CN106215620A - Super large air quantity zeolite adsorption concentration systems - Google Patents
Super large air quantity zeolite adsorption concentration systems Download PDFInfo
- Publication number
- CN106215620A CN106215620A CN201610824273.7A CN201610824273A CN106215620A CN 106215620 A CN106215620 A CN 106215620A CN 201610824273 A CN201610824273 A CN 201610824273A CN 106215620 A CN106215620 A CN 106215620A
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- China
- Prior art keywords
- zeolite
- desorption
- airduct
- gas
- air
- 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
- 229910021536 Zeolite Inorganic materials 0.000 title claims abstract description 59
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title claims abstract description 59
- 239000010457 zeolite Substances 0.000 title claims abstract description 59
- 238000001179 sorption measurement Methods 0.000 title claims abstract description 16
- 238000003795 desorption Methods 0.000 claims abstract description 39
- 239000012855 volatile organic compound Substances 0.000 claims abstract description 21
- 238000009835 boiling Methods 0.000 claims description 3
- 239000004575 stone Substances 0.000 claims description 3
- 210000003437 trachea Anatomy 0.000 claims 1
- 238000010276 construction Methods 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 239000000463 material Substances 0.000 abstract description 4
- 239000007789 gas Substances 0.000 description 40
- 239000002912 waste gas Substances 0.000 description 10
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 206010028980 Neoplasm Diseases 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 201000011510 cancer Diseases 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005538 encapsulation Methods 0.000 description 1
- 208000032839 leukemia Diseases 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- GOLXNESZZPUPJE-UHFFFAOYSA-N spiromesifen Chemical compound CC1=CC(C)=CC(C)=C1C(C(O1)=O)=C(OC(=O)CC(C)(C)C)C11CCCC1 GOLXNESZZPUPJE-UHFFFAOYSA-N 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
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/106—Silica or silicates
- B01D2253/108—Zeolites
-
- 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
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)
- Separation Of Gases By Adsorption (AREA)
- Treating Waste Gases (AREA)
Abstract
Super large air quantity zeolite adsorption concentration systems, it relates to technical field of environment protection equipment；It comprises VOCs exhaust gas inlet, zeolite, desorption air airduct, air inlet, desorption gas airduct, concentrated gas exhaustor, concentrated gas outlet；The side of described zeolite is provided with VOCs exhaust gas inlet, and the opposite side of zeolite is provided with desorption gas airduct, and desorption gas airduct is fixing with desorption air airduct to be connected, and the upper end of desorption air airduct is provided with air inlet；The upper end of described zeolite is provided with concentrated gas exhaustor and concentrated gas outlet.Super large air quantity zeolite adsorption concentration systems of the present invention, can make separate unit zeolite runner reach 1,000,000 air quantity, it is not necessary to multiple stage is installed, and floor space is little, has saved manpower, material resources and financial resources, and the present invention has simple in construction, arranges the advantages such as reasonable, cost of manufacture is low.
Description
Technical field
The present invention relates to technical field of environment protection equipment, be specifically related to super large air quantity zeolite adsorption concentration systems.
Background technology
In industrial processes, can discharge a large amount of containing VOCs waste gas, be PM2.5 formation previous most important before
Body thing, if administering not in time, can aggravate PM2.5 concentration, more directly affecting the healthy of workman.Particularly in unguarded feelings
Under condition, in air of workplace, VOCs concentration is at a relatively high, very big to the body harm of workman, the most then occur that aplastic is lean
Blood is heavy then suffer from leukemia and cancer etc..
Processing mode at present: Adsorption Concentration, zeolite adsorption concentration systems single device can accomplish 150,000 air quantity, more than 150,000
The operating mode of air quantity, then need to install multiple stage zeolite adsorption concentration systems, and floor space is big, more consumes manpower, material resources and financial resources.
Summary of the invention
Present invention aims to defect and the deficiency of prior art, it is provided that a kind of simple in construction, reasonable in design, make
With convenient super large air quantity zeolite adsorption concentration systems.
For achieving the above object, the technical solution used in the present invention is: it comprises VOCs exhaust gas inlet, zeolite, solution are emptied
Gas airduct, air inlet, desorption gas airduct, concentrated gas exhaustor, concentrated gas export；The side of described zeolite is provided with
VOCs exhaust gas inlet, the opposite side of zeolite is provided with desorption gas airduct, and desorption gas airduct is fixing with desorption air airduct even
Connecing, the upper end of desorption air airduct is provided with air inlet；The upper end of described zeolite is provided with concentrated gas exhaustor, concentrated gas
The side of body exhaustor is provided with concentrated gas outlet.
As preferably, described exhaustor seals setting with the junction of zeolite.
As preferably, described zeolite is cylindrical structure, and desorption air airduct is arranged on the center of zeolite.
