CN202823093U - Exhaust gas purifier - Google Patents
Exhaust gas purifier Download PDFInfo
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- CN202823093U CN202823093U CN 201220360899 CN201220360899U CN202823093U CN 202823093 U CN202823093 U CN 202823093U CN 201220360899 CN201220360899 CN 201220360899 CN 201220360899 U CN201220360899 U CN 201220360899U CN 202823093 U CN202823093 U CN 202823093U
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- absorber
- air inlet
- shell body
- adsorbent
- cavity
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Abstract
The utility model discloses an exhaust gas purifier which comprises an outer shell body (1), an absorber (2), an air inlet cavity or an air outlet cavity (5), an air inlet or an air outlet (3), an air outlet cavity or an air inlet cavity (6) and an air outlet or an air inlet (4), wherein the absorber (2) is arranged in the outer shell body (1), micro holes used for air admission or air exhaust are formed in the surface of the absorber (2), the upper end and the lower end are respectively connected with the outer shell body (1) in a sealing mode, the air inlet cavity or the air outlet cavity (5) is defined by the front portion of the outer shell body (1) and the absorber (2), the air inlet or the air outlet (3) is communicated with the air inlet cavity or the air outlet cavity (5), the air outlet cavity or the air inlet cavity (6) is defined by the back portion of the outer shell body (1) and the absorber (2), and the an air outlet or the air inlet (4) is communicated with the air outlet cavity or the air inlet cavity (6). The exhaust gas purifier has the advantages of being high in absorption rate, without environmental restriction and secondary pollution, favorable for replacement of adsorbent, low in operation cost and widely applied to exhaust gas treatment in industries such as paper product, electron, machinery and metallurgy.
Description
Technical field
The utility model relates to a kind of clarifier, particularly relates to a kind of catalytic converter.
Background technology
Conduct page or leaf made of paper generally all can cause a lot of industrial waste gases, waste water, and the utility model produces the purification scheme of waste gas mainly for paper product industries.
Compare with traditional plate column, packed tower has the advantages such as production capacity is large, structure is simple, separative efficiency is high, pressure drop is little, operating flexibility is large, liquid holdup is little, thereby extensive use.
Yet, in traditional packed tower, when liquid flows downward along packing layer, the trend of concentrating to the tower wall is gradually arranged, so that near the flow quantity the tower wall increases gradually, this wall stream effect causes gas-liquid two-phase skewness in packing layer, thereby mass-transfer efficiency is descended, and absorption efficiency reduces; And, when liquid load wetting filling surface hour effectively, mass-transfer efficiency is reduced; In addition, also there is problems such as to carry out after-treatment to absorption liquid.
The utility model content
Primary and foremost purpose of the present utility model is to provide the catalytic converter that a kind of absorptivity is high, be not subjected to environmental limitations, do not have secondary pollution, have wide range of applications for the problem that above-mentioned prior art exists.Purification efficiency of the present utility model is high, adsorbent is changed conveniently, operating cost is low.
In order to achieve the above object, the utility model provides a kind of catalytic converter on the one hand, comprising:
Shell body;
Be installed in the absorber in the described shell body, the micropore that its surface has air inlet or gives vent to anger, its top and bottom are tightly connected with described shell body respectively;
By anterior inlet chamber or the outlet chamber that surrounds with described absorber of described shell body;
The air inlet or the gas outlet that are communicated with described inlet chamber or outlet chamber;
The outlet chamber or the inlet chamber that are surrounded by described shell body rear portion and described absorber;
The gas outlet or the air inlet that are communicated with described outlet chamber or inlet chamber.
Wherein, in the described absorber adsorbent is housed.
Particularly, described adsorbent contains alkaline matter, is used for absorption also and the property composition in the waste gas.
Absorber among embodiment of the utility model is hollow cylinder, and adsorbent is equipped with at the hollow position place of described hollow cylinder.
Absorber among another embodiment of the utility model is sleeve body, and it comprises the hollow outer cylinder body that the hollow inner cylinder body is outer with being enclosed within described inner barrel, and the part between described inner barrel and the outer cylinder body is equipped with adsorbent.
Wherein, described micropore is positioned at the surface of described hollow inner cylinder body and described hollow outer cylinder body.
Particularly, described absorber also comprises: be used for adding the charging aperture of adsorbent and the discharging opening that is used for discharging adsorbent.
