CN208194044U - Zeolite runner Adsorption Concentration cleaning equipment - Google Patents
Zeolite runner Adsorption Concentration cleaning equipment Download PDFInfo
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- CN208194044U CN208194044U CN201820288784.6U CN201820288784U CN208194044U CN 208194044 U CN208194044 U CN 208194044U CN 201820288784 U CN201820288784 U CN 201820288784U CN 208194044 U CN208194044 U CN 208194044U
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Abstract
The utility model provides a kind of zeolite runner Adsorption Concentration cleaning equipment, including filter device, zeolite runner, heating device, catalytic combustion system and control system；The zeolite runner is equipped with adsorption zone, cooling zone and renewing zone, and the filter device is connect by the first air inlet pipe with absorption blower, and the absorption blower is connect by the second air inlet pipe with adsorption zone, and the adsorption zone is connect with blowdown stack；Second air inlet pipe is in charge of equipped with air inlet, and the air inlet is in charge of to be connect with cooling zone, and the cooling zone is connect by the first escape pipe with heating device, and the heating device is connect with the renewing zone；The renewing zone is connect with desorption blower, and the desorption blower is connect by the second escape pipe with catalytic combustion system；Second escape pipe is in charge of equipped with outlet, and the outlet is in charge of to be connected to first air inlet pipe.The utility model can handle the organic exhaust gas of low concentration, Wind Volume；Structurally simple, economical saving, purification efficiency are high.
Description
Technical field
The utility model relates to the purified treatment fields of organic waste, net more particularly to a kind of zeolite runner Adsorption Concentration
Change equipment.
Background technique
In industries such as packages printing, coating, electronics sprayings, zeolite runner is because for the treatment of effeciency height, long service life, processing wind
Amount is big, take up little area, adsorption desorption is high-efficient and is widely used.Organic exhaust gas passes through the adsorption zone of concentration runner device.It is adsorbing
Area VOC is discharged by zeolite Adsorption, purified air from the processing section of concentration runner.It is adsorbed in having in concentration runner
Machine exhaust gas VOCs is handled through hot wind in renewing zone and is desorbed, is concentrated to 5~20 times of degree.
Now, the enterprise of VOC is generated because of differences such as production technology, operating condition, products, the type difference for generating exhaust gas is larger,
It is lower than the exhaust gas of 100mg/m3 for processing VOC concentration, zeolite runner is concentrated 5~20 times, and concentrated gas enters heat accumulating type catalysis
There is still a need for consume certain energy to guarantee the abundant reaction of exhaust gas for combustion bed system.
Application No. is 201620440811.8 Chinese utility model patent, to disclose a kind of zeolite runner organic exhaust gas net
Makeup is set, including filter, zeolite runner, heater, catalytic combustion system, heat exchanger, system fan, desorption blower, heat exchange
Device and pipeline；The zeolite runner is equipped with adsorption zone, desorption area and cooling zone；The filter, adsorption zone and system fan are logical
Piping is successively linked in sequence；The filter, heat exchanger, heater, desorption area, desorption blower, heat exchanger, is urged at cooling zone
Change burner, heat exchanger, heat exchanger, adsorption zone and system fan to be successively linked in sequence by pipeline；The filter is
Grain object filter.Although above-mentioned zeolite runner cleaning equipment for waste organic gas can purify in Wind Volume, the organic exhaust gas of low concentration,
However there is still a need for consume certain energy to guarantee the abundant reaction of exhaust gas.
Utility model content
The technical problem to be solved by the present invention is to provide a kind of zeolite runner Adsorption Concentration cleaning equipments, existing to overcome
There is the drawbacks described above of technology.
