CN209605181U - RCO organic exhaust gas adsorption desorption catalyzing burning all-in-one machine - Google Patents
RCO organic exhaust gas adsorption desorption catalyzing burning all-in-one machine Download PDFInfo
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- CN209605181U CN209605181U CN201821824485.6U CN201821824485U CN209605181U CN 209605181 U CN209605181 U CN 209605181U CN 201821824485 U CN201821824485 U CN 201821824485U CN 209605181 U CN209605181 U CN 209605181U
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- exhaust gas
- spray column
- activated carbon
- rco
- column ontology
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- 238000002336 sorption--desorption measurement Methods 0.000 title claims abstract description 19
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 99
- 239000007921 spray Substances 0.000 claims abstract description 64
- 238000001179 sorption measurement Methods 0.000 claims abstract description 51
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 22
- 238000003795 desorption Methods 0.000 claims abstract description 20
- 238000012856 packing Methods 0.000 claims abstract description 19
- 238000002485 combustion reaction Methods 0.000 claims abstract description 18
- 239000003973 paint Substances 0.000 claims abstract description 18
- 239000002245 particle Substances 0.000 claims abstract description 16
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 15
- 125000004122 cyclic group Chemical group 0.000 claims abstract description 10
- 238000007689 inspection Methods 0.000 claims description 20
- 239000000945 filler Substances 0.000 claims description 15
- 239000010865 sewage Substances 0.000 claims description 10
- 238000002386 leaching Methods 0.000 claims description 5
- 241001466460 Alveolata Species 0.000 claims description 4
- 239000003610 charcoal Substances 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- 239000003463 adsorbent Substances 0.000 claims description 3
- 239000003960 organic solvent Substances 0.000 abstract description 15
- 238000000034 method Methods 0.000 abstract description 10
- 230000008569 process Effects 0.000 abstract description 8
- 238000007084 catalytic combustion reaction Methods 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 32
- 238000006555 catalytic reaction Methods 0.000 description 11
- 230000003647 oxidation Effects 0.000 description 6
- 238000007254 oxidation reaction Methods 0.000 description 6
- 238000012545 processing Methods 0.000 description 6
- 238000001816 cooling Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 230000003197 catalytic effect Effects 0.000 description 4
- 238000005485 electric heating Methods 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 230000009471 action Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000006210 lotion Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000007592 spray painting technique Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
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- Treating Waste Gases (AREA)
Abstract
The utility model discloses RCO organic exhaust gas adsorption desorption catalyzing burning all-in-one machines, belong to RCO catalytic combustion device field, RCO organic exhaust gas adsorption desorption catalyzing burning all-in-one machine, including spray column ontology, combustion chamber and three activated carbon adsorption beds, activated carbon adsorption layer is connected in activated carbon adsorption bed, desorption electric heater is connected in combustion chamber, the side of spray column ontology is connected with exhaust gas inlet, air intake blower fan is connected in exhaust gas inlet, the inside of spray column ontology is fixedly connected sequentially has spiral board and packing layer from top to bottom, the side of spray column ontology is equipped with cyclic water tank, high-pressure hydraulic pump is connected in cyclic water tank, the water outlet of high-pressure hydraulic pump is connected with water-supply-pipe, it may be implemented to pre-process the organic solvent in exhaust gas by spray column and spiral board, adsorption/desorption catalyzing burning is carried out again, it can be improved pair The adsorption rate of paint particle in exhaust gas, extends the service life of active carbon.
Description
Technical field
The utility model relates to RCO catalytic combustion device fields, are desorbed more specifically to RCO organic exhaust gas adsorption
Catalysis burning all-in-one machine.
Background technique
RCO cleaning principle is, in industrial processes, the organic tail gas of discharge enters the rotation of equipment by air-introduced machine
Valve, by selecting rotary valve that inlet gas and exit gas is completely separable, it is pre- that gas fills foot (bottom) by ceramic material first
Then deposit and the heat exchange of heat occurs, temperature nearly reaches Catalytic Layer (middle category) and carries out temperature set by catalysis oxidation
It spends, at this moment part of pollutant oxygenolysis, exhaust gas continues through heating zone, and (Electric heating or natural can be used in upper layer
Gas heating method) heating, and set temperature is maintained, it enters back into Catalytic Layer and completes catalytic oxidation, is i.e. reaction generates CO2
And H20, and a large amount of heat is discharged, to reach expected treatment effect.Gas after catalysis oxidation enters other ceramics
Filled layer is discharged into big machine after recycling heat by rotary valve, and purification final vacuum temperature is only slightly higher than the temperature before exhaust-gas treatment
Degree, system continuously run, automatically switch.It is worked by rotary valve, all ceramic filler layers complete heating, cooling, purification
Circulation step, heat recycled.
