end connection desorption chamber air inlet 11, for by catalytic combustor gas outlet 24
The hot-air of discharge is transported to desorption chamber air inlet 11.In a further preferred embodiment, be additionally provided with admission line 13 into
Air valve group 15, for opening or closing admission line 13, air inlet valve group 15 can be that hand-operated valve, motor-driven valve or both combine.Go out
One end connection desorption chamber gas outlet 12 of feed channel 14, the other end connects the inlet end of main air blower 3, for by the work of desorption chamber 1
Property charcoal desorption after air be delivered to main air blower 3, and be further delivered to by main air blower 3 in catalytic combustor 2.Outlet pipe
Outlet valve group 16 is provided with 14, for opening or closing outlet pipe 14, outlet valve group 16 can also be hand-operated valve with it is electronic
The combining structure of valve.The outlet side connection catalytic combustor air inlet 23 of main air blower 3.Discharge duct 6 connects catalytic combustor and gone out
Gas port 24, chimney 62 can be provided with discharge duct 6, for the air after burning to be emitted.Set on discharge duct 6
There is exhaust valve group 61, for controlling opening and the closing of discharge duct 6.The second end connection admission line of warm-up cycle pipeline 10
13, namely the second end of warm-up cycle pipeline 10 is connected by admission line 13 with catalytic combustor gas outlet 24.In other realities
Apply in example, the second end of warm-up cycle pipeline 10 can also be directly connected to catalytic combustor gas outlet 24.
In a preferred embodiment, desorption chamber air inlet 11 is arranged at the top of desorption chamber 1, and desorption chamber gas outlet 12 is arranged at
The bottom of desorption chamber 1, desorption chamber air inlet 11 is diagonally set with desorption chamber gas outlet 12 in desorption chamber 1, such as desorption chamber is entered
Gas port 11 is arranged on the upper left corner of desorption chamber 1, and desorption chamber gas outlet 12 is arranged on the lower right corner of desorption chamber 1.By diagonally setting,
Allow hot-air that the activated carbon in desorption chamber 1 is fully contacted and is desorbed.
With reference to figure 1 and Fig. 3, in a preferred embodiment, second circulation valve group 8 is provided with admission line 13, from air stream
Logical path sees that the second end of warm-up cycle pipeline 10 is between second circulation valve group 8 and catalytic combustor gas outlet 24,
One Circulation valve 7 is adjacent to the first end of warm-up cycle pipeline 10, namely first circulation valve group 7 is to the first of warm-up cycle pipeline 10
The distance at end is less than first circulation valve group 7 to the distance at the second end of warm-up cycle pipeline 10, specifically, first circulation valve group
7 close to the end of the first end of warm-up cycle pipeline 10.In other embodiments, first circulation valve group 7 can also neighbouring preheating
Second end of circulating line 10.Second circulation valve group 8 is used for opening and the closing for controlling admission line 13.Second circulation valve group 8
When opening and the closing of first circulation valve group 7, the hot-air come out from catalytic combustor gas outlet 24 can pass through admission line 13
Desorption chamber 1 is entered, when second circulation valve group 8 is closed and first circulation valve group 7 is opened, is come out from catalytic combustor gas outlet 24
Hot-air can enter warm-up cycle pipeline 10.
In a preferred embodiment, the offline regenerating active carbon purifier of the integral type also includes controller (not shown) and combustion
Detection module is burnt, combustion supervision module is arranged in catalytic combustor 2, controller and combustion supervision module and the electricity of exhaust valve group 61
Connection.Combustion supervision module is used to detect whether catalytic combustor 2 is in fired state.Controller is according to combustion supervision module
The opening of testing result control exhaust valve group 61 and closing.Burnt when combustion supervision module is detected in catalytic combustor 2
When, controller control exhaust valve group 61 is opened, and the air after burning is discharged from discharge duct 6.When combustion supervision module
Detect that then control exhaust valve group 61 is closed when not burnt in catalytic combustor 2.In a further preferred embodiment,
Combustion supervision module includes the first temperature sensor 224 and second temperature sensor 223, the first temperature sensor 224 it is neighbouring plus
Thermal 222, the neighbouring catalysis burning bed 221 of second temperature sensor 223.The first temperature sensor of meaning 224 is neighbouring herein adds
Thermal 222 refers to that the distance of the first temperature sensor 224 to heater 222 is less than the first temperature sensor 224 to catalysis
The distance of burning bed 221, similarly, the neighbouring catalysis burning bed 221 of second temperature sensor 223 refer to second temperature sensor
223 to catalysis burning bed 221 distance be less than second temperature sensor 223 to heater 222 distance.Second temperature senses
When the temperature that device 223 detects is more than the temperature of the first temperature sensor 224 detection, illustrate that the air in catalytic combustor 2 occurs
Burning, now controller, which is opened, is vented valve group 61.In other embodiments, combustion supervision module can also be arranged on by one
Temperature sensor near catalysis burning bed 221 is examined to detect whether burning, or even by light sensor etc.
