CN206138956U - Super large amount of wind zeolite adsorption concentration system - Google Patents
Super large amount of wind zeolite adsorption concentration system Download PDFInfo
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- CN206138956U CN206138956U CN201621053525.2U CN201621053525U CN206138956U CN 206138956 U CN206138956 U CN 206138956U CN 201621053525 U CN201621053525 U CN 201621053525U CN 206138956 U CN206138956 U CN 206138956U
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Abstract
Super large amount of wind zeolite adsorption concentration system, it relates to environmental protection equipment technical field, it contains the import of VOCs waste gas, zeolite, desorption air tuber pipe, air intake, the gaseous tuber pipe of desorption, concentrated gaseous blast pipe, concentrated gas outlet, one side of zeolite be provided with the import of VOCs waste gas, the opposite side of zeolite is provided with the gaseous tuber pipe of desorption, gaseous tuber pipe of desorption and desorption air tuber pipe fixed connection, the upper end of desorption air tuber pipe is provided with the air intake, the upper end of zeolite be provided with concentrated gaseous blast pipe and concentrated gas outlet. Super large amount of wind zeolite adsorption concentration system, can make separate unit zeolite runner reach 1, 000, 000 amount of wind, need not many installations, area is little, has practiced thrift manpower, material resources and financial resources, the utility model has the advantages of simple structure, set up reasonable, the cost of manufacture low.
Description
Technical field
The present invention relates to technical field of environment protection equipment, and in particular to super large air quantity zeolite adsorption concentration systems.
Background technology
In industrial processes, can discharge in a large number containing VOCs waste gas, be PM2.5 formation it is previous most important before
Body thing, if administering not in time, can aggravate PM2.5 concentration, more directly affect the healthy of workman.Particularly in unguarded feelings
Under condition, VOCs concentration is at a relatively high in air of workplace, very big to the body harm of workman, aplastic gently then occurs lean
Blood is heavy then suffer from leukaemia and cancer etc..
Current processing mode：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.
The content of the invention
Present invention aims to the defect and deficiency of prior art, there is provided a kind of simple structure, it is 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 is emptied comprising VOCs exhaust gas inlets, zeolite, solution
Gas airduct, air inlet, desorption gas airduct, concentrated gas blast pipe, concentrated gas outlet；The side of described zeolite is provided with
VOCs exhaust gas inlets, the opposite side of zeolite is provided with desorption gas airduct, and desorption gas airduct is fixed with desorption air airduct and connected
Connect, the upper end of desorption air airduct is provided with air inlet；The upper end of described zeolite is provided with concentrated gas blast pipe, concentrated gas
The side of body blast pipe is provided with concentrated gas outlet.
Preferably, described blast pipe is arranged with the junction sealing of zeolite.
Preferably, described zeolite is cylindrical structure, and desorption air airduct is arranged on the center of zeolite.
The present invention operation principle be：Adsorption section：Waste gas containing low concentration VOCs enters boiling by VOCs exhaust gas inlets
Inside stone, zeolite adsorbs to the VOCs in waste gas, and purified gas is immediately discharged in air；Desorption section：180 DEG C of solution
Suck enters zeolite inwall by the air inlet above zeolite, and now the VOCs in zeolite is desorbed out by hot-air, is desorbed
High concentration VOCs waste gas afterwards is discharged by concentrated gas outlet.The inside of described zeolite is tightly isolated with outside,
Prevent from being mixed into original waste gas in gas after purification；Described desorption air airduct is fixed as one with desorption gas airduct, at the uniform velocity
Zeolite around cylinder is rotated；Described concentrated gas blast pipe and concentrated gas outlet is fixed on zeolite top, carries out close
Envelope process, forbids desorption gas to leak；The design of area's rotation is fixed, be desorbed to this kind of zeolite, and separate unit zeolite runner can be made to reach 100
Ten thousand air quantity.
After said structure, what the present invention was 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, installs without the need for multiple stage, and floor space is little, has saved manpower, material resources and financial resources,
The present invention has the advantages that simple structure, arranges reasonable, low manufacture cost.
Description of the drawings
Fig. 1 is the structural representation of the present invention.
Description of reference numerals：
VOCs exhaust gas inlets 1, zeolite 2, desorption air airduct 3, air inlet 4, the exhaust of desorption gas airduct 5, concentrated gas
Pipe 6, concentrated gas outlet 7.