To achieve the above object, the utility model provides a kind of zeolite runner Adsorption Concentration cleaning equipment, including filtering dress
It sets, zeolite runner, heating device, catalytic combustion system and control system；The zeolite runner be equipped with adsorption zone, cooling zone and
Renewing zone, the filter device by the first air inlet pipe with absorption blower connect, the absorption blower pass through the second air inlet pipe and
Adsorption zone connection, the adsorption zone are connect with blowdown stack；Second air inlet pipe is in charge of equipped with air inlet, and the air inlet is in charge of
It is connect with cooling zone, the cooling zone is connect by the first escape pipe with heating device, the heating device and the renewing zone
Connection；The renewing zone is connect with desorption blower, and the desorption blower is connect by the second escape pipe with catalytic combustion system；Institute
It states the second escape pipe to be in charge of equipped with outlet, the outlet is in charge of to be connected to first air inlet pipe.
Preferably, the air inlet, which is in charge of, is equipped with the first control valve, and second escape pipe is equipped with the second control valve, institute
Outlet is stated to be in charge of equipped with third control valve, first control valve, second control valve and third control valve difference
It is connected with control system.
Preferably, the position on second escape pipe close to desorption blower is equipped with VOC concentration meter.
Preferably, the filter device is equipped with the first filter layer that filtration grade is G3, and filtration grade is the second of G4
The third filter layer that filter layer and filtration grade are F9.
Preferably, the catalytic combustion system is heat accumulating type catalytic bed.
It preferably, further include the First Heat Exchanger of concentrated gas and heating described second in heating first escape pipe
Second heat exchanger of concentrated gas in escape pipe.
Preferably, the gas outlet of the catalytic combustion system is connect by third escape pipe with the second heat exchanger, and described the
Two heat exchangers are connect with the First Heat Exchanger, and the First Heat Exchanger is connect with blowdown stack.
Preferably, the third escape pipe is equipped with the 4th control valve, and the 4th control valve is connect with control system.
As described above, the utility model relates to zeolite runner Adsorption Concentration cleaning equipment, have the advantages that this
Utility model can handle the organic exhaust gas of low concentration, Wind Volume；Structurally simple, economical saving, purification efficiency are high.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
Component label instructions
1 filter device
11 first air inlet pipe
101 first filter layers
102 second filter layers
103 third filter layers
2 zeolite runners
201 adsorption zones
202 cooling zones
203 renewing zones
21 first escape pipes
3 heating devices
4 catalytic combustion systems
41 First Heat Exchangers
42 second heat exchangers
43 third escape pipes
431 the 4th control valves
5 absorption blowers
51 second air inlet pipe
52 air inlets are in charge of
521 first control valves
6 blowdown stacks
7 desorption blowers
71 second escape pipes
711 second control valves
712 VOC concentration meters
72 outlets are in charge of
721 third control valves
Specific embodiment
The embodiments of the present invention is illustrated by particular specific embodiment below, those skilled in the art can be by this
Content disclosed by specification understands other advantages and effect of the utility model easily.
It should be clear that this specification structure depicted in this specification institute accompanying drawings, ratio, size etc., only to cooperate specification to be taken off
The content shown is not intended to limit the utility model enforceable restriction item so that those skilled in the art understands and reads
Part, therefore do not have technical essential meaning, the modification of any structure, the change of proportionate relationship or the adjustment of size are not influencing
Under the effect of the utility model can be generated and the purpose that can reach, should all still it fall in the revealed technology of the utility model
In the range of appearance can cover.Meanwhile in this specification cited such as "upper", "lower", "left", "right", " centre " term,
It is merely convenient to being illustrated for narration, rather than to limit the enforceable range of the utility model, the change of relativeness or tune
It is whole, under the content of no substantial changes in technology, when being also considered as the enforceable scope of the utility model.
As shown in Figure 1, the utility model provides a kind of zeolite runner Adsorption Concentration cleaning equipment, including filter device 1, boiling
Stone runner 2, heating device 3, catalytic combustion system 4 and control system.There is the filter device 1 filtering dust, impurity to go forward side by side
The functions such as row drying.The zeolite runner 2 is equipped with adsorption zone 201, cooling zone 202 and renewing zone 203, the filter device 1
It being connect by the first air inlet pipe 11 with absorption blower 5, the absorption blower 5 is connect by the second air inlet pipe 51 with adsorption zone 201,
The adsorption zone 201 is connect with blowdown stack 6；Second air inlet pipe 51 is equipped with air inlet and is in charge of 52, and the air inlet is in charge of 52
Connect with cooling zone 202, the cooling zone 202 is connect by the first escape pipe 21 with heating device 3, the heating device 3 and
The renewing zone 203 connects；The renewing zone 203 is connect with desorption blower 7, and the desorption blower 7 passes through the second escape pipe 71
It is connect with catalytic combustion system 4；Second escape pipe 71 is equipped with outlet and is in charge of 72, and the outlet is in charge of 72 and described first
Air inlet pipe 11 is connected to.