Survey burning.
With reference to figure 1 and Fig. 3, in a preferred embodiment, the offline regenerating active carbon purifier of integral type has pre- Warm status
And detachment status.In pre- Warm status, first circulation valve group 7 is opened, second circulation valve group 8, outlet valve group 16 and exhaust valve group 61
Close, start heater 222 and main air blower 3, air blast catalytic combustor by main air blower 3 from catalytic combustor air inlet 23
In 2, then heated by heater 222, the air after heating will be catalyzed urging on burning bed 221 through catalysis burning bed 221
Agent heats, and then air leaves catalytic combustor 2 from catalytic combustor gas outlet 24 again, and preheating is entered from admission line 13
Circulating line 10, under the swabbing action of main air blower 3, enter outlet pipe 14, and by main air blower 3 from catalytic combustor air inlet
Mouth 23 is blasted in catalytic combustor 2, so circulation, and catalyst is heated.In detachment status, second circulation valve group 8 and go out
Air valve group 16 is opened, and is vented valve group 61 and first circulation valve group 7 is closed, now the air after being circulated throughout has reached a constant temperature
Degree, the catalyst being catalyzed on burning bed 221 have also reached the temperature of suitable catalysis, the heat discharged from catalytic combustor gas outlet 24
Air is entered in desorption chamber 1 by second circulation valve group 8 and admission line 13, is carried out to being placed on Alveolate activated carbon therein
Heating desorption, the organic principle of charcoal absorption is evaporated into air, carry volatilization after organic principle air again from
Outlet pipe 14 is delivered in catalytic combustor 2.Repeatedly after circulation desorption, the organic principle in air reaches finite concentration, and
The temperature of air is gradually heated by the sonochemical activity to ignition temperature, and now air is through burning after catalysis burning bed 221, organic principle change
For carbon dioxide and water, the air after burning is expelled in air from exhaust passage 6.
With reference to figure 2, in another embodiment, first circulation valve group 7 is triple valve, and first circulation valve group 7 connects air inlet pipe
Road 13 and warm-up cycle pipeline 10, control air-flow flow to desorption chamber air inlet 11 or warm-up cycle from catalytic combustor gas outlet 24
Pipeline 10.When pre- Warm status, the valve for flowing to admission line 13 is closed, and the valve for flowing to warm-up cycle pipeline 10 is opened, heat
Gas enters warm-up cycle pipeline 10 from catalytic combustor gas outlet 24.When detachment status, the valve of warm-up cycle pipeline 10 is flowed to
Door is closed, and the valve for flowing to admission line 13 is opened, and hot gas enters desorption chamber 1 by admission line 13.
With reference to figure 1, in a preferred embodiment, the first end of warm-up cycle pipeline 10 passes through outlet pipe 14 and main air blower 3
Inlet end connection, and between outlet valve group 16 and the inlet end of main air blower 3.In other embodiments, warm-up cycle pipe
The first end in road 10 can also be directly with main air blower 3 inlet end connect.
With reference to figure 1, Fig. 3 and Fig. 4, in a preferred embodiment, the offline regenerating active carbon purifier of the integral type also includes
First mends air-cooler 4, and first, which mends air-cooler 4, connects admission line 13, and positioned at the second end of warm-up cycle pipeline 10 and desorption
Between room air inlet 11.When the temperature in desorption chamber 1 is too high, the first benefit air-cooler 4 can be started, cold air is blasted into desorption
In room 1, cool for desorption chamber 1.In a further preferred embodiment, it is provided between the first benefit air-cooler 4 and admission line 13
First mends low temperature valve group 41, and the first benefit low temperature valve group 41 can open or close the first benefit air-cooler 4 to the passage of admission line 13, or
The benefit cold blast rate of air-cooler 4 is mended in person's regulation first, that is, controls first to mend the flow that air-cooler 4 mends cold air.
