CN206715617U - The concentration of VOC and separation discharge processing equipment - Google Patents
The concentration of VOC and separation discharge processing equipment Download PDFInfo
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- CN206715617U CN206715617U CN201720040212.1U CN201720040212U CN206715617U CN 206715617 U CN206715617 U CN 206715617U CN 201720040212 U CN201720040212 U CN 201720040212U CN 206715617 U CN206715617 U CN 206715617U
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- 238000000926 separation method Methods 0.000 title claims abstract description 22
- 238000001179 sorption measurement Methods 0.000 claims abstract description 36
- 230000007246 mechanism Effects 0.000 claims abstract description 23
- 238000000746 purification Methods 0.000 claims abstract description 14
- 238000010276 construction Methods 0.000 claims abstract description 13
- 238000007789 sealing Methods 0.000 claims description 22
- 239000003463 adsorbent Substances 0.000 claims description 8
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 8
- 229910052782 aluminium Inorganic materials 0.000 claims description 8
- 239000004411 aluminium Substances 0.000 claims description 8
- 229920001971 elastomer Polymers 0.000 claims description 7
- 239000000806 elastomer Substances 0.000 claims description 7
- 239000000741 silica gel Substances 0.000 claims description 6
- 229910002027 silica gel Inorganic materials 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 238000012423 maintenance Methods 0.000 abstract description 3
- 239000012855 volatile organic compound Substances 0.000 description 31
- 239000007789 gas Substances 0.000 description 18
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 238000007599 discharging Methods 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000002912 waste gas Substances 0.000 description 3
- 238000004134 energy conservation Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 230000003044 adaptive effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Abstract
Concentration and the separation discharge processing equipment of a kind of VOC, including body are the utility model is related to, blow zones, adsorption zone and purification gas wind outlet area is sequentially provided with the body, release area is connected with the adsorption zone；The blow zones include the first independent air-feeding mechanism connected with the adsorption zone, the second independent air-feeding mechanism connected with the release area；The air-supply power of the first independent air-feeding mechanism is more than the air-supply power of the second independent air-feeding mechanism.The utility model handles air quantity independently supplying, it is simple in construction, energy consumption is small, with steady performance, solve user due to needing plant maintenance and the unnecessary loss brought that stops production, can continuously run for a long time, exhaust purification efficiency reaches more than 95.9%~99%, service life of equipment is grown, and floor space is small, substantially reduces management of investment cost.
Description
Technical field
It the utility model is related to a kind of processing equipment, more particularly to concentration and the separation row of a kind of VOC
Go out processing equipment, belong to VOCs treatment technical field.
Background technology
In the handling process such as PCB, semiconductor manufacturing, medicine, chemical industry, electroceramics, coating, Furniture manufacture, one can be produced
A little organic matters and gas with foreign flavor waste gas, such as directly discharge, air and surrounding environment certainly will can be polluted, therefore waste gas is passed through
Crossing after organic exhaust gas adsorption device is handled can just discharge.Existing organic exhaust gas adsorption device is that have absorption using activated carbon
Effect, it can effectively remove organic matter in waste gas, peculiar smell etc..Due to the physical adsorbability of activated carbon, when its adsorption saturation
Need periodically to safeguard equipment, to change activated carbon adsorption layer in time, user needs equipment closing carrying out examination and maintenance,
Cause equipment can not normal work and stop production, huge economic loss is brought to enterprise.
VOC processing equipments used in the prior art have following deficiency：
(1) volume is big：The adsorbent equipment of legacy equipment is transverse air-intake axle slewing, can be dropped by the wind speed of adsorbent
It is low, if so to increase adsorbance, it is necessary to increase the radius of rotating disk, in order to remove substantial amounts of VOC, the mistake that equipment is designed
In huge, some has been even more than the height limitation of LCD manufacture section chiefs.
(2) precision is small：The intake volume control of existing equipment be branching type, i.e. Wind Volume airduct and small air quantity airduct by
One Fans provide power, and which results in small airduct air quantity to stablize, and air quantity can float in a big scope, influence
VOC adsorption efficiencies.