When utility model works, organic exhaust gas adsorbs blower 5 for most exhaust gas after the filtering of filter device 1
Through being sent into the adsorption zone 201 of zeolite runner 2,6 qualified discharge of blowdown stack is passed through by the gas after zeolite adsorption cleaning.Absorption
Fraction organic exhaust gas is also sent into the cooling drying in cooling zone 202 by blower 5, then by heating device 3 by temperature be increased to
Assigned temperature is used as regeneration air, is re-fed into renewing zone 203, and the organic solvent on the zeolite of adsorption saturation is heated desorption
Out, restore the adsorption capacity of zeolite.Desorption concentration air-flow behind renewing zone 203 passes through desorption blower 7 again and changes through second
Hot device 42 is sent into catalytic combustion system 4 after heating up, and is burnt, is converted into nontoxic under the action of catalyst after further heating
Free of contamination gas discharge.
Preferably, the utility model further include the First Heat Exchanger 41 of concentrated gas in heating first escape pipe 21 with
And the second heat exchanger 42 of concentrated gas in second escape pipe 71 is heated, the gas outlet of the catalytic combustion system 4 passes through
Third escape pipe 43 is connect with the second heat exchanger 42, and second heat exchanger 42 is connect with the First Heat Exchanger 41, and described
One heat exchanger 41 is connect with blowdown stack 6, through catalytic combustion system 4 burning after gas can enter the second heat exchanger 42 with it is described
Concentrated gas in second escape pipe 71 carries out heat exchange, subsequently into First Heat Exchanger 41 and first escape pipe 41
Concentrated gas carries out heat exchange, is discharged finally by blowdown stack 6, further saves the energy.Preferably, the third goes out
Tracheae 43 is equipped with the 4th control valve 431, and the 4th control valve 431 is connect with control system, is controlled by the 4th control valve 431
System enters the hot gas in third escape pipe 43.
Preferably, the air inlet is in charge of 52 equipped with the first control valve 521, and second escape pipe 71 is equipped with the second control
Valve 711 processed, the outlet are in charge of 72 and are equipped with third control valve 721, the position of close desorption blower 7 on second escape pipe 71
VOC concentration meter 712, first control valve 521, second control valve 711, the third control valve 721 and institute are installed
It states VOC concentration meter 712 to connect with control system respectively, conventional PLC control device can be used in the control system.Open first
Control valve 521 can control small part organic exhaust gas to be sent into the cooling drying in cooling zone 202；When the desorption that VOC concentration meter 712 is shown
When concentration is less than setting value, all it is back to zeolite by the second control valve 711 and the control desorption exhaust gas of third control valve 721 and turns
Wheel 2 runs some cycles, and when VOC concentration meter 712 reaches appropriate value, control system automatically controls the second control valve 711 and third
Control valve 721, a part are back to zeolite runner 2, and a part enters catalytic combustion system 4, after catalytic combustion system 4 burns
Heat can exchange heat for the gas in the first escape pipe 21 and the second escape pipe 71, improve heat utilization rate.
Preferably, the filter device 1 is equipped with the first filter layer 101 that filtration grade is G3, and filtration grade is G4's
The third filter layer 103 that second filter layer 102 and filtration grade are F9, wherein filtration grade is using China and European air filtration
The criteria for classifying of device, G3 grade correspond to partial size >=5.0 μm, 70 > E >=50%, G4 grade of filter efficiency correspond to partial size >=
5.0 μm, 90 > E >=70%, F9 grade of filter efficiency corresponds to partial size >=1.0 μm, 99 > E >=90% of filter efficiency.Preferably,
The catalytic combustion system 4 is heat accumulating type catalytic bed.