In another preferred embodiment, the offline regenerating active carbon purifier of the integral type also includes the second benefit air-cooler 5,
Second, which mends air-cooler 5, connects outlet pipe 14, and between outlet valve group 16 and the inlet end of main air blower 3.When catalysis is burnt
When temperature in room 2 is too high, the second benefit air-cooler 5 and main air blower 3 can be started, cold air is blasted in catalytic combustor 2, is
Catalytic combustor 2 cools.In addition, when the air in catalytic combustor 2 is in burning, the second benefit air-cooler 5 can also be opened, and be
Catalytic combustor 2 supplements more oxygen, the organic principle in air is burnt more abundant.
With reference to figure 1 and Fig. 3, in the present embodiment, the offline regenerating active carbon purifier of the integral type is simultaneously including first
Mend air-cooler 4 and second and mend air-cooler 5, first mends the set-up mode and above-described embodiment phase that air-cooler 4 and second mends air-cooler 5
Together.The second benefit low temperature valve group 51 is additionally provided between second benefit air-cooler 5 and outlet pipe 14, the second benefit low temperature valve group 51 can be opened
Or close second and mend air-cooler 5 to the passage of outlet pipe 14, or the benefit cold blast rate of the benefit air-cooler 5 of regulation second.It is cold mending
During state, the second benefit low temperature valve group 51 and outlet valve group 16 are opened, and first circulation valve group 7 is closed, and main air blower 3, first mends air-cooler 4
Run with the second benefit air-cooler 5, now cold air mends air-cooler 5 from the first benefit air-cooler 4 and second and blasts desorption chamber 1 respectively
In catalytic combustor 2, it is cooled.In this condition, exhaust valve group 61 can be opened and can also closed, if exhaust
Valve group 61 is opened, the air discharging directly into atmosphere that catalytic combustor 2 is discharged.If exhaust valve group 61 is closed, catalytic combustor 2 is discharged
Cold air entered by admission line 13 in desorption chamber 1, the cooling rate of desorption chamber 1 can be accelerated.In pre- Warm status,
Second benefit low temperature valve group 51, outlet valve group 16 and exhaust valve group 61 are closed, and first circulation valve group 7 is opened, and main air blower 3 is run, and first
It is out of service to mend the benefit air-cooler 5 of air-cooler 4 and second.
Fig. 3 to Fig. 6 is refer to, in a preferred embodiment, the offline regenerating active carbon purifier of the integral type also includes one
Body paralell 117, desorption chamber 1, catalytic combustor 2, main air blower 3 are mounted on integral paralell 117.Specifically, one
Paralell 117 can be the carrying platform for being used to carry the equipment such as desorption chamber 1, catalytic combustor 2 being made up of flat board.Entering one
In the preferred embodiment of step, housing 112 is provided with integral paralell 117, workplace 211, desorption chamber 1 are provided with housing 112
It is arranged in housing 112, and is separated by dividing plate 111 and workplace 211.The heat-insulated material such as asbestos can be provided with dividing plate 111
Material, the heat losses of desorption chamber 1 are on the one hand prevented, when on the other hand preventing that staff from entering workplace 211, accidentally quilt
Dividing plate 111 is scalded.Catalytic combustor 2, main air blower 3, outlet pipe 14, discharge duct 6, outlet valve group 16 and exhaust valve group 61 are equal
It is arranged in workplace 211, admission line 13 is located at the top of catalytic combustor 2 and desorption chamber 1.The top of desorption chamber 1 and shell
There is certain space, for installing one end of admission line 13, the other end of admission line 13 is then located at workplace between body 112
In 211.Controller (not shown) can also be arranged in workplace 211, and specifically controller can be electric cabinet.Entering one
In the preferred embodiment of step, desorption chamber 1 is provided with the first door body 118, and workplace is provided with the second door body 119.First door body 118
For opening or closing desorption chamber 1, in order to place activated carbon or take out activated carbon.Second door body 119 is used to play on or off
Close workplace so that operator can be overhauled or controlled outlet valve group 16 and exhaust valve group 61 etc. into workplace.