Existing RCO catalytic adsorption desorption catalyzing combustion apparatus is commonly used in industries such as furniture, in spray painting, has very much
Organic solvent evaporates, it is therefore desirable to which absorbing organic solvent, so that environment protection standard, this equipment is inhaled using active carbon
Attached, existing equipment is not by pretreatment, and paint can block active carbon, so that adsorption substantially reduces, thus every one section
Time just needs replacing active carbon, and cost is very high, and can only at most adsorb 70% organic solvent.
Utility model content
1. technical problems to be solved
Aiming at the problems existing in the prior art, the purpose of this utility model is to provide RCO organic exhaust gas adsorption desorptions
Catalysis burning all-in-one machine, it may be implemented to pre-process the organic solvent in exhaust gas by spray column and spiral board, then
Adsorption/desorption catalyzing burning is carried out, the adsorption rate to organic solvent in exhaust gas can be improved, extend the service life of active carbon.
2. technical solution
To solve the above problems, the utility model adopts the following technical scheme.
RCO organic exhaust gas adsorption desorption catalyzing burning all-in-one machine, including spray column ontology, combustion chamber and three active carbons are inhaled
Attached bed is connected with activated carbon adsorption layer in the activated carbon adsorption bed, desorption electric heater is connected in the combustion chamber, described
The side of spray column ontology is connected with exhaust gas inlet, and air intake blower fan is connected in the exhaust gas inlet, the spray column ontology
Inside is fixedly connected sequentially has spiral board and packing layer from top to bottom, and the side of the spray column ontology is equipped with cyclic water tank, institute
It states and is connected with high-pressure hydraulic pump in cyclic water tank, the water outlet of the high-pressure hydraulic pump is connected with water-supply-pipe, one end of the water-supply-pipe
Through spray column ontology side wall and between packing layer and spiral board, the lower end of the water-supply-pipe be connected with it is multiple uniformly point
The spray head of cloth, and spray head is located at the inside of spray column ontology, between the spray column ontology and three activated carbon adsorption beds
Equipped with dry filter, the first communicating pipe, the dry filter are connected between the spray column ontology and dry filter
It was connected with for the second communicating pipe between three activated carbon adsorption beds, between the lower end and combustion chamber of three activated carbon adsorption beds
It is connected with third connecting pipe, was connected with for the 4th communicating pipe between the upper end and combustion chamber of three activated carbon adsorption beds, it is described
It is connected with desorption blower on 4th communicating pipe, is respectively connected with exhaust pipe on the air outlet of three activated carbon adsorption beds, it can
The organic solvent in exhaust gas is pre-processed by spray column and spiral board with realizing, then carries out adsorption/desorption catalyzing combustion
It burns, the adsorption rate to organic solvent in exhaust gas can be improved, extend the service life of active carbon.
Further, digging on the side wall of the spray column ontology has a pair of of inspection socket, and a pair of inspection socket distinguishes position
In the two sides up and down of packing layer, it is connected with inspection cover on the inspection socket, it is intrinsic convenient for detecting spray column by inspection cover
Situation.
Further, the lower end of the spray column ontology, which is dug, sewage draining exit, convenient for discharge sewage in time, after processing may be used
It recycles.
Further, the active carbon in the activated carbon adsorption layer is Alveolate activated carbon, and contact area is bigger, absorption effect
Fruit is more preferable.
Further, the ventilative filler for absorption paint particle, the paint particle in air-flow can be removed, be kept away
Exempt from paint particle and emission-control equipment is damaged as air-flow enters in emission-control equipment, extends subsequent activity
The service life of charcoal adsorbent equipment.
Further, the inner surface of the spray column ontology is coated with oleophobic layer, and organic solvent is not easy to be adhered to spray column sheet
The inner surface of body.
