CN209512044U - A kind of volatile organic compounds processing unit - Google Patents
A kind of volatile organic compounds processing unit Download PDFInfo
- Publication number
- CN209512044U CN209512044U CN201822077366.5U CN201822077366U CN209512044U CN 209512044 U CN209512044 U CN 209512044U CN 201822077366 U CN201822077366 U CN 201822077366U CN 209512044 U CN209512044 U CN 209512044U
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- venthole
- tank
- cushion chamber
- buffer tank
- heat
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- 239000012855 volatile organic compound Substances 0.000 title claims abstract description 63
- 238000005192 partition Methods 0.000 claims abstract description 11
- 230000003139 buffering effect Effects 0.000 claims description 18
- 238000006243 chemical reaction Methods 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 15
- 238000007789 sealing Methods 0.000 claims description 4
- 238000009423 ventilation Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 4
- 239000007789 gas Substances 0.000 description 52
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 32
- 239000003546 flue gas Substances 0.000 description 32
- 230000001172 regenerating effect Effects 0.000 description 24
- 238000002485 combustion reaction Methods 0.000 description 8
- 239000002912 waste gas Substances 0.000 description 8
- 238000005338 heat storage Methods 0.000 description 4
- 239000002918 waste heat Substances 0.000 description 4
- 238000009825 accumulation Methods 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000005299 abrasion Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000003513 alkali Substances 0.000 description 1
- 238000012824 chemical production Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000007592 spray painting technique Methods 0.000 description 1
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- Incineration Of Waste (AREA)
Abstract
The utility model discloses a kind of volatile organic compounds processing units, including triple channel flange end socket, slew buffer tank, gas converting heat tank and heat exchanger tube, wherein, the upper end of the slew buffer tank is set there are three the first venthole, partition is equipped in the slew buffer tank, the inner cavity of slew buffer tank is separated into three cushion chambers by partition, and three cushion chambers are communicated with three the first ventholes, and two of them cushion chamber is individually connected to by the second venthole；The lower end of the slew buffer tank is equipped with third venthole and the 4th venthole, this third venthole and the 4th venthole are communicated with two of them cushion chamber respectively；Three the first ventholes are equipped with valve.This, so as to solve the problems, such as more than pipeline and tediously long, also reduces the loss of heat and simplifies operation using the collective effect for cushion chamber, through-hole and the valve being arranged in slew buffer tank to replace traditional pipeline to be laid with.
Description
Technical field
The utility model relates to VOCs VOCs treatment technologies, and in particular to a kind of volatile organic compounds processing dress
It sets.
Background technique
Since the industrial revolution, the source of atmospheric pollution that people are familiar with is mainly from petroleum and chemical production processes, fire
Power power generation etc..Its common method are as follows: dedusting, acid-mist-removing, alkali cleaning, desulfurization etc..In aerial gasified harmful substance, some
For volatile organic compounds (VOCs).Mainly from solvent production process or using the process of solvent, such as: coal mining
When drawing-off gas, chemical industry and medicine production, spray painting, dipping, coating process, the assembly and transportational process of gasoline industry
Deng.By taking heating power oxidizing fire processing technique (RTO) handles VOCs gas as an example: use is using 3 Room-RTO waste gas combustion furnaces as core
VOCs waste gas treatment equipment technique, this class process be no lack of exhaust extraction into the heat storage Room 1 for preheat in advance completion into
Row preheating, is then passed through RTO waste gas combustion furnace and carries out burning processing, and organic substance cracking burning in exhaust gas is converted into harmless
High-temperature flue gas (800 DEG C or so), and these purified gas contain a large amount of thermal energy, therefore by flue gas by heat storage Room 2, will be hot
It can recycle, for preheating subsequent cycle.And Partial cleansing gas is passed through the pipeline at heat storage Room 3, it is intended that will be residual in pipe
Residual gas is rinsed into combustion chamber in remaining exhaust gas and heat storage Room 3, is prevented subsequent cycle portion to be mixed into purified gas and is discharged.