With reference to figure 1, Fig. 3 and Fig. 4, in a preferred embodiment, catalytic combustor 2 has heating chamber 22 and combustion chamber 21, combustion
The top that chamber 21 is arranged at heating chamber 22 is burnt, heater 222 is arranged in heating chamber 22, and catalysis burning bed 221 is arranged at combustion
Burn chamber 21.Specifically, it is catalyzed burning bed 221 and catalytic combustor 2 is divided into heating chamber 22 and combustion chamber 21, is catalyzed burning bed
221 are located at the bottom of combustion chamber 21.Catalytic combustor 2 is additionally provided with heat exchanger tube 26 and air guide channel 25, one end of heat exchanger tube 26
Connected with catalytic combustor air inlet 23, the other end connects one end of air guide channel 25, and heat exchanger tube 26 passes through combustion chamber 21, air guide
Passage 25 is arranged in the side wall of catalytic combustor 2, and the other end of air guide channel 25 connects with heating chamber 22.Specifically, urge
A heat exchanger tube 26 can be provided with by changing combustion chamber 2, it can also be provided that multiple parallel heat exchanger tubes 26.When being provided with multiple change
During heat pipe 26, multiple heat exchanger tubes 26 can be arranged at intervals.The air containing organic principle after desorption is from catalytic combustor air inlet
Mouth 23 enters catalytic combustor 2, successively by heat exchanger tube 26, air guide channel 25, heating chamber 22, catalysis burning bed 221, finally exists
Combustion chamber 21 burns, and the hot-air after burning flows through from the outer surface of heat exchanger tube 26, finally flows to catalytic combustor gas outlet 24.
When hot-air after burning flows through from the outer surface of heat exchanger tube 26, heat exchange is carried out with heat exchanger tube 26, is made relative in heat exchanger tube 26
The relatively low atmosphere temperature rising of temperature, so as to which when these air enter heating chamber 22 by air guide channel 25, heater 222 can
With relatively low power these air can be made to reach required temperature, thus make the offline regenerating active carbon purification of integral type
Device more saves.
Fig. 8 is refer to, in another preferred embodiment, catalytic combustor 2 is additionally provided with heat exchanger tube 26 and air guide channel 25.
Air guide channel 25 includes interconnection 251 and vertical passage 252, and interconnection 251 is arranged in combustion chamber 21, interconnection
251 first end connects with catalytic combustor air inlet 23, the second end of interconnection 251 and the first end of vertical passage 252
Connection, the second end of vertical passage 252 connects with heating chamber 22.Heat exchanger tube 26 is arranged in interconnection 251, and along longitudinal side
To through interconnection 251.One end of heat exchanger tube 26 is towards catalysis burning bed 221, and the other end is towards catalytic combustor gas outlet
24.Specifically, multiple heat exchanger tubes 26 can be arranged at intervals in interconnection 251.It should be noted that signified transverse direction herein
And longitudinal direction, might not just it be horizontally oriented and vertical direction, it is possibility to have certain inclination, it might even be possible to have certain curved
It is bent.The air containing organic principle after desorption enters catalytic combustor 2 from catalytic combustor air inlet 23, successively by laterally
Passage 251, vertical passage 252, heating chamber 22, catalysis burning bed 221, finally burn in combustion chamber 21, the hot-air after burning
Through heat exchanger tube 26, catalytic combustor gas outlet 24 is flowed to.Heated because the hot-air after burning can exchange heat pipe 26, behind from
The leaked-in air of interconnection 251, when flowing through the outer surface of heat exchanger tube 26, carry out heat exchange with heat exchanger tube 26 and heat up, so as to
When these air enter heating chamber 22 by vertical passage 252, heater 222 can be with relatively low power
These air is reached required temperature, regenerating active carbon purifier is more saved.
In a further preferred embodiment, air guide channel 25 has flaring opening with one end that heating chamber 22 connects, i.e.,
Nearer from heating chamber 22, the opening size of air guide channel 25 is bigger.This structure can enable the air in air guide channel 25
Quickly it is distributed in heating chamber 22, heating effect is more preferable.In another preferred embodiment, catalytic combustor air inlet 23 is set
In another side wall relative with the place side wall of air guide channel 25, heat exchanger tube 26 can be connected to two of catalytic combustor 1 relatively
In the side wall of setting, it can so make the simple shape of heat exchanger tube 26, be easily worked.Certainly, catalytic combustor air inlet 23 is set
At the top of catalytic combustor 2.