3. beneficial effect
Compared with the prior art, utility model has the advantages that
(1) this programme may be implemented to pre-process the organic solvent in exhaust gas by spray column and spiral board, then
Adsorption/desorption catalyzing burning is carried out, the adsorption rate to paint particle in exhaust gas can be improved, extend the service life of active carbon, it is existing
The organic solvent of 60%-70% in exhaust gas generally can only be at most adsorbed in technology, adsorption efficiency can be increased to 85%- by this programme
95%.
(2) digging on the side wall of spray column ontology has a pair of of inspection socket, and a pair of of inspection socket is located at the upper and lower of packing layer
Two sides are connected with inspection cover on inspection socket, convenient for passing through the inspection cover detection intrinsic situation of spray column.
(3) lower end of spray column ontology, which is dug, sewage draining exit, convenient for discharge sewage in time, can be recycled after processing.
(4) active carbon in activated carbon adsorption layer is Alveolate activated carbon, and contact area is bigger, and adsorption effect is more preferable.
(5) packing layer is the ventilative filler for adsorbing paint particle, and material is the cotton that aperture is less than paint particle, paint
Grain by filler blocking and be attached on filler, spray equipment injection water mist filler last time formed water flow, these water flows
Paint particle on filler can be washed away, prevent paint particle accumulation excessive and the permeability of filler will be reduced.
(6) inner surface of spray column ontology is coated with oleophobic layer, and organic solvent is not easy to be adhered to the inner surface of spray column ontology.
Detailed description of the invention
Fig. 1 is the part-structure schematic diagram of the utility model；
Fig. 2 is the utility model adsoption catalysis burning process principle figure.
Figure label explanation:
1 spray column ontology, 2 cyclic water tanks, 3 high-pressure hydraulic pumps, 4 water-supply-pipes, 5 spray heads, 6 packing layers, 7 spiral boards, 8 inspections
Look into lid, 9 exhaust gas inlets, 10 air intake blower fans, 11 activated carbon adsorption beds, 12 first communicating pipes, 13 desorption electric heaters, 14 burnings
Room, 15 third connecting pipes, 16 the 4th communicating pipes, 17 desorption blowers, 18 exhaust pipes, 19 activated carbon adsorption layers, 20 sewage draining exits, 21
Dry filter, 22 second communicating pipes.
Specific embodiment
The following is a combination of the drawings in the embodiments of the present utility model；The technical scheme in the embodiment of the utility model is carried out
Clearly and completely describe；Obviously, the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment, based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
In the description of the present invention, it should be noted that term " on ", "lower", "inner", "outside", " top/bottom end " etc.
The orientation or positional relationship of instruction is to be based on the orientation or positional relationship shown in the drawings, and is merely for convenience of description the utility model
It is described with simplifying, rather than the device or element of indication or suggestion meaning must have a particular orientation, with specific orientation structure
It makes and operates, therefore should not be understood as limiting the present invention.In addition, term " first ", " second " are only used for description mesh
, it is not understood to indicate or imply relative importance.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " is pacified
Dress ", " being provided with ", " be arranged/connect ", " connection " etc., shall be understood in a broad sense, such as " connection ", may be a fixed connection, can also be with
It is to be detachably connected, or be integrally connected；It can be mechanical connection, be also possible to be electrically connected；It can be directly connected, it can also be with
Indirectly connected through an intermediary, it can be the connection inside two elements.For the ordinary skill in the art, may be used
The concrete meaning of above-mentioned term in the present invention is understood with concrete condition.