But the RTO processing unit of current only Room 3 just needs to be laid with a large amount of pipeline, and various and interminable pipeline keeps gas recyclable
The exhaust gas that the thermal loss utilized does not eliminate quite greatly, in pipeline is more, pipeline service efficiency is insufficient；And it is run in processing
Need the switch of the multiple pipeline valves of frequent switching in the process, one day switching times close to up to ten thousand times, selection to valve and
Intensity requirement is high, and the rate of wear is very fast in use process.
Utility model content
The purpose of this utility model is to overcome above the shortcomings of the prior art, provide a kind of volatile organic
Gas treatment equipment, this volatile organic compounds processing unit it is simple and reasonable for structure, and heat-energy losses can be reduced, also solved
Pipeline is more and tediously long problem.
The purpose of this utility model is realized by the following technical solution: this volatile organic compounds processing unit, including
Triple channel flange end socket, slew buffer tank, gas converting heat tank and heat exchanger tube, the upper end of the slew buffer tank are set there are three first
Venthole, the slew buffer tank is interior to be equipped with partition, and the inner cavity of slew buffer tank is separated into three cushion chambers by partition, and this three
Cushion chamber is respectively the first cushion chamber, the second cushion chamber and third cushion chamber, first cushion chamber, the second cushion chamber and third
Cushion chamber is communicated with three the first ventholes respectively, and wherein the second cushion chamber and third cushion chamber are independent by the second venthole
Connection；The lower end of the slew buffer tank is equipped with third venthole and the 4th venthole, this third venthole and the first cushion chamber
It communicates, the 4th venthole is communicated with the second cushion chamber or the 4th venthole with third cushion chamber；The slew buffer tank
Upper end is rotatably installed on triple channel flange end socket, and three channels in the triple channel flange end socket lead to three first
Stomata is corresponding；The lower end of the slew buffer tank is rotatably installed on gas converting heat tank, is equipped in the gas converting heat tank
Heat exchanging chamber, the lower end of the gas converting heat tank are equipped with air inlet, and the side of the gas converting heat tank is equipped with exhaust outlet；The heat exchanger tube
One end connect with third venthole, the other end of the heat exchanger tube is connect after passing through heat exchanging chamber with air inlet, the four-way
Stomata is connected to by heat exchanging chamber with exhaust outlet, and three the first ventholes are equipped with valve.
Preferably, the slew buffer tank includes buffering tank body and capping, first cushion chamber, the second cushion chamber and the
Three cushion chambers are set in surge tank body, and the capping and the lower ending opening of buffering tank body are tightly connected；The third venthole
It is set to capping with the 4th venthole, three the first ventholes are equipped with the upper end of buffering tank body.
Preferably, the upper end of the buffering tank body is equipped with shaft, and the shaft is sealed by first bearing and triple channel flange
Head connection.
Preferably, the gas converting heat tank includes heat exchange tank body and conversion disk, and the slew buffer tank passes through conversion circle
Disk is connect with heat exchange tank body；The air inlet is set to the lower end of heat exchange tank body, and the exhaust outlet is set to the side wall of heat exchange tank body.
Preferably, the lower end of the slew buffer tank is equipped with the rotation boss with conversion disk match, the rotation boss
It is connect by second bearing with conversion disk.
Preferably, the junction of the conversion disk and the tank body that exchanges heat is equipped with sealing ring.
Preferably, the heat exchanger tube is Z-shaped, and the other end of the heat exchanger tube is connect by 3rd bearing with air inlet.
Preferably, the triple channel flange end socket includes end socket disk and interior three flanged pipes for setting channel, the end socket disk
Middle part with buffering rotary tank rotatably connect, one end of the flanged pipe is connect with end socket disk, and in three flanged pipes
Channel is corresponding with three the first ventholes, and the other end of the flanged pipe is equipped with flange portion.
Preferably, three flanged pipes are distributed relative to the central axis even circumferential of end socket disk.