Fig. 5 and Fig. 6 are refer to, in a preferred embodiment, the electro-heat equipment 222 is electric heating tube, and the electric heating tube includes S
Type body 2221 and the spiral heat dissipation piece being arranged on the S bend pipe body 2221, spiral heat dissipation piece is by multiple interconnection one
Spiral element 2222 forms.When air flows through electro-heat equipment 222, more fully heat exchange can be carried out with spiral heat dissipation piece, from
And the heat for being advantageous to send S bend pipe body 2221 faster, more uniformly distributes.The both ends of electric heating tube can be provided with
The electrical joint 2223 being connected with S bend pipe body 2221, for being connected with circuit.In a further preferred embodiment, spiral list
Multiple equally distributed projections 2224 are also formed with member 2222, the one side of projection 2224 can strengthen the machine of spiral element 2222
Tool intensity, it on the other hand can play flow-disturbing effect so that air can carry out more fully heat exchange with spiral element 2222.
In another preferred embodiment, the electric heating tube includes the S bend pipe body 2221 of two or more concatenations.
With reference to figure 1, Fig. 3 and Fig. 4, in a preferred embodiment, the offline regenerating active carbon purifier of the integral type also includes
Controller (not shown), main air blower 3, heater 222 and first circulation valve group 7 are electrically connected with the controller；Controller is in main wind
After machine 3 and first circulation valve group 7 open preset time, stop in advance after closing first circulation valve group 7, namely preheating preset time
Heat；Or
The 5th temperature sensor (not shown), the 5th temperature sensor and controller electricity are additionally provided with catalytic combustor 2
Connection, after the temperature value that the 5th temperature sensor detects is more than or equal to preset temperature value, controller closes first circulation valve
Group 7.The temperature value that 5th temperature sensor detects can be air temperature value or catalysis in catalytic combustor 2
The temperature of catalyst on burning bed 221.Judged by the temperature of the 5th temperature sensor in catalytic combustor 2, controller is controllable
The folding of first circulation valve group 7 processed, it is to be in pre- Warm status or detachment status so as to control whole active carbon regenerating unit.
In further preferred embodiments, the first benefit low temperature valve group 41 and the second benefit low temperature valve group 51 are electrically connected with the controller, so as to control benefit cold
The flow of gas.
Referring to figs. 1 to Fig. 4, in a preferred embodiment, the offline regenerating active carbon purifier of the integral type also includes water source
9th, spray head 92 and water pump 91, spray head 92 are arranged in desorption chamber 1 and are connected with water source 9, and water pump is connected to the He of spray head 92
Between water source 9, for by water from the pump of water source 9 to spray head 92.Specifically, the top of desorption chamber 1 is provided with multiple spray heads
92, water source 9 can be provided in the water tank after desorption chamber 1.Water tank is also disposed on integral paralell 117.Further preferred
In embodiment, the offline regenerating active carbon purifier of the integral type also includes the controller electrically connected with water pump 91；Desorption chamber is entered
Three-temperature sensor 113 is provided with air port 11, the 4th temperature sensor 114 is provided with desorption chamber air outlet 12；3rd temperature
The temperature sensor 114 of sensor 113 and the 4th is spent to be electrically connected with controller.When the temperature that the 4th temperature sensor 114 is measured
When angle value is higher by the temperature value that three-temperature sensor 113 is measured, illustrate that the activated carbon in desorption chamber 1 may burn, control
Device control water pump 91 processed is opened to be sprayed to desorption chamber 1, reduces potential safety hazard.In a further preferred embodiment, this one
The offline regenerating active carbon purifier of body formula also includes the alarm (not shown) being connected with controller, when the 4th temperature sensor
When 114 temperature values measured are higher by the temperature value that three-temperature sensor 113 is measured, controller control alarm sends alarm signal
Number, to remind the activated carbon in operator's desorption chamber 1 that burning may occur.
With reference to figure 1, Fig. 3 and Fig. 4, in a preferred embodiment, the offline regenerating active carbon purifier of the integral type also includes
Air inlet spark arrester 231 and gas outlet spark arrester 241, air inlet spark arrester 231 are located at catalytic combustor air inlet 23 and main wind
Between the outlet side of machine 3；Gas outlet spark arrester 241 is located at catalytic combustor gas outlet 24 and the second end of warm-up cycle pipeline 10
Between.The setting of two spark arresters, the risk that flame enters desorption chamber 1 can be reduced, make the offline regenerating active carbon of integral type net
Makeup is put safer.