(3) power consumption is big：Existing equipment can not accomplish the recovery and utilization of heat, cause substantial amounts of heat energy by unnecessary wave
Take, increase the energy consumption of equipment.
Utility model content
The purpose of this utility model is the concentration and separation discharge processing equipment for a kind of VOC of proposition,
Indoor VOC is adsorbed, concentrated, is discharged, is discharged in the processing equipment of one, the equipment also has heat recovery energy-conservation structure
Make, energy-conservation is reached while VOC is largely removed, reduces the purpose of volume.
To reach above-mentioned purpose, the technical solution adopted in the utility model is：A kind of concentration of VOC
And processing equipment, including body are discharged in separation, and blow zones, adsorption zone and purification gas wind outlet area are sequentially provided with the body,
Release area is connected with the adsorption zone；The blow zones include connect with the adsorption zone the first independent air-feeding mechanism, and
Second independent air-feeding mechanism of release area connection；It is only that the air-supply power of the first independent air-feeding mechanism is more than described second
The air-supply power of vertical wind pushing mechanism.
Preferred scheme, the adsorption zone are rotatable vertically arranged cylindric tower structure；Described cylindric
The adsorbent that tower structure is set built with modularization.
Preferred scheme, the release area include being oppositely arranged on the cylindric tower structure outer wall, inwall respectively
Outside plenum area, the inner side plenum area communicated with outside plenum area.
Preferred scheme, the second independent air-feeding mechanism include the second power Fan, connected with second power Fan
The second air supply duct and one end be connected to the blowpipe that second air supply duct connects；Connect on second air supply duct
There is gas heater.
Preferred scheme, the outside plenum area include outer connector, in the outer connector between offer outer cold wind chamber,
External hot air chamber；Both sides further respectively have the blast pipe connected with the second power Fan and connected with external hot air chamber on the outer connector
Logical VOC release pipelines.
Preferred scheme, the inner side plenum area include interior connector；On the interior connector both sides be respectively equipped with it is described
Upper interface that second air supply duct communicates, the side interface connected with the blowpipe；Offered between in the interior connector
The interior hot air cavity communicated with the upper interface, the interior cold wind chamber communicated with side interface.
Preferred scheme, the outside plenum area, inner side plenum area and the cylindric tower structure outer wall, inwall it
Between be provided with seal construction area.
Preferred scheme, the seal construction area include baffle plate, sealing flange and sealing aluminium block；Described sealing flange one end with
Elastomer is provided between the baffle plate；Described sealing aluminium block one end is connected with sealing flange, and the other end is in and the cylindric frame
The arc shape structure that rack and panel construction outer wall, inwall match.
Preferred scheme, the wind outlet area are sequentially provided with cooler, chemical filter and purification gas outlet air flange.
Preferred scheme, silica gel strip is equipped with the cylindric tower structure outer wall, inwall.
Due to the utilization of above-mentioned technical proposal, the utility model has following advantages compared with prior art：
The concentration of the VOC of the utility model and separation discharge processing equipment, processing air quantity are independent
Supply, simple in construction, energy consumption is small, has steady performance, solves user and stops production and bring due to needing plant maintenance
Unnecessary loss, can for a long time continuously run, exhaust purification efficiency reaches more than 95.9%~99%, service life of equipment
Long, floor space is small, substantially reduces management of investment cost.
Brief description of the drawings
Technical solutions of the utility model are described further below in conjunction with the accompanying drawings：
Accompanying drawing 1 is the concentration of VOC of the present utility model and the structural representation of separation discharge processing equipment
Figure；
Accompanying drawing 2 is the concentration of VOC of the present utility model and the opposite side knot of separation discharge processing equipment
Structure schematic diagram
Accompanying drawing 3 is adsorption zone of the present utility model and the structural representation for discharging area；
Accompanying drawing 4 is the adsorption zone of the utility model accompanying drawing 3 and the top plan view in release area；
Accompanying drawing 5 is the structural representation of the outside plenum area of adsorption zone of the present utility model；
Accompanying drawing 6 is the structural representation of the inner side plenum area of adsorption zone of the present utility model；
The seal construction area of the present utility model of accompanying drawing 7 and the structural representation of adsorption zone annexation；
Accompanying drawing 8 is the structural representation for expressing seal construction area of the present utility model.
