CN2334481Y - Organic waste gas purifing equipment - Google Patents
Organic waste gas purifing equipment Download PDFInfo
- Publication number
- CN2334481Y CN2334481Y CN 97216725 CN97216725U CN2334481Y CN 2334481 Y CN2334481 Y CN 2334481Y CN 97216725 CN97216725 CN 97216725 CN 97216725 U CN97216725 U CN 97216725U CN 2334481 Y CN2334481 Y CN 2334481Y
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- bed
- air
- organic waste
- waste gas
- charcoal
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- 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.)
- Expired - Fee Related
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Abstract
The utility model relates to organic waste gas purifying equipment for treating industrial organic waste gas, which is especially suitable for treating the organic waste gas of low concentration and big air volume. The organic waste gas purifying equipment overcomes the disadvantages of similar type equipment. The organic waste gas purifying equipment has reasonable length width ratio, and is additionally matched with a conic airflow distributor with holes. The conic airflow distributor with holes enables gas flow to be evenly distributed on a cross section. The organic waste gas purifying equipment solves the question that the periphery of a bed body and a charcoal layer can not be sealed together. The peripheral edges of front and rear net plates are additionally provided with fixing side frames for overcoming border effect. The charcoal layer is designed into an integral type fixing bed, and any steel is not arranged in the charcoal layer. The filling of the charcoal layer adopts longitudinal and transversal double displacing arrangement, which overcomes a leak short-circuit phenomenon.
Description
The utility model relates to a kind of cleaning equipment of organic exhaust gas.Be used for the improvement of industrial organic exhaust gas, be particularly useful for the improvement of organic exhaust gas under the big air quantity of low concentration.
The cleaning equipment of domestic organic exhaust gas of the same type is a filling material with the honeycomb block shaped activated carbon at present, and its charcoal layer adopts assembling (drawer) formula structure, but exists following major defect:
1, long (height H on the equipment air-flow front) wide (the width b in equipment air-flow front) of bed influences air-flow and evenly distributes on the bed cross section, thereby reduced the equipment effective rate of utilization than excessive (being about 2).
2, because bed is assembling (drawer) formula structure, form by many movably drawer type lectulum layers in the bed, just on drawer frames and its moving track, formed crack inevitably, caused serious boundary effect, thereby reduced the purifying rate of equipment;
3, since in the bed many little drawer frames adopt the weldering of stuffiness iron straps to make, retaining has removed the front portion passage, this has not only increased bed resistance, face and also reduced the effective rate of utilization of sorbing material in the bed;
4, because little drawer frames and its track that is complementary in the bed are made by steel, not only increased the weight and the processing charges of adsorbent bed, and relatively reduced the gas defence ability.
The purpose of this utility model provides a kind of cleaning equipment of improved organic exhaust gas, can overcome crack short circuit phenomenon and serious boundary effect in the bed; Improve air-flow distribution in the bed; Improve the effective filtration area of bed.
The purpose of this utility model is achieved in that the cleaning equipment that a kind of organic exhaust gas promptly is provided, and it comprises airscoop shroud, adsorbent bed body and air leaving cover, the two ends of adsorbent bed body respectively with airscoop shroud and giving vent to anger.Cover connects with flange screw.A conical air-flow distributor that has several uniform small sircle holes is arranged in airscoop shroud, between airscoop shroud and circular cone air-flow distributor, be welded in the outside of the inboard and circular cone air-flow distributor of airscoop shroud respectively in two ends separately with some uniform poles, the honeycomb block shaped activated carbon filling layer of arranging by the two dislocation of vertical, horizontal (claiming charcoal layer and bed again) is housed in the adsorbent bed body, two ends at the charcoal layer are fixed with the front and back web plate respectively promptly, web plate comprises frame and wire netting, and frame can be used angle steel.Wire netting between placed in the middle and one side of frame are fixedly connected, and another periphery of frame is fixed on the body with screw.
The cleaning equipment of the organic exhaust gas that the utility model proposes has rational length-width ratio, and generally being controlled at 1~1.3 is ab=1~1.3; Other increases and joins a conical air-flow distributor with some holes (can uniform 12 apertures at the conical surface), and air-flow is evenly distributed on equipment; Equipment sectional area A1=H * b and conical bottom area A 2=Π O
2/ 4 ratio is 5~6, i.e. A1/A2=5~6.To overcome serious boundary effect and bed crack phenomenon, increase the flatness and the rigidity of bed body, charcoal layer contact-making surface is close on the body periphery.If little crack is arranged with fillings such as other material such as asbestos cords, the charcoal layer adopts the two dislocation of vertical and horizontal to arrange when filling charcoal piece in addition, to overcome the crack short circuit phenomenon that forms in the charcoal layer, if there is crack to adopt little charcoal piece to fill up, to improve the gas defence performance of equipment; Filling layer of the present utility model is an overall fixed formula bed, no any steel in the bed.