Fig. 3, Fig. 4 and Fig. 7 are refer to, the offline regenerating active carbon purifier of the integral type also includes transporter 400, turns
The desorption chamber 1 that shipping unit 400 is used to the activated carbon of outside being transported to the offline regenerating active carbon purifier of integral type is taken off
Attached regeneration purification.Transporter 400 is preferably transfer car(buggy), may be provided for placing activated carbon on transporter 400
Activated carbon frame.In a further preferred embodiment, the offline regenerating active carbon purifier of the integral type also includes and transfer car(buggy)
400 tracks 300 being engaged, one end connection desorption chamber 1 of track 300, the other end are used for the adsorption plant 200 for connecting outside,
Transfer car(buggy) is arranged on track 300, for the activated carbon of the adsorption plant 200 of outside to be transported into desorption chamber 1.By setting rail
Road 300 so that transfer car(buggy) is easier to move.Fig. 3 and Fig. 7 are refer to, in another further preferred embodiment, desorption chamber 1
Inside it is provided with the retaining rail 101 being engaged with transfer car(buggy), before desorption, transfer car(buggy) directly pushes away together with the activated carbon of its carrying
Enter in desorption chamber 1, and be fixed on the positioning by retaining rail 101.Then the first door body 118 of desorption chamber 1 is shut, makes the one
The offline regenerating active carbon purifier of formula proceeds by desorption.Preferably, retaining rail 101 is engaged with track 300, retaining rail pair
Standard gauge road 300 connects one end of desorption chamber 1, so transfer car(buggy) can be allow directly to shift retaining rail 101 onto by track 300
On.
The embodiment of the present invention also provides a kind of offline regenerating active carbon cleaning system, and it includes adsorption plant 200 and above-mentioned
The offline regenerating active carbon purifier of integral type described in embodiment.Adsorption plant 200 and the offline regenerating active carbon of integral type are net
Interval pre-determined distance is put in makeup, and transporter 400 is active offline for the activated carbon in adsorption plant 200 to be transported into integral type
The desorption chamber 1 of charcoal regeneration purification apparatus.Adsorption plant 200 can be provided in the tail gas treatment device in factory, adsorption plant
Activated carbon is provided with 200, for the organic principle in adsorption plant tail gas.The offline regenerating active carbon purifier of integral type can
Be arranged on according to the actual conditions of factory from the position with a certain distance from adsorption plant 200, such as 4-6 rice, thus when integral type from
When line regenerating active carbon purifier carries out catalysis burning, the spark in catalytic combustor 2 will not enter the institute of adsorption plant 200
In the exhaust system of connection, so as to avoid the occurrence of fire even explosion accident.When the activated carbon in adsorption plant 200 reaches full
During with state, it is net the activated carbon in adsorption plant 200 can be transported to by the offline regenerating active carbon of integral type by transporter 400
Before makeup is put, activated carbon is put into desorption chamber 1, the offline regenerating active carbon purifier of integral type is opened, carries out regeneration purification,
Complete after regenerating purification, then the activated carbon in desorption chamber 1 be loaded into transporter 400, be transported to adsorption plant 200 again,
Reused.
Compared to online regenerating active carbon purifier, the offline regenerating active carbon of integral type provided in an embodiment of the present invention
Purifier and system, desorption and regeneration purification is carried out to activated carbon by the way of offline, therefore be catalyzed fire caused by burning
Flower will not be entered in the exhaust system that adsorption plant is connected, so as to avoid the occurrence of the generation of fire even explosion accident,
It is safer.
The preferred embodiments of the present invention are the foregoing is only, are not intended to limit the scope of the invention, every utilization
The equivalent structure or equivalent flow conversion that description of the invention and accompanying drawing content are made, or directly or indirectly it is used in other correlations
Technical field, be included within the scope of the present invention.
Claims (22)
1. a kind of offline regenerating active carbon purifier of integral type, it is characterised in that including integral paralell, desorption chamber, catalysis
Combustion chamber, main air blower, admission line, outlet pipe and controller；The desorption chamber, catalytic combustor, main air blower are mounted on
On the integral paralell；The desorption chamber is provided with desorption chamber air inlet and desorption chamber gas outlet, and the catalytic combustor is set
It is equipped with catalytic combustor air inlet, catalytic combustor gas outlet；One end of the admission line connects the catalytic combustor and gone out
Gas port, the other end connect the desorption chamber air inlet；One end of the outlet pipe connects the desorption chamber gas outlet, the other end
The inlet end of the main air blower is connected, the outlet side of the main air blower connects the catalytic combustor air inlet；The catalysis combustion
Burn and heater and catalysis burning bed are provided with room, the heater and catalysis burning bed are arranged at the catalytic combustor
Between air inlet and catalytic combustor gas outlet.