Preferably, the air inlet and exhaust outlet are equipped with connecting flange.
The utility model has the advantage that compared with the existing technology
1, this volatile organic compounds processing unit is mainly by triple channel flange end socket, slew buffer tank, gas converting heat tank
And heat exchanger tube, set in slew buffer tank there are three cushion chamber and slew buffer tank and triple channel flange end socket it is rotatably mounted,
This solves the problems, such as that the pipeline in volatile organic compounds processing unit is more and tediously long, drastically reduces pipeline and is laid to this
With maintenance cost backward.
2, in this volatile organic compounds processing unit slew buffer tank be arranged three cushion chambers and with three cushion chamber phases
The first logical venthole, and valve is set in the first venthole, these three cushion chambers, three valves and gas converting heat tank etc. are common
Effect, not only reduce that pipeline is more and tediously long problem, recoverable thermal energy gone back, to reduce thermal loss.This is practical new
For type compared with traditional volatile organic compounds processing unit, thermal loss amount can reduce one third.
3, this volatile organic compounds processing unit replaces traditional pipeline using slew buffer tank, to reduce making for pipeline
With, while the use of valve is decreased, while total valve transfer number is only traditional 1 percent, can slow down valve significantly
The abrasion of door also has more selections to the material selection of valve.
4, this volatile organic compounds processing unit reduces the use of pipeline, then can reduce the use of valve, therefore avoids
As traditional identically controlled numerous valves of volatile organic compounds processing unit, Row control hardly possible has been greatly reduced
Degree.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the volatile organic compounds processing unit of embodiment 1.
Fig. 2 is the cross-sectional view of the slew buffer tank of embodiment 1.
Fig. 3 is the top view of the slew buffer tank of embodiment 1.
Fig. 4 is the bottom view of the slew buffer tank of embodiment 1.
Fig. 5 is the cross-sectional view of the triple channel flange end socket of embodiment 1.
Fig. 6 is the top view of the triple channel flange end socket of embodiment 1.
Fig. 7 is the cross-sectional view of the gas converting heat tank of embodiment 1.
Wherein, 1 is triple channel flange end socket, and 101 be end socket disk, and 102 be flanged pipe, and 103 be flange portion, and 104 be channel,
2 be slew buffer tank, and 201 be buffering tank body, and 202 be capping, and 203 be shaft, and 204 be rotation boss, and 3 be gas converting heat tank,
301 be heat exchange tank body, and 302 be conversion disk, and 4 be heat exchanger tube, and 5 be the first venthole, and 6 be partition, and 7 be the first cushion chamber, and 8 are
Second cushion chamber, 9 be third cushion chamber, and 10 be the second venthole, and 11 be third venthole, and 12 be the 4th venthole, and 13 be to change
Hot chamber, 14 be air inlet, and 15 be exhaust outlet, and 16 be valve, and 17 be sealing ring, and 18 be connecting flange, and 19 be first bearing, and 20 are
Second bearing, 21 be 3rd bearing.
Specific embodiment
The utility model is described in further detail with reference to the accompanying drawings and examples.
Embodiment 1
Volatile organic compounds processing unit as shown in Figures 1 to 6, including triple channel flange end socket, slew buffer tank,
Gas converting heat tank and heat exchanger tube, the upper end of the slew buffer tank are set there are three the first venthole, are set in the slew buffer tank
There is partition, the inner cavity of slew buffer tank is separated into three cushion chambers by partition, this three cushion chambers are respectively the first cushion chamber,
Two cushion chambers and third cushion chamber, first cushion chamber, the second cushion chamber and third cushion chamber are ventilated with three first respectively
Hole communicates, and wherein the second cushion chamber is individually connected to third cushion chamber by the second venthole；Under the slew buffer tank
End is equipped with third venthole and the 4th venthole, this third venthole communicates with the first cushion chamber, the 4th venthole and the
Three cushion chambers communicate；The upper end of the slew buffer tank is rotatably installed on triple channel flange end socket, and the threeway Dow process
Three channels in blue end socket are corresponding with three the first ventholes；The lower end of the slew buffer tank is rotatably installed on gas
Body heat exchange tank, the gas converting heat tank is interior to be equipped with heat exchanging chamber, and the lower end of the gas converting heat tank is equipped with air inlet, and the gas changes
The side of hot tank is equipped with exhaust outlet；One end of the heat exchanger tube is connect with third venthole, and the other end of the heat exchanger tube, which passes through, to be changed
It is connect after hot chamber with air inlet, the 4th venthole is connected to by heat exchanging chamber with exhaust outlet, and three the first ventholes are equipped with valve
Door.Specifically, this replaces traditional pipeline using slew buffer tank, so as to effectively reduce the laying length and valve of pipeline
Usage quantity, it is easy to operate, reduce the abrasion and service life of valve.