In sum, the cleaning equipment of the organic exhaust gas that the utility model proposes can solve the distribution of air flow problem of non-uniform, overcome serious boundary effect and bed crack short circuit phenomenon, the filling layer is the overall fixed layer, wherein there are not any steel, improved effective area, the overall performance level of equipment is increased, at first increased substantially the gas defence ability, more than 30%, reduce concentration of emission according to height drug abuse total capacity, alleviated weight, reduce cost, had tangible economic benefit and social benefit.
The utility model comprises the following drawings;
Fig. 1 is the front view of the utility model cleaning equipment;
Fig. 2 is the vertical view of the utility model cleaning equipment;
Fig. 3 is the A-A cutaway view of Fig. 1;
Fig. 4 connects partial enlarged drawing for web plate;
Fig. 5 is that 8 to arrange first row to the two dislocation of charcoal layer be odd number row schematic diagram;
Fig. 6 is that 8 to arrange second row to the two dislocation of charcoal layer be even numbers row schematic diagram;
The organic waste-gas purification equipment that the utility model proposes referring to Fig. 1~6 comprises airscoop shroud 1, adsorbent bed body 4 and air leaving cover 6, the two ends of adsorbent bed body 4 are connected with air leaving cover 6 usefulness flange screws with airscoop shroud 1 respectively, in airscoop shroud 1, be provided with a conical air-flow distributor 2 that has some uniform small sircle holes, circular cone air-flow distributor 2 is connected on the airscoop shroud 1 by three uniform poles, the two ends that are pole are welded in the inboard of airscoop shroud 1 and the outside of circular cone air-flow distributor respectively, be equipped with by vertical adsorbent bed body 4 inboards, the honeycomb block shaped activated carbon filling layer 7 that laterally two dislocation are arranged (claims charcoal layer or bed again, structural representation is seen Fig. 5, Fig. 6, two dislocation are arranged promptly, and first row adopts the complete arrangement of monoblock charcoal to see Fig. 5, second horizontal row is to 1/3 or 1/4 block of charcoal of dislocation, vertically go up the arrangement of 1/3 or 1/4 block of charcoal of dislocation and see Fig. 6, odd number row is again that Fig. 5 is seen in normal monoblock charcoal arrangement later on, even numbers row is vertical, Fig. 6 is seen in 1/3 or 1/4 arrangement that respectively misplaces again on horizontal, arranges until bed and finishes.Front and back at this filling layer 7 are fixed with preceding web plate 3 and after otter board 5 respectively, web plate is made of wire netting 3-2 and frame 3-1 before said, said frame 3-1 can be with 20 * 20 * 3 angle steel, one side of frame 3-1 is fixing with the wire netting welding, and the another side of frame is screwed on the bed body.The structure of after otter board 5 is identical with above-mentioned preceding web plate 3.
The high H of adsorbent bed body 4 is 1~1.3 with the ratio of wide b, and the sectional area H * b of bed body is about 5~6 with the ratio of conical air-flow distributor floor space, so that airflow uniform distribution is on the cross section.
Organic exhaust gas to be clean enters from airscoop shroud 1, and through conical air-flow distributor 2, equally distributed then air-flow enters honeycomb block shaped activated carbon layer 7 through preceding web plate 3, and purified gas enters through after otter board 5 and enters atmosphere after air leaving cover 6 converges.
The circular cone lateral area of said conical air-flow distributor 2 with its on the ratio of the gross area of uniform several apertures be about about 15.
The bed body adopts all-in-one-piece fixed bed, and the periphery and the charcoal layer periphery of bed body fit tightly, and have small gap can use other material again, for example with fillings such as asbestos cords, thereby overcome boundary effect.
Though described the utility model in conjunction with the embodiments, these are described and only to be used for explanation rather than to restriction of the present utility model.Under the condition that does not break away from protection scope of the present invention and design, those skilled in the art can make various distortion and application.
Claims (5)
1, a kind of cleaning equipment of organic exhaust gas, it comprises airscoop shroud, adsorbent bed body and air leaving cover, bed body two ends connect with airscoop shroud and air leaving cover respectively, in the adsorbent bed body, active carbon layer is housed, it is characterized in that in airscoop shroud, being equipped with a conical air-flow distributor that has some uniform small sircle holes, weld fixing respectively in two ends separately with some uniform poles on it between airscoop shroud and circular cone air-flow distributor; The honeycomb block shaped activated carbon layer of arranging by the two dislocation of vertical, horizontal is housed in the adsorbent bed body, two ends at the charcoal layer are fixed with the front and back web plate respectively promptly, web plate comprises wire netting and frame, frame adopts angle steel, one side of frame is fixing with wire netting placed in the middle welding, and another periphery of frame is screwed respectively on the bed body.