Embodiment 1:
The all-in-one machine referring to Fig. 1, RCO organic exhaust gas adsorption desorption catalyzing burns, including spray column ontology 1, combustion chamber 14
With three activated carbon adsorption beds 11, activated carbon adsorption layer 19 is connected in activated carbon adsorption bed 11, is connected in combustion chamber 14 de-
Attached electric heater 13, the side of spray column ontology 1 are connected with exhaust gas inlet 9, and air intake blower fan 10 is connected in exhaust gas inlet 9, spray
The inside of leaching tower ontology 1 is fixedly connected sequentially has spiral board 7 and packing layer 6 from top to bottom, and the side of spray column ontology 1, which is equipped with, to be followed
Ring water tank 2 is connected with high-pressure hydraulic pump 3 in cyclic water tank 2, and the water outlet of high-pressure hydraulic pump 3 is connected with water-supply-pipe 4, water-supply-pipe 4
One end runs through the side wall of spray column ontology 1 and between packing layer 6 and spiral board 7, and the lower end of water-supply-pipe 4 is connected with multiple
Equally distributed spray head 5, and spray head 5 is located at the inside of spray column ontology 1, spray column ontology 1 and three activated carbon adsorptions
It is equipped with dry filter 21 between bed 11, was connected with for the first communicating pipe 12 between spray column ontology 1 and dry filter 21, does
The second communicating pipe 22, the lower end of three activated carbon adsorption beds 11 are connected between formula filter 21 and three activated carbon adsorption beds 11
It is connected with third connecting pipe 15 between combustion chamber 14, is connected between the upper end and combustion chamber 14 of three activated carbon adsorption beds 11
There is the 4th communicating pipe 16, be connected on the 4th communicating pipe 16 and blower 17 is desorbed, on the air outlet of three activated carbon adsorption beds 11
It is connected with exhaust pipe 18, air intake blower fan 10, desorption blower 17, high-pressure hydraulic pump 3, desorption electric heater 13 and dry filter 21
Model be required to those skilled in the art and determine that it may be implemented to pass through spray according to the actual exhausted air quantity using required processing
Leaching tower and spiral board pre-process the organic solvent in exhaust gas, then carry out adsorption/desorption catalyzing burning, can be improved to useless
The adsorption rate of paint particle in gas, extends the service life of active carbon；The material of packing layer 6 is that aperture is less than paint particle
Cotton, paint particle by filler blocking and be attached on filler, spray equipment injection water mist filler last time formed water flow,
These water flows can wash away the paint particle on filler, prevent paint particle accumulation excessive and will reduce the gas permeability of filler
Can, the material of packing layer 6 can directly be purchased from 3M company to be obtained.
Digging on the side wall of spray column ontology 1 has a pair of of inspection socket, and a pair of of inspection socket is located at the upper and lower of packing layer 6
Two sides are connected with inspection cover 8 on inspection socket, convenient for detecting the situation in spray column ontology 1, spray column ontology by inspection cover 8
1 lower end, which is dug, sewage draining exit 20, convenient for discharge sewage in time, can be recycled after processing, in activated carbon adsorption layer 19
Active carbon is Alveolate activated carbon, and contact area is bigger, and adsorption effect is more preferable, and packing layer 6 is the ventilative of absorption paint particle
Filler, the inner surface of spray column ontology 1 are coated with oleophobic layer, and organic solvent is not easy to be adhered to the inner surface of spray column ontology 1.
In use, enough water lotions are put into cyclic water tank 2, under the action of high-pressure hydraulic pump 3, through 4 He of water-supply-pipe
The spray of spray head 5 is flowed down along the surface of packing layer 6 on packing layer 6, exhaust gas under the action of air intake blower fan 10 from exhaust gas into
Mouth 9 enters spray column ontology 1, and enters in dry filter 21 from the first communicating pipe 12, between, gas-liquid on packing layer 6
Two-phase close contact carries out mass transfer washing, and pretreated exhaust gas carries out gas-liquid separation, the waste liquid after washing when passing through spiral board 7
It is discharged by sewage draining exit 20, sewage draining exit 20 can be connect by reflux circuit with cyclic water tank 2, and waste liquid can be reused for spraying through processing
Leaching, recycles, and then gas enters dry filter 21 and is filtered, and enters activated carbon adsorption bed 11 later, by active carbon
Adsorption layer 19 adsorbs, and desorption electric heater 13 burns in combustion chamber 14, and hot wind is led to work under the action of blower 17 are desorbed
Property charcoal adsorbent bed 11, the organic solvent on activated carbon adsorption layer 19 is desorbed, then will be organic by third connecting pipe 15
Solvent brings combustion chamber 14 into and carries out burning processing, eventually by exhaust pipe 18 be discharged it is up to standard after air, three activated carbon adsorptions
Bed 11 is worked alternatively by rotary valve.
Referring to Fig. 2, the structure and principle of adsoption catalysis burning process include control content:
1, using Siemens S7 series PLC control system, electrical part uses Siemens, ABB or Schneider product, two touchings
Touching screen, one of them is used at the scene, another can remotely be used；
2,14 sets of pneumatic operated valves, 3 sets of solenoid valves, 1 set of motor-driven valve, 1 set of electric proportional-regulation valve are controlled；
3,16 temperature inputs (PT100), 2 pressure difference switch inputs, 1 differential pressure pickup input, a concentration input.
Control process:
1, three sets of activated carbon adsorption devices, wherein two sets of uses, wherein a set of spare.
2, when normal shutdown, all valves of system, blower and electric heater are closed.
3, every set activated carbon adsorption device includes following operation: adsorption and desorption, cooling, spare and fire-fighting totally 5 operations.
4, fire protection:
A, when any one of Tn1, Tn2 and Tn3 temperature reach setting value (150 degree) (n=1,2,3), into fire-fighting shape
State, sound-light alarm；
B, main air blower is closed；
C, air inlet valve F7 is closed, Fn5, Fn1, Fn2 is opened, closes remaining all valve；
C, when maximum value is less than 100 degree in Tn1, Tn2 and Tn3, Fn5 is closed；
D, artificial disposition resets；
E, fire protection be in shutdown also do not stop, wherein a set of active carbon start fire-fighting when, other stream oriented devices also otherwise
Stop carrying out fire protection.
5, when being switched on, air inlet valve F7 is opened, wherein any two activated-carbon device carries out adsorption operations process, another set of active carbon
Device is spare, opens main air blower, keeps differential pressure pickup P1 value constant at setting value (200Pa).
6, it when pressure difference switch P2 is closed, prompts replacement air intake filter and alarms and (do not shut down).
7, it when pressure difference switch P3 is closed, prompts more inletting fresh air filter and alarms and (do not shut down).
8, adsorption operations:
A, valve Fn1, Fn2 opens (n=1,2,3)；
B, when air draft concentration sensor C reaches setting value (25ppm), start spare a set of activated-carbon device and inhaled
Attached operation；
C, the longer a set of activated-carbon device of adsorption time enters desorption manipulation.
9, desorption manipulation:
A, valve Fn1, Fn2 is closed, and Fn3, Fn4, F4 are opened；
B, starting desorption blower 17；
C, starting catalysis electric heating (120Kw), control catalysis electric heating outlet temperature T7 are constant in set temperature (350
Degree)；
D, it when catalysis oxidation outlet temperature T8 reaches starting device value (200 degree) (and T7 is greater than the set value -5 degree), opens
Dynamic desorption electric heater 13, desorption 13 outlet temperature T5 of heater is constant at setting value (100 degree), and desorption starts timing；
F, when catalysis oxidation outlet temperature T8 is greater than running equipment value (450 degree) Shi Zengjia F6 aperture, is less than setting value
Reduce aperture until closing；
G, when desorption time reaches setting value (2 hours), it is transferred to cooling down operation.
10, cooling down operation:
A, desorption electric heater and catalysis oxidation electric heating are closed；
B, F5 is opened, F4, F6 are closed, it is cooling to start timing；
C, when cooled between when reaching setting value (40 minutes), close desorption blower, close valve F5, Fn3, Fn4；
D, into stand-by state.
11, it shuts down: closing two electric heaters, close two blowers, close all valves.
12, all input information and state need to store, convenient for checking and setting on two touch screens.
Meanwhile also needing to be equipped with liquid nitrogen extinguishment device, it can just keep the safety in production.
It is described above；The only preferable specific embodiment of the utility model；But the protection scope of the utility model is not
It is confined to this.Anyone skilled in the art is within the technical scope disclosed by the utility model, practical according to this
Novel technical solution and its improvement design is subject to equivalent substitution or change, should all cover in the protection scope of the utility model
It is interior.
Claims (6)
1.RCO organic exhaust gas adsorption desorption catalyzing burning all-in-one machine, including spray column ontology (1), combustion chamber (14) and three work
Property charcoal adsorbent bed (11), activated carbon adsorption layer (19) are connected in the activated carbon adsorption bed (11), in the combustion chamber (14)
It is connected with desorption electric heater (13), it is characterised in that: the side of the spray column ontology (1) is connected with exhaust gas inlet (9), institute
It states and is connected on exhaust gas inlet (9) air intake blower fan (10), the inside of the spray column ontology (1) is fixedly connected sequentially from top to bottom
There are spiral board (7) and packing layer (6), the side of the spray column ontology (1) is equipped with cyclic water tank (2), the cyclic water tank (2)
It being inside connected with high-pressure hydraulic pump (3), the water outlet of the high-pressure hydraulic pump (3) is connected with water-supply-pipe (4), and the one of the water-supply-pipe (4)
End runs through the side wall of spray column ontology (1) and between packing layer (6) and spiral board (7), and the lower end of the water-supply-pipe (4) connects
Multiple equally distributed spray heads (5) are connected to, and spray head (5) is located at the inside of spray column ontology (1), the spray column ontology
(1) dry filter (21), the spray column ontology (1) and dry filter are equipped between three activated carbon adsorption beds (11)
(21) it is connected between the first communicating pipe (12), is connected between the dry filter (21) and three activated carbon adsorption beds (11)
Have the second communicating pipe (22), is connected with third connecting between the lower end and combustion chamber (14) of three activated carbon adsorption beds (11)
It manages (15), is connected with the 4th communicating pipe (16), institute between the upper end and combustion chamber (14) of three activated carbon adsorption beds (11)
It states and is connected with desorption blower (17) on the 4th communicating pipe (16), be all connected on the air outlet of three activated carbon adsorption beds (11)
There are exhaust pipe (18).
The all-in-one machine 2. RCO organic exhaust gas adsorption desorption catalyzing according to claim 1 burns, it is characterised in that: the spray
It drenches to dig on the side wall of tower ontology (1) and has a pair of of inspection socket, a pair of inspection socket is located at up and down the two of packing layer (6)
Side is connected with inspection cover (8) on the inspection socket.
The all-in-one machine 3. RCO organic exhaust gas adsorption desorption catalyzing according to claim 1 burns, it is characterised in that: the spray
The lower end of leaching tower ontology (1), which is dug, sewage draining exit (20).
The all-in-one machine 4. RCO organic exhaust gas adsorption desorption catalyzing according to claim 1 burns, it is characterised in that: the work
Property charcoal adsorption layer (19) in active carbon be Alveolate activated carbon.
The all-in-one machine 5. RCO organic exhaust gas adsorption desorption catalyzing according to claim 1 burns, it is characterised in that: described to fill out
The bed of material (6) is the ventilative filler for adsorbing paint particle.
The all-in-one machine 6. RCO organic exhaust gas adsorption desorption catalyzing according to claim 1 burns, it is characterised in that: the spray
The inner surface of leaching tower ontology (1) is coated with oleophobic layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821824485.6U CN209605181U (en) | 2018-11-07 | 2018-11-07 | RCO organic exhaust gas adsorption desorption catalyzing burning all-in-one machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821824485.6U CN209605181U (en) | 2018-11-07 | 2018-11-07 | RCO organic exhaust gas adsorption desorption catalyzing burning all-in-one machine |
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| Publication Number | Publication Date |
|---|---|
| CN209605181U true CN209605181U (en) | 2019-11-08 |
Family
ID=68394178
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821824485.6U Expired - Fee Related CN209605181U (en) | 2018-11-07 | 2018-11-07 | RCO organic exhaust gas adsorption desorption catalyzing burning all-in-one machine |
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| Country | Link |
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| CN (1) | CN209605181U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111359406A (en) * | 2020-04-13 | 2020-07-03 | 山东欧亚化工有限公司 | Organic waste gas treatment device and treatment method |
| CN112354342A (en) * | 2020-07-17 | 2021-02-12 | 万向一二三股份公司 | Lithium ion battery electrolyte waste gas treatment device and system |
| CN112973376A (en) * | 2021-03-04 | 2021-06-18 | 重庆新允创环保技术研究院有限公司 | Combined environment-friendly processing device for industrial waste gas treatment |
| CN114797351A (en) * | 2022-04-02 | 2022-07-29 | 江苏爱尚环境科技有限公司 | Multi-bin type catalytic waste gas treatment device for waste gas treatment process |
-
2018
- 2018-11-07 CN CN201821824485.6U patent/CN209605181U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111359406A (en) * | 2020-04-13 | 2020-07-03 | 山东欧亚化工有限公司 | Organic waste gas treatment device and treatment method |
| CN112354342A (en) * | 2020-07-17 | 2021-02-12 | 万向一二三股份公司 | Lithium ion battery electrolyte waste gas treatment device and system |
| CN112973376A (en) * | 2021-03-04 | 2021-06-18 | 重庆新允创环保技术研究院有限公司 | Combined environment-friendly processing device for industrial waste gas treatment |
| CN114797351A (en) * | 2022-04-02 | 2022-07-29 | 江苏爱尚环境科技有限公司 | Multi-bin type catalytic waste gas treatment device for waste gas treatment process |
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Granted publication date: 20191108 |