The slew buffer tank as described in Fig. 2 to Fig. 4 includes buffering tank body and capping, first cushion chamber, the second cushion chamber
It is set in surge tank body with third cushion chamber, the capping and the lower ending opening of buffering tank body are tightly connected；The third is logical
Stomata and the 4th venthole are set to capping, and three the first ventholes are equipped with the upper end of buffering tank body.This structure is simple, facilitates peace
Dress and maintenance.
The upper end of the buffering tank body is equipped with shaft, and the shaft is connect by first bearing with triple channel flange end socket.
This structure is simple, guarantees the rotation that slew buffer tank can be stable.
As shown in fig. 7, the gas converting heat tank includes heat exchange tank body and conversion disk, the slew buffer tank passes through conversion
Disk is connect with heat exchange tank body；The air inlet is set to the lower end of heat exchange tank body, and the exhaust outlet is set to the side wall of heat exchange tank body.
The lower end of the slew buffer tank is equipped with the rotation boss with conversion disk match, and the rotation boss is by second bearing and turns
Change disk connection.Specific rotation boss is set to capping, this structure facilitates installation, and ensure that steady when the rotation of slew buffer tank
It is qualitative.
The junction of the conversion disk and the tank body that exchanges heat is equipped with sealing ring.This guarantees the opposing seal of gas converting heat tank
Property, improve the reliability and heat exchange efficiency of gas converting heat tank.
The heat exchanger tube is Z-shaped, and the other end of the heat exchanger tube is connect by 3rd bearing with air inlet.This can increase
Stroke of the VOCs exhaust gas in gas converting heat tank, to improve heat transfer effect.
The triple channel flange end socket includes end socket disk and interior three flanged pipes for setting channel, the middle part of the end socket disk with
Buffering rotary tank rotatably connects, and one end of the flanged pipe is connect with end socket disk, and the channel and three in three flanged pipes
A first venthole is corresponding, and the other end of the flanged pipe is equipped with flange portion.This structure is simple, facilitates volatile organic compounds
Processing unit is attached with the other component in RTO equipment.Central axis circumference of three flanged pipes relative to end socket disk
It is uniformly distributed.Circular arc solution between i.e. adjacent two flanged pipes is 120 °.
The air inlet and exhaust outlet are equipped with connecting flange.This structure is simple, facilitates connection.
Specific step is as follows for this volatile organic compounds processing unit working method:
(1) VOCs exhaust gas enters heat exchanger tube from air inlet, during the heat exchanger tube that VOCs exhaust gas passes through Z-type with heat exchange tank
Intracorporal high-temperature flue gas carries out first round heat exchange, realizes the first round preheating of VOCs exhaust gas.VOCs after the first round preheats
Into intracorporal first cushion chamber of slew buffer tank, then pass sequentially through the first venthole and corresponding with the first venthole at this time
One channel is preheated subsequently into the first regenerative chamber of RTO equipment with the second wheel.VOCs by two wheel preheatings is passed through RTO and sets
Standby waste gas combustion furnace carries out burning processing, is converted into harmless high-temperature flue gas.The harmless high-temperature flue gas generated after burning enters
Second regenerative chamber of RTO equipment recycles a large amount of thermal energy in high-temperature flue gas by the second regenerative chamber, and then the flue gas is passed through second
Cushion chamber, access enter third cushion chamber from the second cushion chamber.It is divided into two strands in the flue gas of third cushion chamber: wherein one flue gas
Third regenerative chamber is flowed into, will not be eliminated in third regenerative chamber or remaining VOCs is poured at the waste gas combustion furnace of RTO equipment
Reason；Another strand of flue gas enters in heat exchange tank body from the 4th venthole below third cushion chamber, and untreated in heat exchanger tube
VOCs exchanges heat to realize that the first round preheats, and the flue gas after completing heat exchange is discharged from the exhaust outlet of heat exchange tank wall, with reality
Now the waste heat in flue gas is utilized.
