CN106731468A - A kind of VOC adsorbent equipment - Google Patents
A kind of VOC adsorbent equipment Download PDFInfo
- Publication number
- CN106731468A CN106731468A CN201710025041.XA CN201710025041A CN106731468A CN 106731468 A CN106731468 A CN 106731468A CN 201710025041 A CN201710025041 A CN 201710025041A CN 106731468 A CN106731468 A CN 106731468A
- Authority
- CN
- China
- Prior art keywords
- voc
- adsorbent equipment
- interior
- area
- tower structure
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000003463 adsorbent Substances 0.000 title claims abstract description 32
- 239000000463 material Substances 0.000 claims abstract description 5
- 238000007789 sealing Methods 0.000 claims description 22
- 238000010276 construction Methods 0.000 claims description 11
- 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
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 5
- 238000000926 separation method Methods 0.000 claims 1
- 238000009423 ventilation Methods 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 abstract description 10
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 238000010521 absorption reaction Methods 0.000 abstract description 4
- 238000012423 maintenance Methods 0.000 abstract description 4
- 238000005516 engineering process Methods 0.000 abstract description 3
- 238000000746 purification Methods 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 239000002912 waste gas Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 230000006978 adaptation Effects 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 238000005265 energy consumption 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
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
- B01D2257/708—Volatile organic compounds V.O.C.'s
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40083—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption
- B01D2259/40088—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by heating
- B01D2259/4009—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by heating using hot gas
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treating Waste Gases (AREA)
Abstract
The present invention relates to a kind of VOC adsorbent equipment, belong to VOC processing technology field, be the cylindric tower structure that the sorbing material assembling set by several modularizations is constituted；The power set for driving its rotation are provided with below cylindric tower structure.The present invention program makes its dismounting and change convenient and swift by the sorbing material that modularization is set；Adsorption Concentration is separated into integrated design with release, absorption can be concentrated to be separated with release while carrying out, solve user due to need plant maintenance and the unnecessary loss for bringing that stops production, can continuously run for a long time, exhaust purification efficiency reaches more than 95.9% 99%, service life of equipment is long, and floor space is small, substantially reduces management of investment cost.
Description
Technical field
The present invention relates to a kind of adsorbent equipment, more particularly to a kind of VOC adsorbent equipment, belong to volatilization
Property organic compound processing technology 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, and air and surrounding environment certainly will can be polluted, therefore waste gas is passed through
Crossing after organic exhaust gas adsorption device is processed can just discharge.Existing exhaust gas adsorption device is that using activated carbon there is absorption to make
With can effectively remove organic matter, peculiar smell in waste gas etc..Due to the physical adsorbability of activated carbon, needed when its adsorption saturation
Periodically equipment is safeguarded, activated carbon adsorption layer is changed in time, and user needs for equipment closing to carry out examination and maintenance, leads
Cause equipment cannot normal work and stop production, bring huge economic loss to enterprise.And the structure of adsorbent equipment is fixed
Formula, dismounting is not easy, and changes adsorbent cumbersome.
The content of the invention
The present invention provides a kind of VOC adsorbent equipment in view of the shortcomings of the prior art, and dismounting is more
Change conveniently, and Adsorption Concentration is separated into integrated design with release, solve organic matter, peculiar smell waste gas treatment equipment and stop
Machine maintenance issues.
To reach above-mentioned purpose, the technical solution adopted by the present invention is a kind of VOC adsorbent equipment, institute
It is the cylindric frame-type that the sorbing material assembling set by several modularizations is constituted to state VOC adsorbent equipment
Structure；The cylindric tower structure lower section is provided with the power set for driving its rotation.
Preferred scheme, equipped with release area on the cylindric tower structure.
Preferred scheme, the release area includes being oppositely arranged on the cylindric tower structure outer wall, inwall respectively
The inner side plenum area that outside plenum area communicates with outside plenum area.