Wherein, described air inlet or gas outlet are arranged on a side of described shell body, and described gas outlet or air inlet are arranged on the opposite side of described shell body.
Catalytic converter of the present utility model also comprises: the blower fan that is connected with air inlet or gas outlet by pipeline.
Particularly, described blower fan is Middle pressure draught fan.
Catalytic converter of the present utility model compared with prior art, have absorption efficiency high, be not subjected to environmental limitations, do not have secondary pollution, adsorbent changes the advantages such as convenient, that operating cost is low, can be widely used in the industries such as electronics, machinery, metallurgy, be used for administering the waste gas that contains that contains nitre, sulphur, salt, hydrogen fluorine, phosphorus, boron etc.
Description of drawings
Fig. 1 is the partial sectional view of the catalytic converter of an embodiment of the utility model;
Fig. 2 is the top view of the catalytic converter of an embodiment of the utility model;
Fig. 3 is the partial sectional view of the catalytic converter of another embodiment of the utility model;
Fig. 4 is the top view of the catalytic converter of another embodiment of the utility model.
The specific embodiment
Below in conjunction with accompanying drawing catalytic converter of the present utility model is conducted further description.
Fig. 1 and Fig. 2 are respectively partial sectional view and the top views of the catalytic converter of an embodiment of the utility model.
As shown in Figure 1 and Figure 2, catalytic converter of the present utility model comprises shell body 1 and is installed in absorber 2 in the described shell body 1, the micropore that the surface of absorber 2 has air inlet or gives vent to anger can make to contain waste gas and free in and out absorber through the absorber purified gas.Adsorbent 9 is housed in the absorber 2, contains alkaline matter in the described adsorbent 9, be used for absorption also and the property composition in the waste gas, waste gas is purified, thereby reaches discharge standard.Absorber 2 of the present utility model need not absorption liquid is carried out after-treatment, and adsorption efficiency is high.
The top and bottom of absorber 2 are tightly connected with shell body 1 respectively, and the front portion of shell body 1 and absorber 2 surround inlet chamber or outlet chamber 5, and the rear portion of shell body 1 and absorber 2 surround outlet chamber or inlet chamber 6.Side at shell body 1 is provided with air inlet or the gas outlet 3 that is communicated with inlet chamber or outlet chamber 5, is provided with gas outlet or the air inlet 4 of connection outlet chamber or inlet chamber 6 at the opposite side of shell body 1.
As shown in Figure 1, 2, absorber 2 can be hollow cylinder, and adsorbent 9 is contained in the hollow position place of hollow cylinder.After containing waste gas and entering into inlet chamber by air inlet, flow into the absorber from the micropore on absorber 2 surfaces, adsorbent absorption in the absorber and neutralization contain the property material in the waste gas, and the gas after purified treatment flow into outlet chamber from the micropore on absorber surface, then flows out through the gas outlet.
Fig. 3 and Fig. 4 are respectively partial sectional view and the top views of the catalytic converter of another embodiment of the utility model.
Shown in Fig. 3,4, absorber 2 is sleeve body, and it comprises the hollow outer cylinder body 11 that hollow inner cylinder body 10 is outer with being enclosed within described inner barrel, and the part between described inner barrel and the outer cylinder body is equipped with adsorbent 9.Described air inlet or the micropore of giving vent to anger are positioned at the surface of hollow inner cylinder body 10 and described hollow outer cylinder body 11.After containing waste gas and entering into inlet chamber by air inlet, flow into the absorber from the micropore on hollow outer cylinder body surface, adsorbent absorption in the absorber and neutralization contain the property material in the waste gas, after purified treatment, contain waste gas flow into the hollow inner cylinder body from the micropore on hollow inner barrel surface hollow space, and then re-inject through the micropore of hollow inner cylinder surface and to carry out further purified treatment in the absorber, micropore from hollow outer cylinder body surface flow into outlet chamber at last, flows out through the gas outlet again.
Catalytic converter of the present utility model can also comprise the blower fan that is connected with air inlet or gas outlet by pipeline, such as Middle pressure draught fan.Described blower fan is used for waste gas being sent into absorber 2 or purified gas being extracted out from absorber 2, and the pressure that it can improve waste gas in the inlet chamber makes waste gas can enter smoothly absorber 2.