2. the offline regenerating active carbon purifier of integral type as claimed in claim 1, it is characterised in that set on the admission line
Air inlet valve group is equipped with, outlet valve group is provided with the outlet pipe, the catalytic combustor gas outlet is provided with discharge duct,
Exhaust valve group is provided with the discharge duct, combustion supervision module is additionally provided with the catalytic combustor；The controller
Electrically connected with the combustion supervision module and exhaust valve group, for according to the control of the testing result of the combustion supervision module
It is vented opening and the closing of valve group.
3. the offline regenerating active carbon purifier of activated carbon integral type as claimed in claim 2, it is characterised in that the burning
Detection module includes the first temperature sensor and second temperature sensor, and first temperature sensor is adjacent to the heating dress
Put, second temperature sensor is more than described first adjacent to the catalysis burning bed, the temperature of the second temperature sensor detection
During the temperature of temperature sensor detection, the controller opens the exhaust valve group.
4. the offline regenerating active carbon purifier of integral type as claimed in claim 1, it is characterised in that also include and be arranged at
Water tank on the integral paralell, it is arranged at the spray head being connected in the desorption chamber and with the water tank and is connected to the spray
The water pump drenched between head and the water tank.
5. the offline regenerating active carbon purifier of integral type as claimed in claim 4, it is characterised in that the water pump with it is described
Controller is electrically connected with；The three-temperature sensor being electrically connected with the controller is provided with the desorption chamber air inlet,
The 4th temperature sensor being electrically connected with the controller is provided with the desorption chamber gas outlet；When the 4th TEMP
When the temperature value that device is measured is higher by the temperature value that three-temperature sensor is measured, the controller control water pump is opened to described de-
Alcove is sprayed.
6. the offline regenerating active carbon purifier of integral type as claimed in claim 5, it is characterised in that also include and the control
The connected alarm of device processed, when the temperature value that the 4th temperature sensor is measured is higher by the temperature that three-temperature sensor measures
During value, the controller control alarm sends alarm signal.
7. the offline regenerating active carbon purifier of integral type as claimed in claim 1, it is characterised in that the desorption chamber air inlet
Mouth is arranged at the top of the desorption chamber, and the desorption chamber gas outlet is arranged at the bottom of the desorption chamber, and the desorption chamber is entered
Gas port is diagonally set with desorption chamber gas outlet in the desorption chamber.
8. the offline regenerating active carbon purifier of integral type as claimed in claim 1, it is characterised in that the electro-heat equipment is
Electric heating tube, the electric heating tube includes S bend pipe body and the spiral heat dissipation piece being arranged on the S bend pipe body, the spiral dissipate
Backing is made up of multiple spiral elements being integrated that are connected with each other.
9. the offline regenerating active carbon purifier of integral type as claimed in claim 8, it is characterised in that on the spiral element
It is also formed with multiple equally distributed projections.
10. the offline regenerating active carbon purifier of integral type as claimed in claim 8, it is characterised in that the electric heating tube
Include the S bend pipe body of two or more concatenations.
11. the offline regenerating active carbon purifier of integral type as claimed in claim 1, it is characterised in that also followed including preheating
Endless tube road, the first end of the warm-up cycle pipeline connect with the inlet end of the main air blower, and the of the warm-up cycle pipeline
Two ends are connected with the catalytic combustor, and air is formed between the catalytic combustor and the warm-up cycle pipeline, main air blower
Circulation canal, the air circulation duct is through the heater and is catalyzed burning bed, is also set on the warm-up cycle pipeline
It is equipped with first circulation valve group.
12. the offline regenerating active carbon purifier of integral type as claimed in claim 11, it is characterised in that the outlet pipe
On be provided with outlet valve group, the second end of the warm-up cycle pipeline connects the admission line, is set on the admission line
There is second circulation valve group, the second end of the warm-up cycle pipeline is located at the second circulation valve group and gone out with the catalytic combustor
Between gas port, the first end of the warm-up cycle pipeline is connected by the outlet pipe with the inlet end of the main air blower, and
Between the outlet valve group and the inlet end of the main air blower, in pre- Warm status, the first circulation valve group is opened, described
Second circulation valve group and outlet valve group are closed；In detachment status, the second circulation valve group and outlet valve group are opened, and described first
Circulation valve is closed.