Wherein：1- bodies；
2- blow zones；The first independent air-feedings of 21- mechanism；The second independent air-feedings of 22- mechanism；The power Fans of 221- second；
The air supply ducts of 222- second；223- blowpipes；224- gas heaters；
3- adsorption zones；The cylindric tower structures of 31-；The adsorbent that 32- modularizations are set；311- silica gel strips；
4- purification gas wind outlet area；41- coolers；42- chemical filters；43- purification gas outlet air flanges；
5- discharges area；Plenum area on the outside of 51-；The outer connectors of 511-；The outer cold wind chambers of 512-；513- external hot air chambers；514- enters
Airduct；515-VOC discharges pipeline；Plenum area on the inside of 52-；Connector in 521-；The upper interfaces of 522-；523- side interfaces；In 524-
Hot air cavity；Cold wind chamber in 525-；
6- seal constructions area；61- baffle plates；62- sealing flanges；63- seals aluminium block；64- elastomers；65- up/down is fixed
Plate.
Embodiment
Below in conjunction with the accompanying drawings and specific embodiment the utility model is described in further detail.
At the concentration and separation discharge of a kind of VOC described in the utility model as shown in accompanying drawing 1,2
Equipment, including body 1 are managed, blow zones 2, adsorption zone 3 and purification gas wind outlet area 4, adsorption zone 3 are sequentially provided with the body 1
On be connected with release area 5；The first independent air-feeding mechanism 21 that blow zones 2 include connect with adsorption zone 3, connect with discharging area 5
Second independent air-feeding mechanism 22；The air-supply power of first independent air-feeding mechanism 21 is more than sending for the second independent air-feeding mechanism 22
Wind power.
Independent air feed is carried out to adsorption zone 3, release area 5 respectively by the different independent air-feeding mechanism of two power, reached
The stable purpose of air quantity, so as to improve removal efficiency.
As shown in accompanying drawing 3,4, adsorption zone 3 is rotatable vertically arranged cylindric tower structure 31；Cylindric
The adsorbent 32 that tower structure 31 is set built with modularization.
As shown in Figure 2, the second independent air-feeding mechanism 22 includes the second power Fan 221 and second power Fan
The second air supply ducts 222 and one end of 221 connections are connected to the blowpipe 223 that second air supply duct 222 connects；Second
Gas heater 224 is connected on air supply duct 222.
Release area 5 include be oppositely arranged on respectively the cylindric outer wall of tower structure 31, inwall outside plenum area 51, with
The inner side plenum area 52 that outside plenum area 51 communicates.
As shown in Figure 5, outside plenum area 51 includes outer connector 511, and outer cold wind is offered between outer connector 511 is interior
Chamber 512, external hot air chamber 513；Both sides further respectively have the blast pipe 514 connected with the second power Fan 221 on outer connector 511
The VOC release pipelines 515 connected with external hot air chamber 513, VOC release pipelines 515 outer end access incinerator.
As shown in Figure 6, inner side plenum area 52 includes interior connector 521；Both sides are respectively equipped with the interior connector 521
The upper interface 522 communicated with the second air supply duct 222, the side interface 523 connected with blowpipe 223；In interior connector 521
Between offer the interior hot air cavity 524 communicated with upper interface 522, the interior cold wind chamber 525 communicated with side interface 523.
The utility model, the air containing VOC is passed through powerful first by the first independent air-feeding mechanism 21
Power Fan inhalation device, into adsorption zone 3, adsorption treatment is carried out, after adsorption zone 3 removes VOC by clean air successively
It is transmitted back to by the cooler 41, chemical filter 42 and purification gas outlet air flange 43 of wind outlet area 4 in room；Wherein cooler
Purification gas is cooled to assigned temperature by 41；Chemical filter 42, VOC is further removed, improve removal efficiency；Purification gas goes out
Purification gas is transmitted back in room by wind flange 43.
