CN201750983U - Absorption material fluidization rotary purifier - Google Patents
Absorption material fluidization rotary purifier Download PDFInfo
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- CN201750983U CN201750983U CN2010202151412U CN201020215141U CN201750983U CN 201750983 U CN201750983 U CN 201750983U CN 2010202151412 U CN2010202151412 U CN 2010202151412U CN 201020215141 U CN201020215141 U CN 201020215141U CN 201750983 U CN201750983 U CN 201750983U
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Abstract
The utility model relates to an absorption material fluidization rotary purifier which comprises a rotary body provided with a plurality of containing chambers filled with absorption material, a speed reducer used for driving the rotary body, and an absorption material filling unit that is provided with a discharge pipe and a feed pipe and leads the absorption material to be sent out through the discharge pipe and fed in through the feed pipe of the containing chambers of the rotary body. The utility model greatly improves the purification capability, has no problem of heat accumulation, and is not collocated with external desorption so as to improve the desorption efficiency.
Description
Technical field
The utility model relates to and a kind of the adsorption material fluidisation is transported to the design that the desorption program is carried out in the outside, relates in particular to a kind of adsorption material fluidisation Clothoid type clarifier that a revolution is separated into several accommodation chambers that are used for the filling adsorption material.
Background technology
Life with produce in the organic solvent highly volatile of extensive use become gas, so have another name called volatile organic matter (Volatile Organic Compounds, VOCs), but because of most VOCs have certain toxicity to human body, must be incinerated or be reclaimed, and incinerate or reclaimer before, can utilize clarifier earlier with the VOCs adsorption cleaning usually, desorption carries out follow-up incineration or recycling program again; Wherein, the Clothoid type clarifier of runner type or change type is common clarifier, and existing as shown in Figure 1 runner type Clothoid type clarifier 10 and as shown in Figure 2 change type Clothoid type clarifier 20, its structure kenel is to constitute in the solid substrate coating one deck adsorption material powder with gas channel, solid substrate is sintered into by pottery, glass or activated carbon fiber paper, the adsorption material kind is to look composition that desire handles gas and different, generally can adopt activated carbon or zeolite; So existing runner type or change type Clothoid type clarifier are to rotate (1～10RPH because of the drive of reductor (Geared motor, 30); Major part is 2～6RPH), and runner (or change) is positioned at the adsorption material of adsorption zone (11 or 21), is the absorption program of carrying out the phase I, and the VOCs in the waste gas is adsorbed under normal temperature, and purified gas directly is disposed to atmosphere; And along with the rotation of runner (or change), when the adsorption material behind the absorption VOCs goes to desorption district (12 or 22), promptly enter the desorption program of second stage, borrow hot-air from the desorption district VOCs desorption to be come out, the VOCs that desorption comes out then can carry out the incineration or the condensation recycling in another stage.
Secondly, because existing runner type or change type Clothoid type clarifier, because of its solid substrate does not have detergent power, and the actual adsorption material that possesses detergent power only accounts for below 30% of overall volume, causes the detergent power of unit volume limited; In addition, provide the adsorption material solid substrate that coating is adhered to, cause a large amount of heat storages easily, and then must shut down the problem that solves heat storage.
The utility model content
Technical problem underlying to be solved in the utility model is, overcome the limited problem of unit volume detergent power that prior art exists, and provide a kind of adsorption material fluidisation Clothoid type clarifier, can significantly promote detergent power, and have no heat storage problem and arrange in pairs or groups outside desorption and promote the effect of desorption efficient.
The technical scheme that its technical problem that solves the utility model adopts is:
A kind of adsorption material fluidisation Clothoid type clarifier is characterized in that, comprising: a revolution, the accommodation chamber with several filling adsorption material; One reductor drives this revolution; One adsorption material filling unit, this revolution is provided with discharge nozzle and feeding pipe relatively, and allows the accommodation chamber of this revolution send adsorption material and to send into adsorption material in this feeding pipe in this discharge nozzle.
Aforesaid adsorption material fluidisation Clothoid type clarifier, wherein revolution comprises runner type revolution and change type revolution.
Aforesaid adsorption material fluidisation Clothoid type clarifier, wherein the inner and outer rings mask of the left and right wheel side of runner type revolution and described change type revolution has the air-flow through hole.
Aforesaid adsorption material fluidisation Clothoid type clarifier, wherein runner type revolution and change type revolution are separated into several accommodation chambers with several dividing plates.
Aforesaid adsorption material fluidisation Clothoid type clarifier, wherein runner type revolution and change type revolution are synthetic with several accommodation chamber set of monomers.
Aforesaid adsorption material fluidisation Clothoid type clarifier, wherein adsorption material is directly made moulding by porous series materials such as activated carbon, zeolite, aluminium oxide or resins.