Catalytic converter of the present utility model do not adopt in traditional absorption liquid and waste gas in the property material, thereby the mass-transfer efficiency of effectively having avoided wall stream effect to cause descends and the defective such as absorption efficiency reduction; Need not in addition absorption liquid is carried out after-treatment, technological operation is easier, absorptivity is higher, and be not subjected to environmental limitations, that non-secondary pollution, adsorbent are changed is convenient, operating cost is low, can be widely used in the waste gas pollution control and treatment of the industries such as paper products, electronics, machinery, metallurgy.
Above-mentioned embodiment only is exemplary, scope of the present utility model is not consisted of any restriction.It will be understood by those skilled in the art that and do not departing under the spirit and scope of the present utility model and can make amendment or replace the details of technical solutions of the utility model and form, but these modifications and replacing all fall in the protection domain of the present utility model.
Claims (6)
1. a catalytic converter is characterized in that, comprising:
Shell body (1);
Be installed in the absorber (2) in the described shell body (1), the micropore that its surface has air inlet or gives vent to anger, its top and bottom are tightly connected with described shell body (1) respectively;
By anterior inlet chamber or the outlet chamber (5) that surrounds with described absorber (2) of described shell body (1);
The air inlet or gas outlet (3) that are communicated with described inlet chamber or outlet chamber (5);
The outlet chamber or the inlet chamber (6) that are surrounded by described shell body (1) rear portion and described absorber (2);
The gas outlet or the air inlet (4) that are communicated with described outlet chamber or inlet chamber (6).
2. catalytic converter as claimed in claim 1 is characterized in that, adsorbent (9) is housed in the described absorber (2).
3. catalytic converter as claimed in claim 1 or 2 is characterized in that, described absorber (2) is hollow cylinder, and adsorbent (9) is equipped with at the hollow position place of described hollow cylinder.
4. catalytic converter as claimed in claim 1 or 2, it is characterized in that, described absorber (2) is sleeve body, it comprises hollow inner cylinder body (10) and is enclosed within the outer hollow outer cylinder body (11) of described inner barrel, and the part between described inner barrel and the outer cylinder body is equipped with adsorbent (9).
5. catalytic converter as claimed in claim 4 is characterized in that, described micropore is positioned at the surface of described hollow inner cylinder body (10) and described hollow outer cylinder body (11).
6. catalytic converter as claimed in claim 1 or 2 is characterized in that, described absorber (2) also comprises:
Be used for adding the charging aperture (7) of adsorbent; And
Be used for discharging the discharging opening (8) of adsorbent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220360899 CN202823093U (en) | 2012-07-25 | 2012-07-25 | Exhaust gas purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220360899 CN202823093U (en) | 2012-07-25 | 2012-07-25 | Exhaust gas purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202823093U true CN202823093U (en) | 2013-03-27 |
Family
ID=47934894
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220360899 Expired - Fee Related CN202823093U (en) | 2012-07-25 | 2012-07-25 | Exhaust gas purifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202823093U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103272459A (en) * | 2013-06-20 | 2013-09-04 | 苏州新区枫桥净化设备厂 | Assembling purifying tower |
| CN106064842A (en) * | 2016-08-04 | 2016-11-02 | 东华大学 | Waste water from dyestuff pollutant adsorbent equipment and using method thereof |
| WO2017166838A1 (en) * | 2016-03-31 | 2017-10-05 | 威格气体纯化科技（苏州）股份有限公司 | Glove case and purification column for online replacement of adsorbent material |
-
2012
- 2012-07-25 CN CN 201220360899 patent/CN202823093U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103272459A (en) * | 2013-06-20 | 2013-09-04 | 苏州新区枫桥净化设备厂 | Assembling purifying tower |
| CN103272459B (en) * | 2013-06-20 | 2015-04-01 | 太仓云联信息科技有限公司 | Assembling purifying tower |
| WO2017166838A1 (en) * | 2016-03-31 | 2017-10-05 | 威格气体纯化科技（苏州）股份有限公司 | Glove case and purification column for online replacement of adsorbent material |
| US10933365B2 (en) | 2016-03-31 | 2021-03-02 | Vigor Gas Purification Technologies, Inc. | Decontaminating column for on-line replacing adsorption material and glove box |
| CN106064842A (en) * | 2016-08-04 | 2016-11-02 | 东华大学 | Waste water from dyestuff pollutant adsorbent equipment and using method thereof |
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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: 20130327 Termination date: 20130725 |