Preferred scheme, the outside plenum area includes outer connector, in the outer connector between offer outer cold wind chamber,
External hot air chamber；Both sides further respectively have the blast pipe that is communicated with outer cold wind chamber and are connected with external hot air chamber on the outer connector
VOC discharges pipeline；The air intake tube end is connected with the second power Fan communicated with outside air.
Preferred scheme, the inner side plenum area includes interior connector；Offered between in the interior connector interior hot air cavity,
Interior cold wind chamber；The interior connector top both sides further respectively have the side interface and the interior hot air cavity communicated with interior cold wind chamber
The upper interface for communicating；The second air supply duct with gas heater is connected with the upper interface；The side interface is by sending
Wind branch pipe is connected with second air supply duct；The outer cold wind chamber, interior cold wind chamber, interior hot air cavity, external hot air chamber internal gas flow
Circulation is communicated.
Preferred scheme, the outside plenum area, inner side plenum area and the cylindric tower structure outer wall, inwall it
Between be equipped with seal construction area.
Preferred scheme, the seal construction area includes 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, silica gel strip is equipped with the cylindric tower structure outer wall, inwall.
Due to the utilization of above-mentioned technical proposal, the present invention has following advantages compared with prior art：
The VOC adsorbent equipment of the present invention program, the sorbing material that modularization is set makes its dismounting and change
It is convenient and swift；Adsorption Concentration is separated into integrated design with release, absorption can be concentrated and separated with release while carrying out, solution
User determine due to needing plant maintenance and the unnecessary loss for bringing that stops production, can continuously run for a long time, waste gas purification effect
Rate reaches more than 95.9%-99%, and service life of equipment is long, and floor space is small, substantially reduces management of investment cost.
Brief description of the drawings
Technical solution of the present invention is described further below in conjunction with the accompanying drawings：
Accompanying drawing 1 is the structural representation of VOC adsorbent equipment of the invention；
Accompanying drawing 2 is the use state structural representation of VOC adsorbent equipment of the invention；
Accompanying drawing 3 is the top plan view of accompanying drawing of the present invention 1；
Accompanying drawing 4 is the structural representation of outside plenum area of the invention；
Accompanying drawing 5 is the structural representation of present invention inner side plenum area；
The seal construction area of the invention of accompanying drawing 6 and the structural representation of adsorbent equipment annexation；
Accompanying drawing 7 is the structural representation in expression seal construction area of the invention.
Wherein：The first independent air-feedings of 21- mechanism；The second independent air-feedings of 22- mechanism；The power Fans of 221- second；222-
Two air supply ducts；223- blowpipes；224- gas heaters；
The cylindric tower structures of 31-；The adsorbent that 32- modularizations are set；311- silica gel strips；
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 airs chamber；514- enters
Airduct；515-VOC discharges pipeline；52- inner sides plenum area；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.
Specific embodiment
Below in conjunction with the accompanying drawings and specific embodiment the present invention is described in further detail.
VOC adsorbent equipment of the present invention as shown in Figure 1, is rotatable vertically arranged
Cylindric tower structure 31, be provided with below cylindric tower structure 31 provide rotary power power set (do not show
Go out)；In the adsorbent 32 that cylindric tower structure 31 is set built with modularization.It is equipped with cylindric tower structure 31
Release area 5, is capable of achieving to turn clockwise automatically, when in the adsorbent of the release contact portion of area 5 in the presence of power set
After VOC is totally separated out, cylindric tower structure turns clockwise an angle, and release area works on, make Adsorption Concentration and
Separate is carried out simultaneously, improves equipment service efficiency.
Release area 5 include be oppositely arranged on respectively the outer wall of cylindric tower structure 31, the outside plenum area 51 of inwall and
The inner side plenum area 52 that outside plenum area 51 communicates.