Aforesaid adsorption material fluidisation Clothoid type clarifier, wherein adsorption material comprises structure kenels such as graininess, spherical, ellipticity and column.
Aforesaid adsorption material fluidisation Clothoid type clarifier, wherein adsorption material filling unit is connected with the desorption device of outside.
The beneficial effects of the utility model are, can significantly promote detergent power, and have no heat storage problem and arrange in pairs or groups outside desorption and promote the effect of desorption efficient.
Description of drawings
Below in conjunction with drawings and Examples the utility model is further specified.
Fig. 1 is the structural representation of existing runner type Clothoid type clarifier.
Fig. 2 is the structural representation of existing change type Clothoid type clarifier.
Fig. 3 is the structural representation of the utility model first embodiment.
Fig. 4 is the structural representation of the utility model second embodiment.
Fig. 5 is the structural representation of the utility model the 3rd embodiment.
Fig. 6 is the structural representation of the utility model the 4th embodiment.
Fig. 7 is the schematic diagram of the utility model decontamination procedure.
The number in the figure explanation:
10 runner type Clothoid type clarifiers
20 change type Clothoid type clarifiers
11,21 adsorption zones
12,22 desorption districts
30 reductors
40a, 40b runner type revolution
41 dividing plates
42 accommodation chambers
43 accommodation chamber monomers
50 adsorption material
60 adsorption material filling unit
61 discharge nozzles
62 feeding pipes
70a, 70b change type revolution
71 dividing plates
72 accommodation chambers
73 accommodation chamber monomers
The specific embodiment
At first, see also shown in Figure 3, first embodiment of the present utility model, be that a runner type revolution 40a radially is provided with several dividing plates 41, and be separated into the accommodation chamber 42 of the movable adsorption material 50 of several fillings, and borrow a reductor 30 to drive this runner type revolution 40a, and make an adsorption material filling unit 60 relative this runner type revolution 40a be provided with discharge nozzle 61 and feeding pipe 62, cause the accommodation chamber 42 of this runner type revolution 40a to borrow this discharge nozzle 61 to send adsorption material 50 and send into adsorption material 50 by this feeding pipe 62.Yet this adsorption material filling unit 60 is connected with the desorption device of outside again, carries out the desorption program of adsorption material, but because of non-technology contents of the present utility model, does not repeat them here.This adsorption material 50 is directly made moulding by porous series materials such as activated carbon, zeolite, aluminium oxide or resins, and comprises structure kenels such as graininess, spherical, ellipticity and column.
Then, see also shown in Figure 4, second embodiment of the present utility model and first embodiment different be in: non-ly being separated out accommodation chamber with dividing plate, is that the accommodation chamber monomer 43 with several circular arrangement is combined into runner type revolution 40b.Person in addition, see also shown in Figure 5, the 3rd embodiment of the present utility model and first embodiment different be in: revolution is non-to be the runner type, for the change type revolution 70a that several dividing plates 71 are separated into several accommodation chambers 72 radially is set.Again, see also shown in Figure 6, the 4th embodiment of the present utility model and the 3rd embodiment different be in: non-ly being separated out accommodation chamber with dividing plate, is that the accommodation chamber monomer 73 with several annular array is combined into change type revolution 70b.Yet the inner and outer rings mask of the left and right wheel side of this runner type revolution 40a or 40b and this change type revolution 70a or 70b has the adsorption material of making 50 unlikely air-flow through holes that drop.
Based on said structure, structure kenel with first embodiment cooperates Fig. 7 that decontamination procedure is described again, among the figure runner type revolution 40a is separated into the accommodation chamber 42 of eight movable adsorption material 50 of filling, and the organic solvent waste gas pipeline can cover a side of the accommodation chamber 42 of six positions such as covering A, B, C, D, E, F, that is circle round so far that the accommodation chamber 42 of six positions is the adsorption zone that becomes organic solvent, the adsorption material 50 of adsorption zone inner filling can be with organic solvent absorption, and allow the air-flow by adsorption zone purify; Then, when accommodation chamber 42 circles round discharge zone to the G position, promptly borrow this discharge nozzle 61 to send inner adsorption material 50 of having adsorbed organic solvent, to carry out the desorption program of adsorption material 50; At last, when accommodation chamber 42 circles round material feeding region to the H position, promptly borrow this feeding pipe 62 to send into the adsorption material 50 of finishing the desorption program, prepare to carry out the organic solvent decontamination cycle of next absorption, discharging and pan feeding.