(2) when the indoor temperature of the first accumulation of heat drops to critical value, stop injecting VOCs exhaust gas toward air inlet, rotation is slow
It rushes tank body and rotates 120 °, the first cushion chamber passes through another first venthole and the second regenerative chamber phase in slew buffer tank body at this time
It is logical, and the second surge chamber is communicated with third regenerative chamber, third surge chamber is directly communicated with the first regenerative chamber；Then, restore air inlet
The injection of the VOCs exhaust gas of mouth.Then new VOCs exhaust gas enters heat exchanger tube from air inlet, and VOCs exhaust gas passes through the heat exchanger tube of Z-type
First round heat exchange is carried out with the intracorporal high-temperature flue gas of heat exchange tank in the process, realizes the first round preheating of VOCs exhaust gas.By first
VOCs after wheel preheating enters the first cushion chamber, and the second regenerative chamber into RTO equipment is preheated with the second wheel.By two wheel preheatings
VOCs be passed through the waste gas combustion furnace of RTO equipment and carry out burning processing, be converted into harmless high-temperature flue gas.The nothing generated after burning
Evil high-temperature flue gas enters the third regenerative chamber of RTO equipment, recycles a large amount of thermal energy in high-temperature flue gas by third regenerative chamber, then
The flue gas is passed through the second cushion chamber, and access enters third cushion chamber from the second cushion chamber.It is divided into two in the flue gas of third cushion chamber
Stock: wherein one flue gas flows into the first regenerative chamber, will not eliminate in the first regenerative chamber or remaining VOCs pours the useless of RTO equipment
Gas incinerator is handled；Another strand of flue gas enters in heat exchange tank body from the 4th venthole below third cushion chamber, with heat exchange
Untreated VOCs exchanges heat to realize that the first round preheats in managing, exhaust of the flue gas after completing heat exchange from heat exchange tank wall
Mouth discharge, utilizes the waste heat in flue gas with realizing.
(3) when the indoor temperature of the second accumulation of heat drops to critical value, stop injecting VOCs exhaust gas toward air inlet, revolve again
Turn buffering tank body and rotate 120 °, the first cushion chamber is communicated with third regenerative chamber in slew buffer tank body at this time, and the second surge chamber
It is communicated with the first regenerative chamber, third surge chamber is directly communicated with the first regenerative chamber；Then, restore the note of the VOCs exhaust gas of air inlet
Enter.Then new VOCs exhaust gas enters heat exchanger tube from air inlet, during the heat exchanger tube that VOCs exhaust gas passes through Z-type with heat exchange tank body
Interior high-temperature flue gas carries out first round heat exchange, realizes the first round preheating of VOCs exhaust gas.VOCs after the first round preheats into
Enter the first cushion chamber, is preheated subsequently into the third regenerative chamber of RTO equipment with the second wheel.VOCs by two wheel preheatings is passed through
The waste gas combustion furnace of RTO equipment carries out burning processing, is converted into harmless high-temperature flue gas.The harmless high-temperature flue gas generated after burning
Into the first regenerative chamber of RTO equipment, recycle a large amount of thermal energy in high-temperature flue gas by the first regenerative chamber, then the flue gas is passed through
Second cushion chamber, access enter third cushion chamber from the second cushion chamber.Be divided into two strands in the flue gas of third cushion chamber: wherein one
Flue gas flows into third regenerative chamber, will not be eliminated in third regenerative chamber or remaining VOCs pour the waste gas combustion furnace of RTO equipment into
Row processing；Another strand of flue gas enters in heat exchange tank body from the 4th venthole below third cushion chamber, and untreated in heat exchanger tube
VOCs exchange heat with realize the first round preheat, complete heat exchange after flue gas from heat exchange tank wall exhaust outlet discharge, with
Realization utilizes the waste heat in flue gas.