2, according to the cleaning equipment of the organic exhaust gas of claim 1, it is characterized in that a body adopts rational length-width ratio, be width (b) on height (H) and the equipment air-flow front on the equipment air-flow front than being 1~1.2, promptly (H * b) is (∏ O with conical air-flow distributor floor space A2 to the long-pending A1 of bed body section
2/ 4) ratio of (0 is the conical base diameter) is 5~6, and a body section overdraught is evenly distributed.
3, according to the organic waste-gas purification equipment of claim 1, it is characterized in that bed is all-in-one-piece fixed bed, bed body periphery fits tightly with charcoal layer periphery, have again little crack place in addition with other material as with fillings such as asbestos cords to overcome boundary effect.
4, according to the cleaning equipment of the organic exhaust gas of claim 1, the quantity that it is characterized in that some small sircle holes of conical air-flow distributor is 12, air-flow is evenly distributed, and the ratio of its circular cone lateral area A3 and 12 small sircle hole gross area A4 is about 15 to be that A3/A4 is about 15.
5, according to the cleaning equipment of the organic exhaust gas of claim 1, it is characterized in that the charcoal piece is arranged vertical, the horizontal two dislocation arrangement architectures of employing to overcome crack short circuit phenomenon in the bed in the bed, the i.e. complete arrangement of first cross section employing monoblock charcoal is arranged in two dislocation, second horizontal row is to dislocation 1/3 or 1/4 charcoal piece, vertically go up the arrangement of dislocation 1/3 or 1/4 charcoal piece, odd number row is again that normal monoblock charcoal is arranged later on, and 1/3 or 1/4 arrangement that respectively misplaces again on even numbers row is longitudinal and transverse is arranged until bed and finished.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 97216725 CN2334481Y (en) | 1997-06-09 | 1997-06-09 | Organic waste gas purifing equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 97216725 CN2334481Y (en) | 1997-06-09 | 1997-06-09 | Organic waste gas purifing equipment |
Publications (1)
Publication Number | Publication Date |
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CN2334481Y true CN2334481Y (en) | 1999-08-25 |
Family
ID=33933553
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 97216725 Expired - Fee Related CN2334481Y (en) | 1997-06-09 | 1997-06-09 | Organic waste gas purifing equipment |
Country Status (1)
Country | Link |
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CN (1) | CN2334481Y (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101073737B (en) * | 2006-05-19 | 2010-12-22 | 陈志强 | Pneumatic distributor for adsorptive tower |
CN101934193A (en) * | 2010-10-09 | 2011-01-05 | 郭继中 | Waste gas purification device |
CN102188876A (en) * | 2011-03-25 | 2011-09-21 | 天津赛智科技发展有限公司 | High-efficiency energy-saving adsorption system for industrial volatile organic pollutants |
CN102397738A (en) * | 2011-11-08 | 2012-04-04 | 杭州中泰深冷技术股份有限公司 | Vertical bed adsorber |
CN102814100A (en) * | 2011-06-07 | 2012-12-12 | 东洋纺织株式会社 | Gas adsorption unit device |
CN104874206A (en) * | 2015-05-28 | 2015-09-02 | 江苏瑞吉格泰油气工程有限公司 | Separator tube bundle rotational flow inlet device |
-
1997
- 1997-06-09 CN CN 97216725 patent/CN2334481Y/en not_active Expired - Fee Related
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101073737B (en) * | 2006-05-19 | 2010-12-22 | 陈志强 | Pneumatic distributor for adsorptive tower |
CN101934193A (en) * | 2010-10-09 | 2011-01-05 | 郭继中 | Waste gas purification device |
CN102188876A (en) * | 2011-03-25 | 2011-09-21 | 天津赛智科技发展有限公司 | High-efficiency energy-saving adsorption system for industrial volatile organic pollutants |
CN102814100A (en) * | 2011-06-07 | 2012-12-12 | 东洋纺织株式会社 | Gas adsorption unit device |
CN102814100B (en) * | 2011-06-07 | 2015-05-13 | 东洋纺织株式会社 | Gas adsorption unit device |
CN102397738A (en) * | 2011-11-08 | 2012-04-04 | 杭州中泰深冷技术股份有限公司 | Vertical bed adsorber |
CN104874206A (en) * | 2015-05-28 | 2015-09-02 | 江苏瑞吉格泰油气工程有限公司 | Separator tube bundle rotational flow inlet device |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |