CN201701856U - Absorption bed and organic waste gas purifying system using same - Google Patents
Absorption bed and organic waste gas purifying system using same Download PDFInfo
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- CN201701856U CN201701856U CN2010201942445U CN201020194244U CN201701856U CN 201701856 U CN201701856 U CN 201701856U CN 2010201942445 U CN2010201942445 U CN 2010201942445U CN 201020194244 U CN201020194244 U CN 201020194244U CN 201701856 U CN201701856 U CN 201701856U
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Abstract
The utility model provides an absorption bed, which comprises a front air cover, a bed body and a rear air cover. An absorption inlet and a desorption outlet are arranged on the front air cover; an absorption inlet and a desorption inlet are arranged on the rear air cover; a plurality of activated carbon layers are arranged inside the bed body; a gas collection main pipe and a plurality of horizontally extending gas collection tanks are arranged inside the front air cover; each gas collection tank faces one activated carbon layer; all the gas collection tanks are communicated with the gas collection main pipe; and the gas collection main pipe is communicated with the desorption outlet. The utility model further provides an organic waste gas purifying system using the absorption bed. The absorption bed and the organic waste gas purifying system can effectively prevent heat in the absorption bed from being excessively concentrated in desorption process to cause safety accidents of spontaneous combustion of gas and fire catching of activated carbon inside the absorption bed.
Description
Technical field
The utility model relates to a kind of adsorbent bed and uses the organic waste-gas purification system of this adsorbent bed.
Background technology
Application number is the organic waste-gas purification treatment facility that 02284062.1 Chinese patent is introduced, and entire equipment mainly comprises dirt catcher, adsorbent bed, desorption blower fan, main air blower and the catalytic combustion bed etc. of parallel connection more than three or three.The absorption of this kind equipment collection, desorption and catalytic combustion are one, can effectively handle the industrial waste gas of generation.The desorption process of this equipment is, the adsorbent bed of state of reaching capacity stops absorption, the hot gas that the catalytic combustion bed is sent enters adsorbent bed, active carbon is heated and parses organic gas, the gas that parses is introduced the catalytic combustion bed by the desorption blower fan and is carried out purification of combustion, purifying exhaust air, and the hot gas of discharging is back to the regeneration of active carbon.Yet; in the component in the organic exhaust gas, regular meeting comprises as this type of normal temperature of butanone down for liquid but the lower composition of boiling point, and its steam and air can form explosive mixture; easily cause that in desorption process the active carbon in the adsorbent bed catches fire, and influences the safe handling of equipment.
The utility model content
The technical problems to be solved in the utility model is to provide the adsorbent bed in a kind of cleaning equipment for waste organic gas and uses the organic waste-gas purification system of this adsorbent bed, the active carbon that this adsorbent bed and this organic waste-gas purification system can effectively avoid desorption process the to cause incident of catching fire guarantees system safety operation.
In order to address the above problem, the adsorbent bed that the utility model provides, comprise preceding fan housing, bed body and back fan housing, fan housing is provided with absorption inlet and desorption outlet before described, described back fan housing is provided with absorption outlet and desorption inlet, comprise some active carbon layers in the described bed body, be provided with gas gathering manifold and the horizontally extending pneumatic trough of Duo Gen in the fan housing before described, every pneumatic trough faces an active carbon layer, all pneumatic troughs all are connected with gas gathering manifold, and described gas gathering manifold is connected with described desorption outlet.
Preferably, be equipped with vertical dividing plate in described each active carbon layer.
Further, described dividing plate is made of steel frame and the steel wire that is fixed on the steel frame both sides.
Preferably, described desorption porch also is provided with some flow deflectors, and the two ends overlap joint of described flow deflector is fixed on the inwall of back fan housing.
A kind of organic waste-gas purification system that uses above-mentioned adsorbent bed, comprise absorption and desorption two large divisions, absorbed portion comprises wire gauzee filter, described adsorbent bed that the absorption inlet links to each other with described wire gauzee filter outlet and the main air blower that links to each other with the absorption outlet of described adsorbent bed, the desorption portion branch comprises the catalytic combustion bed, mixed flow heat exchanger and desorption blower fan, the outlet of described catalytic combustion bed links to each other with the inlet of described mixed flow heat exchanger, the outlet of described mixed flow heat exchanger links to each other with the desorption of described adsorbent bed inlet, the desorption outlet of described adsorbent bed links to each other with the inlet of described desorption blower fan, and the outlet of described desorption blower fan links to each other with the inlet of described catalytic combustion bed.