In conclusion the utility model effectively overcomes various shortcoming in the prior art and has high industrial exploitation value
Value.
The above embodiments are only illustrative of the principle and efficacy of the utility model, and not for limitation, this is practical new
Type.Any person skilled in the art can all carry out above-described embodiment under the spirit and scope without prejudice to the utility model
Modifications and changes.Therefore, such as those of ordinary skill in the art without departing from the revealed essence of the utility model
All equivalent modifications or change completed under mind and technical idea, should be covered by the claim of the utility model.
Claims (8)
1. a kind of zeolite runner Adsorption Concentration cleaning equipment, which is characterized in that including filter device (1), zeolite runner (2), add
Thermal (3), catalytic combustion system (4) and control system；The zeolite runner (2) is equipped with adsorption zone (201), cooling zone
(202) it is connect by the first air inlet pipe (11) with absorption blower (5) with renewing zone (203), the filter device (1), the suction
Attached blower (5) is connect by the second air inlet pipe (51) with adsorption zone (201), and the adsorption zone (201) and blowdown stack (6) are even
It connects；Second air inlet pipe (51) is equipped with air inlet and is in charge of (52), and the air inlet is in charge of (52) and is connect with cooling zone (202), institute
It states cooling zone (202) to connect by the first escape pipe (21) with heating device (3), the heating device (3) and the renewing zone
(203) it connects；The renewing zone (203) connect with desorption blower (7), and the desorption blower (7) passes through the second escape pipe (71)
It is connect with catalytic combustion system (4)；Second escape pipe (71) be equipped with outlet be in charge of (72), the outlet be in charge of (72) with
First air inlet pipe (11) connection.
2. zeolite runner Adsorption Concentration cleaning equipment according to claim 1, it is characterised in that: (52) are in charge of in the air inlet
It is equipped with the first control valve (521), second escape pipe (71) is equipped with the second control valve (711), and the outlet is in charge of
(72) third control valve (721) are equipped with, first control valve (521), second control valve (711) and the third control
Valve (721) processed connects with control system respectively.
3. zeolite runner Adsorption Concentration cleaning equipment according to claim 1, it is characterised in that: second escape pipe
(71) VOC concentration meter (712) are equipped with close to the position of desorption blower (7) on.
4. zeolite runner Adsorption Concentration cleaning equipment according to claim 1, it is characterised in that: the filter device (1)
It is equipped with the first filter layer (101) that filtration grade is G3, the second filter layer (102) and filtration grade that filtration grade is G4 are
The third filter layer (103) of F9.
5. zeolite runner Adsorption Concentration cleaning equipment according to claim 1, it is characterised in that: the catalytic combustion system
It (4) is heat accumulating type catalytic bed.
6. zeolite runner Adsorption Concentration cleaning equipment according to claim 1, it is characterised in that: further include heating described the
The First Heat Exchanger (41) of one escape pipe (21) interior concentrated gas and the heating interior concentrated gas of second escape pipe (71)
Second heat exchanger (42).
7. zeolite runner Adsorption Concentration cleaning equipment according to claim 6, it is characterised in that: the catalytic combustion system
(4) gas outlet is connect by third escape pipe (43) with the second heat exchanger (42), second heat exchanger (42) and described the
One heat exchanger (41) connection, the First Heat Exchanger (41) connect with blowdown stack (6).
8. zeolite runner Adsorption Concentration cleaning equipment according to claim 7, it is characterised in that: the third escape pipe
(43) it is equipped with the 4th control valve (431), the 4th control valve (431) connect with control system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820288784.6U CN208194044U (en) | 2018-03-01 | 2018-03-01 | Zeolite runner Adsorption Concentration cleaning equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820288784.6U CN208194044U (en) | 2018-03-01 | 2018-03-01 | Zeolite runner Adsorption Concentration cleaning equipment |
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| Publication Number | Publication Date |
|---|---|
| CN208194044U true CN208194044U (en) | 2018-12-07 |
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ID=64534824
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820288784.6U Active CN208194044U (en) | 2018-03-01 | 2018-03-01 | Zeolite runner Adsorption Concentration cleaning equipment |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109847536A (en) * | 2019-01-31 | 2019-06-07 | 上海大学 | Organic exhaust gas recirculating system and processing method is concentrated in molecular sieve runner |
| CN110075667A (en) * | 2019-05-30 | 2019-08-02 | 江苏新聚环保科技有限公司 | Exhaust treatment system |
| CN110075666A (en) * | 2019-05-30 | 2019-08-02 | 江苏新聚环保科技有限公司 | Exhaust treatment system |
| CN110354639A (en) * | 2019-08-09 | 2019-10-22 | 锦治环保科技(上海)有限公司 | A kind of process based on promotion zeolite runner concentration rate |
| CN111457398A (en) * | 2019-01-21 | 2020-07-28 | 华懋科技股份有限公司 | Direct-combustion backflow high-efficiency organic waste gas treatment system and method |
| CN111804122A (en) * | 2019-04-12 | 2020-10-23 | 华懋科技股份有限公司 | High-efficiency organic waste gas treatment system and method for reflux heat recovery |
| CN111804121A (en) * | 2019-04-12 | 2020-10-23 | 华懋科技股份有限公司 | High-efficiency backflow organic waste gas treatment system and method |
| CN112044236A (en) * | 2020-09-15 | 2020-12-08 | 广州华科环保工程有限公司 | Organic waste gas treatment system and method based on zeolite rotating wheel |
| CN114191936A (en) * | 2021-11-24 | 2022-03-18 | 江苏大信环境科技有限公司 | Comprehensive system for treating low-concentration waste gas by using RTO (regenerative thermal oxidizer) |
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2018
- 2018-03-01 CN CN201820288784.6U patent/CN208194044U/en active Active
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111457398A (en) * | 2019-01-21 | 2020-07-28 | 华懋科技股份有限公司 | Direct-combustion backflow high-efficiency organic waste gas treatment system and method |
| CN109847536B (en) * | 2019-01-31 | 2021-09-07 | 上海大学 | Molecular sieve rotating wheel concentrated organic waste gas recirculation system and treatment method |
| CN109847536A (en) * | 2019-01-31 | 2019-06-07 | 上海大学 | Organic exhaust gas recirculating system and processing method is concentrated in molecular sieve runner |
| CN111804121A (en) * | 2019-04-12 | 2020-10-23 | 华懋科技股份有限公司 | High-efficiency backflow organic waste gas treatment system and method |
| CN111804122A (en) * | 2019-04-12 | 2020-10-23 | 华懋科技股份有限公司 | High-efficiency organic waste gas treatment system and method for reflux heat recovery |
| TWI718521B (en) * | 2019-04-12 | 2021-02-11 | 華懋科技股份有限公司 | Reflux high-efficiency organic waste gas treatment system and method |
| CN110075666A (en) * | 2019-05-30 | 2019-08-02 | 江苏新聚环保科技有限公司 | Exhaust treatment system |
| CN110075667A (en) * | 2019-05-30 | 2019-08-02 | 江苏新聚环保科技有限公司 | Exhaust treatment system |
| CN110075667B (en) * | 2019-05-30 | 2024-04-02 | 江苏新聚环保科技有限公司 | Exhaust gas treatment system |
| CN110075666B (en) * | 2019-05-30 | 2024-05-14 | 江苏新聚环保科技有限公司 | Exhaust gas treatment system |
| CN110354639A (en) * | 2019-08-09 | 2019-10-22 | 锦治环保科技(上海)有限公司 | A kind of process based on promotion zeolite runner concentration rate |
| CN112044236A (en) * | 2020-09-15 | 2020-12-08 | 广州华科环保工程有限公司 | Organic waste gas treatment system and method based on zeolite rotating wheel |
| CN114191936A (en) * | 2021-11-24 | 2022-03-18 | 江苏大信环境科技有限公司 | Comprehensive system for treating low-concentration waste gas by using RTO (regenerative thermal oxidizer) |
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