Hereat, because the adsorption zone area of the utility model and existing Clothoid type clarifier is suitable, but because of the adsorption material of existing Clothoid type clarifier only accounts for below 30% of overall volume, and adsorption material of the present utility model be by porous series materials such as activated carbon, zeolite, aluminium oxide or resin directly make moulding and the fluidisation filling in adsorption zone, cause detergent power can reach more than three times of prior art, and have the effect that significantly promotes detergent power.Again, the adsorption material that the utility model borrows adsorption material filling unit will finish the absorption program is transported to the outside and carries out the desorption program, and the used heat that the absorption program is produced can't be accumulated in revolution inside, has the effect of no heat storage problem and desorption improved efficiency.
The above, it only is preferred embodiment of the present utility model, be not that the utility model is done any pro forma restriction, every foundation technical spirit of the present utility model all still belongs in the scope of technical solutions of the utility model any simple modification, equivalent variations and modification that above embodiment did.
In sum, the utility model is on structural design, use practicality and cost benefit, it is required to meet industry development fully, and the structure that is disclosed also is to have unprecedented innovation structure, have novelty, creativeness, practicality, the regulation that meets relevant utility model patent important document is so mention application in accordance with the law.
Claims (8)
1. an adsorption material fluidisation Clothoid type clarifier is characterized in that, comprising:
One revolution, the accommodation chamber with several filling adsorption material;
One reductor drives this revolution;
One adsorption material filling unit, this revolution is provided with discharge nozzle and feeding pipe relatively, and allows the accommodation chamber of this revolution send adsorption material and to send into adsorption material in this feeding pipe in this discharge nozzle.
2. adsorption material fluidisation Clothoid type clarifier according to claim 1 is characterized in that described revolution comprises runner type revolution and change type revolution.
3. adsorption material fluidisation Clothoid type clarifier according to claim 2 is characterized in that the inner and outer rings mask of the left and right wheel side of described runner type revolution and described change type revolution has the air-flow through hole.
4. adsorption material fluidisation Clothoid type clarifier according to claim 3 is characterized in that described runner type revolution and change type revolution are separated into several accommodation chambers with several dividing plates.
5. adsorption material fluidisation Clothoid type clarifier according to claim 3 is characterized in that, described runner type revolution and change type revolution are synthetic with several accommodation chamber set of monomers.
6. according to each described adsorption material fluidisation Clothoid type clarifier in the claim 1 to 5, it is characterized in that described adsorption material is directly made moulding by activated carbon, zeolite, aluminium oxide or resin porous series material.
7. adsorption material fluidisation Clothoid type clarifier according to claim 6 is characterized in that, described adsorption material comprises graininess, spherical, ellipticity and column structure kenel.
8. adsorption material fluidisation Clothoid type clarifier according to claim 6 is characterized in that, described adsorption material filling unit is connected with the desorption device of outside.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202151412U CN201750983U (en) | 2010-06-04 | 2010-06-04 | Absorption material fluidization rotary purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202151412U CN201750983U (en) | 2010-06-04 | 2010-06-04 | Absorption material fluidization rotary purifier |
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| CN201750983U true CN201750983U (en) | 2011-02-23 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2010202151412U Expired - Fee Related CN201750983U (en) | 2010-06-04 | 2010-06-04 | Absorption material fluidization rotary purifier |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102266705A (en) * | 2010-06-04 | 2011-12-07 | 承杰有限公司 | Absorption material fluidizing convolution purifier |
| CN102580452A (en) * | 2012-02-23 | 2012-07-18 | 宁波市沧海新材料开发有限公司 | Indoor polluted air treatment instrument |
| CN103599676A (en) * | 2013-11-25 | 2014-02-26 | 青岛华世洁环保科技有限公司 | Absorption type rotating wheel gas purifying device |
| CN109589745A (en) * | 2018-10-22 | 2019-04-09 | 南京大学环境规划设计研究院股份公司 | Can on-line measurement VOCs concentration VOCs adsorption plant |
-
2010
- 2010-06-04 CN CN2010202151412U patent/CN201750983U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102266705A (en) * | 2010-06-04 | 2011-12-07 | 承杰有限公司 | Absorption material fluidizing convolution purifier |
| CN102580452A (en) * | 2012-02-23 | 2012-07-18 | 宁波市沧海新材料开发有限公司 | Indoor polluted air treatment instrument |
| CN103599676A (en) * | 2013-11-25 | 2014-02-26 | 青岛华世洁环保科技有限公司 | Absorption type rotating wheel gas purifying device |
| CN103599676B (en) * | 2013-11-25 | 2015-05-20 | 青岛华世洁环保科技有限公司 | Absorption type rotating wheel gas purifying device |
| CN109589745A (en) * | 2018-10-22 | 2019-04-09 | 南京大学环境规划设计研究院股份公司 | Can on-line measurement VOCs concentration VOCs adsorption plant |
| CN109589745B (en) * | 2018-10-22 | 2019-10-01 | 南京大学环境规划设计研究院股份公司 | Can on-line measurement VOCs concentration VOCs adsorption plant |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110223 Termination date: 20140604 |