13. the offline regenerating active carbon purifier of integral type as claimed in claim 1, it is characterised in that also mended including first
Air-cooler, described first, which mends air-cooler, connects the admission line；And/or
Also include second and mend air-cooler, described second, which mends air-cooler, connects the outlet pipe, and is located at the desorption chamber outlet
Between mouth and the inlet end of the main air blower.
14. the offline regenerating active carbon purifier of integral type as claimed in claim 13, it is characterised in that first benefit is cold
Blower fan and second benefit air-cooler electrically connect with the controller, in benefit cold state when, the main air blower, first benefit air-cooler and
Second benefit air-cooler is run.
15. the offline regenerating active carbon purifier of integral type as claimed in claim 1, it is characterised in that the integral platform
Housing is provided with frame, is provided with workplace in the housing, the desorption chamber is arranged in the housing, and passes through dividing plate and institute
State workplace to separate, the catalytic combustor, main air blower and outlet pipe may be contained within the workplace, the admission line
Positioned at the catalytic combustor and the top of desorption chamber.
16. the offline regenerating active carbon purifier of integral type as claimed in claim 15, it is characterised in that the desorption chamber is set
The first door body is equipped with, the workplace is provided with the second door body.
17. the offline regenerating active carbon purifier of integral type as described in any one of claim 1 to 16, it is characterised in that also
Including transporter, the transporter is used to the activated carbon of outside being transported to the offline regenerating active carbon purification of the integral type
The desorption chamber of device.
18. the offline regenerating active carbon purifier of integral type as claimed in claim 17, it is characterised in that the transporter
For transfer car(buggy).
19. the offline regenerating active carbon purifier of integral type as claimed in claim 18, it is characterised in that also include with it is described
The track that transfer car(buggy) is engaged, one end connection desorption chamber of the track, the outside adsorption plant of other end connection, described turn
Fortune car is arranged on the track.
20. the offline regenerating active carbon purifier of integral type as claimed in claim 19, it is characterised in that in the desorption chamber
The retaining rail being engaged with the transfer car(buggy) is provided with, the retaining rail is engaged with the track, and the retaining rail is directed at institute
State one end of track connection desorption chamber.
21. the offline regenerating active carbon purifier of integral type as claimed in claim 18, it is characterised in that in the desorption chamber
It is provided with the retaining rail being engaged with the transfer car(buggy).
22. a kind of offline regenerating active carbon cleaning system, it is characterised in that including appointing in adsorption plant and claim 17-21
The offline regenerating active carbon purifier of integral type described in meaning one, the adsorption plant and the offline activated carbon of the integral type are again
Raw purifier interval pre-determined distance, the transporter are used to the activated carbon in the adsorption plant being transported to the one
The desorption chamber of the offline regenerating active carbon purifier of formula.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201710842957.4A CN107670655A (en) | 2017-09-18 | 2017-09-18 | The offline regenerating active carbon purifier of integral type and offline regenerating active carbon cleaning system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201710842957.4A CN107670655A (en) | 2017-09-18 | 2017-09-18 | The offline regenerating active carbon purifier of integral type and offline regenerating active carbon cleaning system |
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| CN201710842957.4A Pending CN107670655A (en) | 2017-09-18 | 2017-09-18 | The offline regenerating active carbon purifier of integral type and offline regenerating active carbon cleaning system |
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| CN108554118A (en) * | 2018-04-16 | 2018-09-21 | 李庆彪 | Bicyclic return-air road Adsorption Concentration thermal desorption catalytic combustion system |
| CN109432893A (en) * | 2018-12-27 | 2019-03-08 | 机械工业第六设计研究院有限公司 | Separate type spray painting organic exhaust gas VOCs modularization controlling device |
| CN110206617A (en) * | 2019-04-26 | 2019-09-06 | 北京理工大学 | A kind of fixed type particle trap regeneration system |
| CN112619625A (en) * | 2020-11-25 | 2021-04-09 | 中国辐射防护研究院 | Re-impregnation method and device for radioactive iodine adsorption module adsorption material |
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| CN107597083A (en) * | 2017-09-18 | 2018-01-19 | 广州市耀南环保科技有限公司 | Regenerating active carbon purifier and system |
| CN108554118A (en) * | 2018-04-16 | 2018-09-21 | 李庆彪 | Bicyclic return-air road Adsorption Concentration thermal desorption catalytic combustion system |
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| CN112619625A (en) * | 2020-11-25 | 2021-04-09 | 中国辐射防护研究院 | Re-impregnation method and device for radioactive iodine adsorption module adsorption material |
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