The operation principle of the present invention is: adsorption section: the waste gas containing low concentration VOCs enters boiling by VOCs exhaust gas inlet
Inside stone, the VOCs in waste gas is adsorbed by zeolite, and purified gas is immediately discharged in air；Desorption section: the solution of 180 DEG C
Suck enters zeolite inwall by the air inlet above zeolite, and now the VOCs in zeolite is desorbed out by hot-air, desorption
After high concentration VOCs waste gas discharged by concentrated gas outlet.The inside of described zeolite tightly isolates with outside,
It is mixed into original waste gas in gas after preventing from purifying；Described desorption air airduct is fixed as one with desorption gas airduct, at the uniform velocity
Rotate around cylindrical zeolite；Described concentrated gas exhaustor and concentrated gas outlet are fixed on above zeolite, carry out close
Envelope processes, and forbids desorption gas to leak；This kind of zeolite is fixed, is desorbed the design that district rotates, and separate unit zeolite runner can be made to reach 100
Ten thousand air quantity.
After using said structure, what the present invention produced has the beneficial effect that super large air quantity zeolite adsorption of the present invention is dense
Compression system, separate unit zeolite runner reaches 1,000,000 air quantity, it is not necessary to multiple stage is installed, and floor space is little, has saved manpower, material resources and financial resources,
The present invention has simple in construction, arranges the advantages such as reasonable, cost of manufacture is low.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
Description of reference numerals:
VOCs exhaust gas inlet 1, zeolite 2, desorption air airduct 3, air inlet 4, desorption gas airduct 5,
Concentrated gas exhaustor 6, concentrated gas outlet 7.
Detailed description of the invention
In order to be illustrated more clearly that the embodiment of the present invention or technical scheme of the prior art, below will be to embodiment or existing
In having technology to describe, the required accompanying drawing used is briefly described, it should be apparent that, the accompanying drawing in describing below is only this
Some embodiments of invention, for those of ordinary skill in the art, on the premise of not paying creative work, also may be used
To obtain other accompanying drawing according to these accompanying drawings.
Referring to as it is shown in figure 1, this detailed description of the invention adopts the following technical scheme that it comprises VOCs exhaust gas inlet 1, zeolite
2, desorption air airduct 3, air inlet 4, desorption gas airduct 5, concentrated gas exhaustor 6, concentrated gas outlet 7；Described boiling
The side of stone 2 is provided with VOCs exhaust gas inlet 1, and the opposite side of zeolite 2 is provided with desorption gas airduct 5, desorption gas airduct 5 with
Desorption air airduct 3 is fixing to be connected, and the upper end of desorption air airduct 3 is provided with air inlet 4；The upper end of described zeolite 2 is arranged
Concentrated gas exhaustor 6, the side of concentrated gas exhaustor 6 is had to be provided with concentrated gas outlet 7.
As preferably, described exhaustor 6 seals setting with the junction of zeolite 2.
As preferably, described zeolite 2 is cylindrical structure, and desorption air airduct 3 is arranged on the center of zeolite 2.
The operation principle of this detailed description of the invention is: adsorption section: the waste gas containing low concentration VOCs is entered by VOCs waste gas
It is internal that mouth 1 enters zeolite 2, and the VOCs in waste gas is adsorbed by zeolite, and purified gas is immediately discharged in air；Desorption
Section: the desorption air of 180 DEG C enters zeolite inwall by the air inlet 4 above zeolite 2, and now hot-air is by the VOCs in zeolite
Out, the high concentration VOCs waste gas after desorption is by concentrated gas outlet 7 discharge for desorption.The inside of described zeolite 2 is with outside
Tightly isolate, after preventing from purifying, in gas, be mixed into original waste gas；Described desorption air airduct 3 and desorption gas airduct 5
It is fixed as one, at the uniform velocity rotates around cylindrical zeolite 2；Described concentrated gas exhaustor 6 and concentrated gas outlet 7 are fixed
Above zeolite 2, carry out encapsulation process, forbid desorption gas to leak；This kind of zeolite is fixed, is desorbed the design that district rotates, and can make
Separate unit zeolite runner reaches 1,000,000 air quantity.
After using said structure, what this detailed description of the invention produced has the beneficial effect that surpassing described in this detailed description of the invention
Wind Volume zeolite adsorption concentration systems, separate unit zeolite runner reaches 1,000,000 air quantity, it is not necessary to multiple stage is installed, and floor space is little, saves
Manpower, material resources and financial resources, this detailed description of the invention have simple in construction, arrange rationally, the advantage such as cost of manufacture is low.
The ultimate principle of the present invention and principal character and advantages of the present invention have more than been shown and described.The skill of the industry
The art personnel simply explanation it should be appreciated that the present invention is not restricted to the described embodiments, described in above-described embodiment and description
The principle of the present invention, without departing from the spirit and scope of the present invention, the present invention also has various changes and modifications, these
Changes and improvements both fall within scope of the claimed invention.Claimed scope by appending claims and
Its equivalent defines.