As shown in Figure 2, VOC adsorbent equipment is connected with the second independent air-feeding mechanism 22, and second is only
Vertical wind pushing mechanism includes the second air supply duct 222 and that the second power Fan 221 is connected with second power Fan 221
End is connected to the blowpipe 223 of the connection of the second air supply duct 222；Gas heater is connected on second air supply duct 222
224。
As shown in accompanying drawing 3,4, outside plenum area 51 includes outer connector 511, in the outer connector 511 between offer it is outer cold
Wind chamber 512, external hot air chamber 513；Both sides further respectively have the blast pipe connected with the second power Fan 221 on outer connector 511
514 and the VOC release pipelines 515 that are connected with external hot air chamber 513, incinerator is accessed in VOC releases pipeline 515 outer end.
As shown in accompanying drawing 3,5, inner side plenum area 52 includes interior connector 521；Both sides set respectively on the interior connector 521
There is the side interface 523 that the upper interface 522 communicated with the second air supply duct 222 is connected with blowpipe 223；In interior connector 521
The interior cold wind chamber 525 that the interior hot air cavity 524 communicated with upper interface 522 is communicated with side interface 523 is offered between interior.
The present invention program, powerful first power is passed through by the first independent air-feeding mechanism 21 by the air containing VOC
Blower fan inhalation device, into adsorbent equipment, carries out adsorption treatment.Other low power second power Fan 221 will be small
Air quantity air enters adsorbent equipment 3, the removal to script high temperature through blast pipe 514, outer cold wind chamber 512, interior cold wind chamber 525
The intensification of this portion gas while the adsorbent equipment of VOC is lowered the temperature, after through interior cold wind chamber 525, side interface 523 enter give
In wind branch pipe 223, after gas heater 224 is fed through after blowpipe 223, continue heat after through interior hot air cavity 524 with release
The adsorbent contact in area is put, the VOC adsorbed in adsorbed device is discharged that (VOC now is dense using the air of high temperature
Degree is original 39 times), access incinerator discharge finally by external hot air chamber 513, VOC release pipeline 515 and destroy, can thoroughly go
Except VOC, it is to avoid VOC produces pollution to air, environment is influenceed.
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 adsorbent equipment is heated, then delivered to after gas heater 224 is heated release area 5 carry out VOC release separate.Cause
It is to be remained in above for discharging the heat of release VOC in area 5, that is, have impact on the absorption of VOC, wastes resource；When small wind
When the air of amount passes through it, release area 5 can be lowered the temperature, while taking away the heat being wasted originally, be re-used, reached
The purpose of heat energy recycle, the dual purpose of adsorption capacity and reducing energy consumption is improved so as to reach, this be existing equipment institute not
The function having.
As illustrated in 6,7, to prevent release area from revealing, its sealing property is improved, it is logical 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,
Sealing flange 62 is set between fixed plate 65 over/under, and sealing flange 62 can be relatively moved 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 matched with cylindric tower structure outer wall, inwall
Shape structure, is connected on the outer wall of cylindric tower structure 31, inwall respectively.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 is significantly improved.
The ability that seal construction area has self adaptation is made by said structure design, sealing surface can be brought into close contact, make to let out
The possibility of dew is substantially reduced.
In the present embodiment, elastomer uses spring.
The above is only concrete application example of the invention, protection scope of the present invention is not limited in any way.All uses
Equivalents or equivalence replacement and the technical scheme that is formed, all fall within rights protection scope of the present invention.
Claims (8)
1. a kind of VOC adsorbent equipment, it is characterised in that：The VOC adsorbent equipment is
The cylindric tower structure that the sorbing material assembling set by several modularizations is constituted；The cylindric tower structure lower section
It is provided with the power set for driving its rotation.
2. VOC adsorbent equipment according to claim 1, it is characterised in that：In the cylindric framework
Equipped with release area in formula structure.
3. VOC adsorbent equipment according to claim 2, it is characterised in that：The release area includes dividing
Be not oppositely arranged on the cylindric tower structure outer wall, the inner side that the outside plenum area of inwall communicates with outside plenum area
Plenum area.