Other low power second power Fan 221 is by small air quantity air through blast pipe 514, outer cold wind chamber 512, interior
Cold wind chamber 525 enters adsorption zone 3, this portion gas while cooling to the adsorption zone for having removed VOC of script high temperature
Heating, after enter through interior cold wind chamber 525, side interface 523 in blowpipe 223, after blowpipe 223 being fed through gas adds
After hot device 224, contact with the adsorbent in release area through interior hot air cavity 524 after continuing heating, will be inhaled using the air of high temperature
The VOC adsorbed in attached area discharges (VOC concentration now is original 39 times), is released finally by external hot air chamber 513, VOC
Put pipeline 515 and access incinerator discharge destruction, can thoroughly remove VOC, avoid VOC from producing pollution to air, influence environment.
Wherein normal temperature air has been removed VOC's by inside/outside cold wind chamber 521/512 and blowpipe 223 through high temperature first
After adsorption zone is heated, then deliver to release area 5 after gas heater 224 is heated and carry out VOC release separation.Because
Heat for discharging release VOC in area 5 remains in above, that is, have impact on VOC absorption, waste resource；When small air quantity
Air when passing through it, release area 5 can be cooled, while take away the heat being wasted originally, be re-used, reached heat
The purpose that can be recycled, so as to reach the dual purpose for improving adsorption capacity and reducing energy consumption, this is that existing equipment does not have
Some functions.
Adsorption zone is cylindric tower structure 31, in the absorption that cylindric tower structure 31 is set built with modularization
Agent 32, cylindric tower structure 31 can be achieved to turn clockwise automatically under the effect of bottom power set, when release area 5 connects
After VOC in the adsorbent of contact portion point is totally separated out, cylindric tower structure turns clockwise an angle, and release area continues
Work, make Adsorption Concentration and separation while carry out, improve equipment service efficiency.
As shown in accompanying drawing 7,8, to prevent from discharging area's leakage, its sealing property is improved, is led in outside plenum area 51, inner side
Seal construction area 6 is provided between wind area 52 and the outer wall of cylindric tower structure 31, inwall.Seal construction area 6 include baffle plate 61,
Sealing flange 62 and sealing aluminium block 63；Elastomer 64 is provided between the one end of sealing flange 62 and baffle plate.Baffle plate 61, elastomer 64,
Between sealing flange 62 sets fixed plate 65 over/under, sealing flange 62 can relatively move along up/down fixed plate 65, close
Envelope one end of aluminium block 63 is connected with sealing flange 62, and the other end is in the arc to match with cylindric tower structure outer wall, inwall
Shape structure, it is respectively engaged with the cylindric outer wall of tower structure 31, on inwall.Further to strengthen its sealing property, in cylinder
Silica gel strip 311 is equipped with the outer wall of shape tower structure 31, inwall, sealing aluminium block arc shape structure is tightly connected to silica gel strip
On, silica gel strip 311 has certain elastic force, and under the collective effect of elastomer 64, its sealing property significantly improves.
Make seal construction area that there is adaptive ability by said structure design, sealing surface can be brought into close contact, make to let out
The possibility of dew substantially reduces.
In the present embodiment, elastomer uses spring.
It the above is only concrete application example of the present utility model, do not form any limit to the scope of protection of the utility model
System.All technical schemes formed using equivalent transformation or equivalent replacement, all fall within the utility model rights protection scope it
It is interior.
Claims (10)
1. processing equipment, including body are discharged in the concentration and separation of a kind of VOC, set successively in the body
There are blow zones, adsorption zone and purification gas wind outlet area, it is characterised in that：Release area is connected with the adsorption zone；The air-supply
Area includes the first independent air-feeding mechanism connected with the adsorption zone, the second independent air-feeding mechanism connected with the release area；
The air-supply power of the first independent air-feeding mechanism is more than the air-supply power of the second independent air-feeding mechanism.