Preferably, described adsorbent bed has three at least, between the absorption of each adsorbent bed inlet and the described wire gauzee filter, between absorption outlet and the described main air blower, desorption enters the mouth and described mixed flow heat exchanger between and desorption exports and described desorption blower fan between be equipped with motor-driven valve.
Adsorbent bed in the cleaning equipment for waste organic gas of the present utility model can effectively avoid in the desorption process heat in the adsorbent bed too concentrated, and causes the catch fire generation of these security incidents of gas spontaneous combustion, active carbon in it.
Description of drawings
Fig. 1 is the structural representation of the utility model adsorbent bed.
Fig. 2 is the distribution schematic diagram of bed activity in vivo charcoal layer.
Fig. 3 is the structural representation of dividing plate.
Fig. 4 is the structural representation of back fan housing.
Fig. 5 is the schematic diagram at I place among Fig. 4.
Fig. 6 is a gas gathering manifold schematic diagram in the preceding fan housing.
Fig. 7 is the organic waste-gas purification system schematic.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is done and to be specified.
As Fig. 1 and shown in Figure 6, adsorbent bed of the present utility model, fan housing 1 before comprising, bed body 2 and back fan housing 3, preceding fan housing 1 are provided with absorption inlet 18 and desorption outlet 5, back fan housing 3 is provided with absorption outlet 19 and desorption inlet 4, comprise some active carbon layers 6 in the bed body 2, be provided with the horizontally extending pneumatic trough 9 of gas gathering manifold 10 and Duo Gen in the preceding fan housing 1, every pneumatic trough 9 faces an active carbon layer 6, all pneumatic troughs 9 all are connected with gas gathering manifold 10, and gas gathering manifold 10 is connected with desorption outlet 5.This kind structure, make the gas that active carbon layer 6 parses, along each pneumatic trough 9, flow into gas gathering manifold 10, after gas gathering manifold 10 gathers, go out from desorption outlet 5, thereby fan housing 1 negative pressure point is uniform before making, avoided in desorption process that local the appearance causes the low ignition point organic gas because of concentration, temperature drift spontaneous combustion in overheated dead angle in the adsorbent bed.
As shown in Figure 2, be equipped with vertical dividing plate 7 in each active carbon layer 6, as shown in Figure 3, dividing plate 7 is made of steel frame and the steel wire that is fixed on the steel frame both sides, is the steel frame two sides and pastes steel wire and fix.Between each active carbon layer, install the steel frame filter additional and do at interval, increased the gap between the active carbon, thereby avoid heat concentrations between active carbon and security incident takes place.
Shown in Figure 4 and 5, desorption 4 places that enter the mouth also are provided with some flow deflectors 8, and the two ends overlap joint of flow deflector 8 is fixed on the inwall of back fan housing 3.Except on the fan housing 3 of back near the desorption fixing deflector 20 in 4 places that enters the mouth, the gas distribution direction of air inlet can be further adjusted in the setting of flow deflector 8, makes hot-air evenly enter the active carbon layer 6 of a body.
Organic waste-gas purification of the present utility model as shown in Figure 7 system, comprise absorption and desorption two large divisions, absorbed portion comprises wire gauzee filter 11, adsorbent beds that absorption inlet 18 links to each other with wire gauzee filter 11 outlets and export 19 main air blowers that link to each other 15 with the absorption of adsorbent bed, the desorption portion branch comprises catalytic combustion bed 13, mixed flow heat exchanger 14 and desorption blower fan 12, the outlet of catalytic combustion bed 13 links to each other with the inlet of mixed flow heat exchanger 14, the outlet of mixed flow heat exchanger 14 links to each other with the desorption of adsorbent bed inlet 4, the desorption of adsorbent bed outlet 5 links to each other with the inlet of desorption blower fan 12, and the outlet of desorption blower fan 12 links to each other with the inlet of catalytic combustion bed 13.