(4) when the indoor temperature of the second accumulation of heat drops to critical value, stop injecting VOCs exhaust gas toward air inlet, revolve again
Turning buffering tank body and rotates 120 °, then the first surge chamber is communicated with the first regenerative chamber, and the second surge chamber and the second regenerative chamber communicate, the
Three surge chambers are communicated with third regenerative chamber, that is, are restPosed；Then step (1) is repeated.
Thus constantly circulation above-mentioned steps both improved work efficiency to realize the uninterrupted processing of VOCs exhaust gas, also
Waste heat can be made full use of, the loss of heat is reduced.
Embodiment 2:
This volatile organic compounds processing unit is in addition to following technical characteristic with embodiment 1: volatile organic compounds processing
Device includes triple channel flange end socket, slew buffer tank, gas converting heat tank and heat exchanger tube, and the upper end of the slew buffer tank is equipped with
Three the first ventholes, the slew buffer tank is interior to be equipped with partition, and the inner cavity of slew buffer tank is separated into three bufferings by partition
Chamber, this three cushion chambers are respectively the first cushion chamber, the second cushion chamber and third cushion chamber, and first cushion chamber, second are delayed
It rushes chamber and third cushion chamber to communicate with three the first ventholes respectively, and wherein the second cushion chamber and third cushion chamber pass through second
Venthole is individually connected to；The lower end of the slew buffer tank be equipped with third venthole and the 4th venthole, this third venthole with
First cushion chamber communicates, and the 4th venthole is communicated with the second cushion chamber；The triple channel flange end socket is rotatably installed
Three channels in the upper end of slew buffer tank, and in the triple channel flange end socket are corresponding with three the first ventholes；Institute
The lower end for stating slew buffer tank is rotatably installed on gas converting heat tank, is equipped with heat exchanging chamber, the gas in the gas converting heat tank
The lower end of body heat exchange tank is equipped with air inlet, and the side of the gas converting heat tank is equipped with exhaust outlet；One end of the heat exchanger tube and third
Venthole connection, the other end of the heat exchanger tube are connect after passing through heat exchanging chamber with air inlet, and the 4th venthole passes through heat exchange
Chamber is connected to exhaust outlet, and three the first ventholes are equipped with valve.This embodiment 1 except the 4th venthole position and embodiment not
Together, the effect of embodiment 1 can be equally realized.
Above-mentioned specific embodiment is the preferred embodiment of the utility model, can not be defined to the utility model,
Other any changes made without departing from the technical solution of the utility model or other equivalent substitute modes, are included in
Within the protection scope of the utility model.
Claims (10)
1. a kind of volatile organic compounds processing unit, it is characterised in that: including triple channel flange end socket, slew buffer tank, gas
Body heat exchange tank and heat exchanger tube, the upper end of the slew buffer tank are set there are three the first venthole, are equipped in the slew buffer tank
The inner cavity of slew buffer tank is separated into three cushion chambers by partition, partition, this three cushion chambers are respectively the first cushion chamber, second
Cushion chamber and third cushion chamber, first cushion chamber, the second cushion chamber and third cushion chamber respectively with three the first ventholes
It communicates, and wherein the second cushion chamber is individually connected to third cushion chamber by the second venthole；The lower end of the slew buffer tank
Equipped with third venthole and the 4th venthole, this third venthole is communicated with the first cushion chamber, the 4th venthole and second
Cushion chamber or the 4th venthole are communicated with third cushion chamber；The upper end of the slew buffer tank is rotatably installed on threeway Dow process
Blue end socket, and three channels in the triple channel flange end socket are corresponding with three the first ventholes；The slew buffer tank
Lower end be rotatably installed on gas converting heat tank, heat exchanging chamber is equipped in the gas converting heat tank, under the gas converting heat tank
End is equipped with air inlet, and the side of the gas converting heat tank is equipped with exhaust outlet；One end of the heat exchanger tube is connect with third venthole, institute
The other end for stating heat exchanger tube is connect after heat exchanging chamber with air inlet, and the 4th venthole is connected by heat exchanging chamber and exhaust outlet
Logical, three the first ventholes are equipped with valve.