Specific embodiment
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
The accompanying drawing to be used needed for having technology description is briefly described, it should be apparent that, drawings in the following description are only this
Some embodiments of invention, for those of ordinary skill in the art, without having to pay creative labor, may be used also
To obtain other accompanying drawings according to these accompanying drawings.
Referring to as shown in figure 1, this specific embodiment is adopted the following technical scheme that：It includes VOCs exhaust gas inlets 1, zeolite
2nd, desorption air airduct 3, air inlet 4, desorption gas airduct 5, concentrated gas blast pipe 6, concentrated gas outlet 7；Described boiling
The side of stone 2 is provided with VOCs exhaust gas inlets 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 fixedly 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
The side for having concentrated gas blast pipe 6, concentrated gas blast pipe 6 is provided with concentrated gas outlet 7.
Preferably, described blast pipe 6 is arranged with the junction sealing of zeolite 2.
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 specific embodiment is：Adsorption section：Waste gas containing low concentration VOCs is entered by VOCs waste gas
Mouth 1 is entered inside zeolite 2, and zeolite adsorbs to the VOCs in waste gas, and purified gas is immediately discharged in air；Desorption
Section：180 DEG C of desorption air enters zeolite inwall by the air inlet 4 of the top of zeolite 2, and now hot-air is by the VOCs in zeolite
Desorption out, by concentrated gas outlet 7 discharged by the high concentration VOCs waste gas after desorption.The inside of described zeolite 2 and outside
Tightly isolated, prevent from being mixed into original waste gas in gas after purification；Described desorption air airduct 3 and desorption gas airduct 5
It is fixed as one, at the uniform velocity the zeolite 2 around cylinder is rotated；Described concentrated gas blast pipe 6 and concentrated gas outlet 7 is fixed
In the top of zeolite 2, encapsulation process is carried out, forbid desorption gas to leak；The design of area's rotation is fixed, be desorbed to this kind of zeolite, can make
Separate unit zeolite runner reaches 1,000,000 air quantity.
After said structure, what this specific embodiment was produced has the beneficial effect that：It is super described in this specific embodiment
Wind Volume zeolite adsorption concentration systems, separate unit zeolite runner reaches 1,000,000 air quantity, installs without the need for multiple stage, and floor space is little, saves
Manpower, material resources and financial resources, this specific embodiment have the advantages that simple structure, arrange rationally, low manufacture cost.
The general principle and principal character and advantages of the present invention of the present invention has been shown and described above.The skill of the industry
Simply explanation of the art personnel it should be appreciated that the present invention is not restricted to the described embodiments, described in above-described embodiment and specification
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 are both fallen within scope of the claimed invention.The claimed scope of the invention by appending claims and
Its equivalent thereof.
Claims (3)
1. super large air quantity zeolite adsorption concentration systems, it is characterised in that：It includes VOCs exhaust gas inlets, zeolite, desorption air wind
Pipe, air inlet, desorption gas airduct, concentrated gas blast pipe, concentrated gas outlet；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 fixedly connected with desorption air airduct, solution
The upper end of suck airduct is provided with air inlet；The upper end of described zeolite is provided with concentrated gas blast pipe, concentrated gas row
The side of tracheae is provided with concentrated gas outlet.
2. super large air quantity zeolite adsorption concentration systems according to claim 1, it is characterised in that：Described blast pipe and boiling
The junction sealing of stone is arranged.
3. super large air quantity zeolite adsorption concentration systems 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 |
|---|---|---|---|
| CN201621053525.2U CN206138956U (en) | 2016-08-30 | 2016-08-30 | Super large amount of wind zeolite adsorption concentration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621053525.2U CN206138956U (en) | 2016-08-30 | 2016-08-30 | Super large amount of wind zeolite adsorption concentration system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206138956U true CN206138956U (en) | 2017-05-03 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621053525.2U Active CN206138956U (en) | 2016-08-30 | 2016-08-30 | Super large amount of wind zeolite adsorption concentration system |
Country Status (1)
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| CN (1) | CN206138956U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106215620A (en) * | 2016-08-30 | 2016-12-14 | 可迪尔空气技术（北京）有限公司 | Super large air quantity zeolite adsorption concentration systems |
-
2016
- 2016-08-30 CN CN201621053525.2U patent/CN206138956U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106215620A (en) * | 2016-08-30 | 2016-12-14 | 可迪尔空气技术（北京）有限公司 | Super large air quantity zeolite adsorption concentration systems |
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