The mixed flow heat exchanger 14 here is provided with hot-wind inlet, hot-blast outlet, cold air inlet and cold wind outlet, and the outlet of catalytic combustion bed 13 links to each other with the inlet of mixed flow heat exchanger 14, and the inlet here is meant the hot-wind inlet of mixed flow heat exchanger 14; The outlet of mixed flow heat exchanger 14 links to each other with the desorption of adsorbent bed inlet 4, the outlet here is meant the cold wind outlet of mixed flow heat exchanger 14, promptly the heat that comes out from catalytic combustion bed 13 enters the hot-wind inlet of mixed flow heat exchanger 14 with mist, after carrying out heat exchange with the cold air that enters from cold air inlet, through preheating cold air export out from cold wind and enter desorption inlet 4, the gas after other burnings comes out to enter aiutage 16 dischargings from the hot-blast outlet of mixed flow heat exchanger.
Adsorbent bed has three at least, between the absorption of each adsorbent bed inlet 18 and the wire gauzee filter 11, between absorption outlet 19 and the main air blower 15, desorption enter the mouth 4 and mixed flow heat exchanger 14 between and desorption export 5 and desorption blower fan 12 between be equipped with motor-driven valve 17.
As shown in Figure 7, the course of work of the present utility model is, the air that comprises organic exhaust gas flows into efficient wire gauzee filter 11 from C, assorted dirt in the waste gas is filtered removal, then evenly by two in three adsorbent beds, organic principle in the waste gas is by charcoal absorption, and purified gas is pumped to aiutage 16 discharges by main air blower 15.When certain adsorbent bed reaches capacity, stop absorption,, make other two adsorbent beds be operated in adsorbed state by the switching of motor-driven valve 17.Then by the switching of motor-driven valve 17, connection enters the desorption part to the saturated adsorbent bed that reaches.During desorption, hot-air flows to desorption inlet 4 along A place arrow direction among Fig. 1, enter adsorbent bed bed body 2 from desorption inlet 4 again, active carbon in the bed body 2 is heated and parses the organic gas of high concentration, organic gas is exporting under 12 effects of the 5 desorption blower fans that link to each other with desorption, come out from desorption outlet 5, introduce catalytic combustion bed 13 along B place arrow direction by desorption blower fan 12, in catalytic combustion bed 13, carry out catalytic combustion, organic principle is converted into nontoxic, harmless carbon dioxide and water discharge a large amount of heats simultaneously, and energy comes out from catalytic combustion bed 13, a part enters the mixed flow heat exchanger, after carrying out heat exchange, heat is directly sent into desorption inlet 4, carry out active carbon regeneration, gas after another fraction burning enters discharging in the aiutage 16.Improvement by to desorption inlet, active carbon layer and desorption export structure makes organic gas in desorption process, effectively avoids the amount of localized heat concentrations occurring in adsorbent bed, causes the spontaneous combustion of low ignition point gas, causes the active carbon incident of catching fire.
Higher when burnt gas concentration, when reaction temperature is higher, the desorption blower fan is opened automatically, as shown in Figure 7, fresh cold air to replenishing into, to reduce temperature, is guaranteed catalytic combustion bed safety, efficient operation along desorption blower fan 12 arrow indication D.
The utility model makes organic gas in desorption process by to the improvement of desorption inlet, active carbon layer and desorption export structure, effectively avoids causing in adsorbent bed internal cause amount of localized heat concentrations the spontaneous combustion of low ignition point gas, the active carbon incident of catching fire.
More than just the utility model has been carried out exemplary explanation, specific implementation of the present utility model is not limited thereto.The insubstantial modifications that any employing design of the present utility model and technical scheme are carried out is all within protection domain of the present utility model.
Claims (6)
1. adsorbent bed, comprise preceding fan housing (1), bed body (2) and back fan housing (3), fan housing (1) is provided with absorption inlet (18) and desorption outlet (5) before described, described back fan housing (3) is provided with absorption outlet (19) and desorption inlet (4), comprise some active carbon layers (6) in the described bed body (2), it is characterized in that: be provided with gas gathering manifold (10) and many horizontally extending pneumatic troughs (9) in the fan housing (1) before described, every pneumatic trough (9) faces an active carbon layer (6), all pneumatic troughs (9) all are connected with gas gathering manifold (10), and described gas gathering manifold (10) exports (5) with described desorption and is connected.
2. adsorbent bed according to claim 1 is characterized in that: be equipped with vertical dividing plate (7) in described each active carbon layer (6).
3. adsorbent bed according to claim 2 is characterized in that: described dividing plate (7) is made of steel frame and the steel wire that is fixed on the steel frame both sides.
4. adsorbent bed according to claim 1 is characterized in that: described desorption inlet (4) locates also to be provided with some flow deflectors (8), and the two ends overlap joint of described flow deflector (8) is fixed on the inwall of back fan housing (3).