2. volatile organic compounds processing unit according to claim 1, it is characterised in that: the slew buffer tank includes
Buffering tank body and capping, first cushion chamber, the second cushion chamber and third cushion chamber are set in surge tank body, the capping
It is tightly connected with the lower ending opening of buffering tank body；The third venthole and the 4th venthole are set to capping, three first ventilations
Kong Jun is set to the upper end of surge tank body.
3. volatile organic compounds processing unit according to claim 2, it is characterised in that: the upper end of the buffering tank body
Equipped with shaft, the shaft is connect by first bearing with triple channel flange end socket.
4. volatile organic compounds processing unit according to claim 1, it is characterised in that: the gas converting heat tank includes
Exchange heat tank body and conversion disk, and the slew buffer tank is connect by conversion disk with heat exchange tank body；The air inlet is set to and changes
The lower end of hot tank body, the exhaust outlet are set to the side wall of heat exchange tank body.
5. volatile organic compounds processing unit according to claim 4, it is characterised in that: under the slew buffer tank
End is equipped with the rotation boss with conversion disk match, and the rotation boss is connect by second bearing with conversion disk.
6. volatile organic compounds processing unit according to claim 4, it is characterised in that: the conversion disk and heat exchange
The junction of tank body is equipped with sealing ring.
7. volatile organic compounds processing unit according to claim 1, it is characterised in that: the heat exchanger tube is Z-shaped, institute
The other end for stating heat exchanger tube is connect by 3rd bearing with air inlet.
8. volatile organic compounds processing unit according to claim 1, it is characterised in that: the triple channel flange end socket
Including end socket disk and interior three flanged pipes for setting channel, the middle part of the end socket disk is rotatably connect with buffering rotary tank, institute
The one end for stating flanged pipe is connect with end socket disk, and the channel in three flanged pipes is corresponding with three the first ventholes, the method
The other end of blue pipe is equipped with flange portion.
9. volatile organic compounds processing unit according to claim 8, it is characterised in that: three flanged pipes are opposite
It is distributed in the central axis even circumferential of end socket disk.
10. volatile organic compounds processing unit according to claim 1, it is characterised in that: the air inlet and exhaust
Mouth is equipped with connecting flange.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822077366.5U CN209512044U (en) | 2018-12-10 | 2018-12-10 | A kind of volatile organic compounds processing unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822077366.5U CN209512044U (en) | 2018-12-10 | 2018-12-10 | A kind of volatile organic compounds processing unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209512044U true CN209512044U (en) | 2019-10-18 |
Family
ID=68194073
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822077366.5U Expired - Fee Related CN209512044U (en) | 2018-12-10 | 2018-12-10 | A kind of volatile organic compounds processing unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209512044U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109579029A (en) * | 2018-12-10 | 2019-04-05 | 华南理工大学 | A kind of VOCs gas treatment equipment |
-
2018
- 2018-12-10 CN CN201822077366.5U patent/CN209512044U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109579029A (en) * | 2018-12-10 | 2019-04-05 | 华南理工大学 | A kind of VOCs gas treatment equipment |
| CN109579029B (en) * | 2018-12-10 | 2023-09-29 | 华南理工大学 | VOCs gas treatment device |
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