Claims (3)
1. super large air quantity zeolite adsorption concentration systems, it is characterised in that: it comprises VOCs exhaust gas inlet, zeolite, desorption air wind
Pipe, air inlet, desorption gas airduct, concentrated gas exhaustor, concentrated gas export；The side of described zeolite is provided with VOCs
Exhaust gas inlet, the opposite side of zeolite is provided with desorption gas airduct, and desorption gas airduct is fixing with desorption air airduct to be connected, and solves
The upper end of suck airduct is provided with air inlet；The upper end of described zeolite is provided with concentrated gas exhaustor, and concentrated gas is arranged
The side of trachea is provided with concentrated gas outlet.
Super large air quantity zeolite adsorption concentration systems the most according to claim 1, it is characterised in that: described exhaustor and boiling
The junction of stone seals and arranges.
Super large air quantity zeolite adsorption concentration systems the most according to claim 1, it is characterised in that: described zeolite is cylinder
Body structure, and desorption air airduct is arranged on the center of zeolite.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610824273.7A CN106215620A (en) | 2016-08-30 | 2016-08-30 | Super large air quantity zeolite adsorption concentration systems |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610824273.7A CN106215620A (en) | 2016-08-30 | 2016-08-30 | Super large air quantity zeolite adsorption concentration systems |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106215620A true CN106215620A (en) | 2016-12-14 |
Family
ID=58075521
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610824273.7A Pending CN106215620A (en) | 2016-08-30 | 2016-08-30 | Super large air quantity zeolite adsorption concentration systems |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106215620A (en) |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002035529A (en) * | 2000-07-21 | 2002-02-05 | Seibu Giken Co Ltd | Gas concentration apparatus |
| JP2003010626A (en) * | 2001-06-29 | 2003-01-14 | Seibu Giken Co Ltd | Gas adsorption concentration device |
| JP2012166155A (en) * | 2011-02-15 | 2012-09-06 | Toyobo Co Ltd | Organic solvent recovery system |
| CN103990354A (en) * | 2014-05-29 | 2014-08-20 | 江苏兆年涂装科技有限公司 | Waste gas concentration device |
| CN204735113U (en) * | 2015-03-12 | 2015-11-04 | 杰智环境科技股份有限公司 | Indoor low concentration organic waste gas purifier |
| CN205351347U (en) * | 2015-10-14 | 2016-06-29 | 段志勇 | Novel portable concentrated catalytic combustion device |
| CN105749700A (en) * | 2016-04-08 | 2016-07-13 | 长春工业大学 | Novel continuous cylinder type volatile organic compound absorbing method |
| CN105854508A (en) * | 2016-04-20 | 2016-08-17 | 河北先河正源环境治理技术有限公司 | Combined type VOCs (Volatile Organic Chemicals) purification and recovery device |
| CN205461434U (en) * | 2016-03-09 | 2016-08-17 | 新昌县镜岭镇康柳电子元件厂 | Industrial waste gas treatment system |
| CN206138956U (en) * | 2016-08-30 | 2017-05-03 | 可迪尔空气技术（北京）有限公司 | Super large amount of wind zeolite adsorption concentration system |
-
2016
- 2016-08-30 CN CN201610824273.7A patent/CN106215620A/en active Pending
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002035529A (en) * | 2000-07-21 | 2002-02-05 | Seibu Giken Co Ltd | Gas concentration apparatus |
| JP2003010626A (en) * | 2001-06-29 | 2003-01-14 | Seibu Giken Co Ltd | Gas adsorption concentration device |
| JP2012166155A (en) * | 2011-02-15 | 2012-09-06 | Toyobo Co Ltd | Organic solvent recovery system |
| CN103990354A (en) * | 2014-05-29 | 2014-08-20 | 江苏兆年涂装科技有限公司 | Waste gas concentration device |
| CN204735113U (en) * | 2015-03-12 | 2015-11-04 | 杰智环境科技股份有限公司 | Indoor low concentration organic waste gas purifier |
| CN205351347U (en) * | 2015-10-14 | 2016-06-29 | 段志勇 | Novel portable concentrated catalytic combustion device |
| CN205461434U (en) * | 2016-03-09 | 2016-08-17 | 新昌县镜岭镇康柳电子元件厂 | Industrial waste gas treatment system |
| CN105749700A (en) * | 2016-04-08 | 2016-07-13 | 长春工业大学 | Novel continuous cylinder type volatile organic compound absorbing method |
| CN105854508A (en) * | 2016-04-20 | 2016-08-17 | 河北先河正源环境治理技术有限公司 | Combined type VOCs (Volatile Organic Chemicals) purification and recovery device |
| CN206138956U (en) * | 2016-08-30 | 2017-05-03 | 可迪尔空气技术（北京）有限公司 | Super large amount of wind zeolite adsorption concentration system |
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| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| DD01 | Delivery of document by public notice | ||
| DD01 | Delivery of document by public notice |
Addressee: CALIDADDELAIRE TECHNOLOGY (BEIJING) CO.,LTD. Person in charge of patents Document name: Notice of First Examination Opinion |
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| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20161214 |