4. VOC adsorbent equipment according to claim 3, it is characterised in that：The outside plenum area bag
Include outer connector, in the outer connector between offer outer cold wind chamber, external hot air chamber；Both sides are also distinguished on the outer connector
It is provided with the blast pipe communicated with outer cold wind chamber and the VOC release pipelines connected with external hot air chamber；The air intake tube end is connected with
The second power Fan communicated with outside air.
5. VOC adsorbent equipment according to claim 3, it is characterised in that：The inner side plenum area bag
Include interior connector；Interior hot air cavity, interior cold wind chamber are offered between in the interior connector；The interior connector top both sides are also divided
The upper interface that the side interface communicated with interior cold wind chamber is communicated with the interior hot air cavity is not provided with；Band is connected with the upper interface
There is the second air supply duct of gas heater；The side interface is connected by blowpipe with second air supply duct；It is described
Outer cold wind chamber, interior cold wind chamber, interior hot air cavity, the circulation of external hot air chamber internal gas flow are communicated.
6. VOC adsorbent equipment according to claim 3, it is characterised in that：In outside ventilation
Seal construction area is equipped between area, inner side plenum area and the cylindric tower structure outer wall, inwall.
7. the VOC adsorbent equipment according to right wants 6, it is characterised in that：The seal construction area includes
Baffle plate, sealing flange and sealing aluminium block；Elastomer is provided between described sealing flange one end and the baffle plate；The sealing aluminium block
One end is connected with sealing flange, and the other end is in the arc shape structure matched with the cylindric tower structure outer wall, inwall.
8. processing equipment is discharged in the concentration of VOC according to claim 7 and separation, it is characterised in that：
Silica gel strip is equipped with the cylindric tower structure outer wall, inwall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710025041.XA CN106731468A (en) | 2017-01-13 | 2017-01-13 | A kind of VOC adsorbent equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710025041.XA CN106731468A (en) | 2017-01-13 | 2017-01-13 | A kind of VOC adsorbent equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106731468A true CN106731468A (en) | 2017-05-31 |
Family
ID=58945425
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710025041.XA Pending CN106731468A (en) | 2017-01-13 | 2017-01-13 | A kind of VOC adsorbent equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106731468A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6805845B1 (en) * | 1999-09-06 | 2004-10-19 | Taikisha Ltd. | Exhaust gas treatment system |
| CN201263955Y (en) * | 2008-07-29 | 2009-07-01 | 力技科技工程股份有限公司 | Structure for preventing gas leakage of zeolite turning wheel |
| JP2009262111A (en) * | 2008-04-30 | 2009-11-12 | Amano Corp | Voc gas treatment apparatus and filter cleaning method |
| JP2009291723A (en) * | 2008-06-05 | 2009-12-17 | Kanken Techno Co Ltd | Voc removing apparatus and voc removing method |
-
2017
- 2017-01-13 CN CN201710025041.XA patent/CN106731468A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6805845B1 (en) * | 1999-09-06 | 2004-10-19 | Taikisha Ltd. | Exhaust gas treatment system |
| JP2009262111A (en) * | 2008-04-30 | 2009-11-12 | Amano Corp | Voc gas treatment apparatus and filter cleaning method |
| JP2009291723A (en) * | 2008-06-05 | 2009-12-17 | Kanken Techno Co Ltd | Voc removing apparatus and voc removing method |
| CN201263955Y (en) * | 2008-07-29 | 2009-07-01 | 力技科技工程股份有限公司 | Structure for preventing gas leakage of zeolite turning wheel |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB02 | Change of applicant information | ||
| CB02 | Change of applicant information |
Address after: 215000 Jiangsu city of Suzhou province Taicang city Shaxi town Yue Wang Taiwan Science and Technology Innovation Industrial Park Applicant after: SUZHOU U-AIR ENVIRONMENTAL TECHNOLOGY CO.,LTD. Address before: 215000 Jiangsu city of Suzhou province Taicang city Shaxi town Yue Wang Taiwan Science and Technology Innovation Industrial Park Applicant before: SUZHOU U-AIR ENVIRONMENTAL TECHNOLOGY CO.,LTD. |
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| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170531 |