5. organic waste-gas purification system that uses adsorbent bed as claimed in claim 1, it is characterized in that: comprise absorption and desorption two large divisions, absorbed portion comprises wire gauzee filter (11), described adsorbent bed that absorption inlet (18) links to each other with described wire gauzee filter (11) outlet and the main air blower (15) that links to each other with the absorption outlet (19) of described adsorbent bed, the desorption portion branch comprises catalytic combustion bed (13), mixed flow heat exchanger (14) and desorption blower fan (12), the outlet of described catalytic combustion bed (13) links to each other with the inlet of described mixed flow heat exchanger (14), the outlet of described mixed flow heat exchanger (14) links to each other with the desorption of described adsorbent bed inlet (4), the desorption outlet (5) of described adsorbent bed links to each other with the inlet of described desorption blower fan (12), and the outlet of described desorption blower fan (12) links to each other with the inlet of described catalytic combustion bed (13).
6. organic waste-gas purification according to claim 5 system, it is characterized in that: described adsorbent bed has three at least, between the absorption of each adsorbent bed inlet (18) and the described wire gauzee filter (11), between absorption outlet (19) and the described main air blower (15), desorption enters the mouth (4) and described mixed flow heat exchanger (14) between and desorption export between (5) and the described desorption blower fan (12) and be equipped with motor-driven valve (17).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201942445U CN201701856U (en) | 2010-05-14 | 2010-05-14 | Absorption bed and organic waste gas purifying system using same |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201942445U CN201701856U (en) | 2010-05-14 | 2010-05-14 | Absorption bed and organic waste gas purifying system using same |
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| CN201701856U true CN201701856U (en) | 2011-01-12 |
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| CN2010201942445U Expired - Lifetime CN201701856U (en) | 2010-05-14 | 2010-05-14 | Absorption bed and organic waste gas purifying system using same |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102188875A (en) * | 2011-03-25 | 2011-09-21 | 天津赛智科技发展有限公司 | Energy-saving high-efficiency purification system for industrial volatilizable organic pollutant |
| CN102188874A (en) * | 2011-03-25 | 2011-09-21 | 天津赛智科技发展有限公司 | High-efficiency energy-saving absorption device of industrial volatilizable organic pollutant |
| CN102188873A (en) * | 2011-03-25 | 2011-09-21 | 天津赛智科技发展有限公司 | Energy-saving efficient adsorption and desorption combined system |
| 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 |
| CN102240496A (en) * | 2010-05-14 | 2011-11-16 | 上海嘉园环保科技有限公司 | Adsorption bed and organic exhaust gas purifying system employing adsorption bed |
| CN104971618A (en) * | 2014-04-02 | 2015-10-14 | 德清天皓环保科技有限公司 | Communication gas shell with waste gas diffusion device |
-
2010
- 2010-05-14 CN CN2010201942445U patent/CN201701856U/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102240496A (en) * | 2010-05-14 | 2011-11-16 | 上海嘉园环保科技有限公司 | Adsorption bed and organic exhaust gas purifying system employing adsorption bed |
| CN102240496B (en) * | 2010-05-14 | 2013-07-03 | 上海嘉园环保科技有限公司 | Adsorption bed and organic exhaust gas purifying system employing adsorption bed |
| CN102188875A (en) * | 2011-03-25 | 2011-09-21 | 天津赛智科技发展有限公司 | Energy-saving high-efficiency purification system for industrial volatilizable organic pollutant |
| CN102188874A (en) * | 2011-03-25 | 2011-09-21 | 天津赛智科技发展有限公司 | High-efficiency energy-saving absorption device of industrial volatilizable organic pollutant |
| CN102188873A (en) * | 2011-03-25 | 2011-09-21 | 天津赛智科技发展有限公司 | Energy-saving efficient adsorption and desorption combined system |
| 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 |
| CN102188875B (en) * | 2011-03-25 | 2013-03-20 | 天津赛智科技发展有限公司 | Energy-saving high-efficiency purification system for industrial volatilizable organic pollutant |
| CN104971618A (en) * | 2014-04-02 | 2015-10-14 | 德清天皓环保科技有限公司 | Communication gas shell with waste gas diffusion device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20110112 Effective date of abandoning: 20130703 |
|
| RGAV | Abandon patent right to avoid regrant |