2. concentration and the separation discharge processing equipment of VOC according to claim 1, it is characterised in that：
The adsorption zone is rotatable vertically arranged cylindric tower structure；In the cylindric tower structure built with mould
The adsorbent that blockization is set.
3. concentration and the separation discharge processing equipment of VOC according to claim 2, it is characterised in that：
The release area includes the outside plenum area and outside for being oppositely arranged on the cylindric tower structure outer wall, inwall respectively
The inner side plenum area that plenum area communicates.
4. concentration and the separation discharge processing equipment of VOC according to claim 3, it is characterised in that：
The second air supply duct and one that the second independent air-feeding mechanism includes the second power Fan, connected with second power Fan
End is connected to the blowpipe of the second air supply duct connection；Gas heater is connected on second air supply duct.
5. concentration and the separation discharge processing equipment of VOC according to claim 3, it is characterised in that：
The outside plenum area includes outer connector, in the outer connector between offer outer cold wind chamber, external hot air chamber；The outer company
Both sides further respectively have the blast pipe connected with the second power Fan and the VOC connected with external hot air chamber release pipelines on junctor.
6. concentration and the separation discharge processing equipment of VOC according to claim 4, it is characterised in that：
The inner side plenum area includes interior connector；Both sides are respectively equipped with what is communicated with second air supply duct on the interior connector
Upper interface, the side interface connected with the blowpipe；Offer between in the interior connector with it is described on interface communicate
Interior hot air cavity, the interior cold wind chamber communicated with side interface.
7. concentration and the separation discharge processing equipment of VOC according to claim 3, it is characterised in that：
Seal construction area is provided between the outside plenum area, inner side plenum area and the cylindric tower structure outer wall, inwall.
8. concentration and the separation discharge processing equipment of VOC according to claim 7, it is characterised in that：
The seal construction area includes baffle plate, sealing flange and sealing aluminium block；It is provided between described sealing flange one end and the baffle plate
Elastomer；Described sealing aluminium block one end is connected with sealing flange, and the other end is in and the cylindric tower structure outer wall, inwall
The arc shape structure to match.
9. concentration and the separation discharge processing equipment of VOC according to claim 1, it is characterised in that：
The wind outlet area is sequentially provided with cooler, chemical filter and purification gas outlet air flange.
10. the concentration of VOC according to claim 2 and separation discharge processing equipment, its feature exist
In：Silica gel strip is equipped with the cylindric tower structure outer wall, inwall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720040212.1U CN206715617U (en) | 2017-01-13 | 2017-01-13 | The concentration of VOC and separation discharge processing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720040212.1U CN206715617U (en) | 2017-01-13 | 2017-01-13 | The concentration of VOC and separation discharge processing equipment |
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| Publication Number | Publication Date |
|---|---|
| CN206715617U true CN206715617U (en) | 2017-12-08 |
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| CN201720040212.1U Active CN206715617U (en) | 2017-01-13 | 2017-01-13 | The concentration of VOC and separation discharge processing equipment |
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| Country | Link |
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| CN (1) | CN206715617U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106731469A (en) * | 2017-01-13 | 2017-05-31 | 苏州悠远环境科技股份有限公司 | The concentration of VOC and separation discharge processing equipment |
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2017
- 2017-01-13 CN CN201720040212.1U patent/CN206715617U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106731469A (en) * | 2017-01-13 | 2017-05-31 | 苏州悠远环境科技股份有限公司 | The concentration of VOC and separation discharge processing equipment |
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| GR01 | Patent grant | ||
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| CP01 | Change in the name or title of a patent holder |
Address after: 215000 Jiangsu city of Suzhou province Taicang city Shaxi town Yue Wang Taiwan Science and Technology Innovation Industrial Park Patentee after: SUZHOU YOUYUAN ENVIRONMENTAL SCIENCE AND TECHNOLOGY CO., LTD. Address before: 215000 Jiangsu city of Suzhou province Taicang city Shaxi town Yue Wang Taiwan Science and Technology Innovation Industrial Park Patentee before: Suzhou Polytron Technologies Inc |