CN204261532U - Novel organic exhaust gas adsorption-desorption treating apparatus - Google Patents
Novel organic exhaust gas adsorption-desorption treating apparatus Download PDFInfo
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- CN204261532U CN204261532U CN201420704535.2U CN201420704535U CN204261532U CN 204261532 U CN204261532 U CN 204261532U CN 201420704535 U CN201420704535 U CN 201420704535U CN 204261532 U CN204261532 U CN 204261532U
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Abstract
The utility model relates to a kind of novel organic exhaust gas adsorption-desorption treating apparatus.Its technical scheme is: comprise distribution feed system, adsorption reaction system and product separation acquisition system, first material device, the second material device, 3 material device are connected to distribution tank respectively by pipeline, described work liquid pool is connected to distribution tank by vaporizer, the output of described distribution tank is connected to adsorption reaction system, gas after each adsorption column process is connected respectively to the first cooler, the second cooler and the 3rd cooler, carries out sampling analysis respectively.Beneficial effect is: fluidised bed adsorption post not only can be used for organic exhaust gas adsorption process, and can realize saturated filler desorption, thus reaches regneration of adsorbent material and the object of recycling.The method can reduce costs and alleviate the pollution of saturated load sorbing material for environment; Sorbing material can be extended and use the longevity, input of economizing on the use of funds.
Description
Technical field
The utility model relates to a kind of industrial organic exhaust gas treating apparatus, particularly one novel organic exhaust gas adsorption-desorption treating apparatus.
Background technology
Absorption method is a kind of method of comparatively ripe process organic exhaust gas, has removal efficiency advantages of higher.But adsorb saturated rear active carbon desorption problem to be comparatively difficult to resolve certainly.Activated carbon fiber is a kind of novel porous sorbing material, has the performance more excellent compared with conventional carbon, has that phosphorus content is high, specific area is large, micropore is abundant, adsorbance is large and the advantage such as adsorption rate is fast.In addition, biological enzyme formulation is nontoxic pollution-free and can complete biodegradable, utilizes the waste gas processing method of organic contamination component in biological enzyme oxidation process waste gas, can reach the object of environmental protection process organic gas.
Summary of the invention
The purpose of this utility model is exactly in view of the foregoing defects the prior art has, provides a kind of novel organic exhaust gas adsorption-desorption treating apparatus, both can realize multiple sorbing material co-treatment industrial waste gas, and can carry out regneration of adsorbent material again simultaneously.
Its technical scheme is: comprise distribution feed system, adsorption reaction system and product separation acquisition system, described distribution feed system comprises the first material device, second material device, 3 material device, work liquid pool, distribution tank, vaporizer, the first described material device, second material device, 3 material device is connected to distribution tank respectively by pipeline, described work liquid pool is connected to distribution tank by vaporizer, the output of described distribution tank is connected to adsorption reaction system, described adsorption reaction system comprises the first adsorption column, second adsorption column, 3rd adsorption column, primary heater, secondary heater, 3rd heater, the first described adsorption column connects primary heater, second adsorption column connects secondary heater, 3rd adsorption column connects the 3rd heater, described product separation acquisition system comprises the first cooler, the second cooler, the 3rd cooler, the first collector, the second collector, the 3rd collector, gas after each adsorption column process is connected respectively to the first cooler, the second cooler and the 3rd cooler, carries out sampling analysis respectively.
The first above-mentioned material device, the second material device, 3 material device are respectively equipped with heater.
The first above-mentioned adsorption column, the second adsorption column are fixed bed form, and the 3rd adsorption column is fluid bed form, and three adsorption columns can also, serial conversion.
The high filler of 12cm is filled in the first above-mentioned adsorption column, the second adsorption column and the 3rd adsorption column inside.
The beneficial effects of the utility model are: (1) air distribution system can simulate multicomponent organic exhaust gas, realizes different component combination of gases, and accurately can control gas flow; (2) adsorption reaction partial adsorbates unit process pipe realizes replacement by dismounting; (3) be provided with temperature regulating device outside reaction tube and can keep temperature constant, to guarantee that filler plays maximum adsorption effect under optimum temperature; (4), in each adsorption column series connection situation, the raising of organic exhaust gas treatment effect under different filler acting in conjunction can be realized.In situation in parallel, both can be used for studying the treatment effect of different filler for same component gas, can be used for again contrast gas treatment effect and multi-form bed interlayer relation; (5) fluidised bed adsorption post not only can be used for organic exhaust gas adsorption process, and can realize saturated filler desorption, thus reaches regneration of adsorbent material and the object of recycling.The method can reduce costs and alleviate the pollution of saturated load sorbing material for environment; (6) this device can carry out adsorption-desorption-absorption continuous circulation operation, can extend sorbing material and use the longevity, input of economizing on the use of funds.
Accompanying drawing explanation
Accompanying drawing 1 is structural representation of the present utility model;
In upper figure: the first material device 1, second material device 2,3 material device 3, work liquid pool 4, distribution tank 5, vaporizer 6, first adsorption column 7, second adsorption column 8, the 3rd adsorption column 9, primary heater 10, secondary heater 11, the 3rd heater 12, first cooler 13, second cooler 14, the 3rd cooler 15, first collector 16, second collector 17, the 3rd collector 18.
Detailed description of the invention
By reference to the accompanying drawings 1, the utility model will be further described:
The utility model comprises distribution feed system, adsorption reaction system and product separation acquisition system, described distribution feed system comprises the first material device 1, second material device 2, 3 material device 3, work liquid pool 4, distribution tank 5, vaporizer 6, the first described material device 1, second material device 2, 3 material device 3 is connected to distribution tank 5 respectively by pipeline, described work liquid pool 4 is connected to distribution tank 5 by vaporizer 6, the output of described distribution tank 5 is connected to adsorption reaction system, three gas generating units are within the scope of 1.5KW heating power, different gas sample component is produced according to charging difference.Gas sample enters distributing valve under carrier gas nitrogen, ar gas acting, and in distributing valve, realize different gas sample component Homogeneous phase mixing, and can carry out sample analysis.
Described adsorption reaction system comprises the first adsorption column 7, second adsorption column 8, the 3rd adsorption column 9, primary heater 10, secondary heater 11, the 3rd heater 12, the first described adsorption column 7 connects primary heater 10, second adsorption column 8 connects secondary heater 11, and the 3rd adsorption column 9 connects the 3rd heater 12;
Wherein, the reaction tube in adsorption column adopts quartz glass to make, 20 × 250mm, withstand voltage below 1.0Mpa, coating film treatment, constant temperature 20 ~ 120 DEG C, is furnished with insulation temperature control control appliance.The high filler of 12cm is filled in adsorption column reaction tube inside, realizes organic waste-gas purification effect by absorption or adsoption catalysis effect.Fluidised bed adsorption post not only can be used for organic exhaust gas adsorption process, and can realize saturated filler desorption.
Described product separation acquisition system comprises the first cooler 13, second cooler 14, the 3rd cooler 15, first collector 16, second collector 17, the 3rd collector 18, gas after each adsorption column process is connected respectively to the first cooler 13, second cooler 14 and the 3rd cooler 15, carries out sampling analysis respectively.
Wherein, the first material device 1, second material device 2,3 material device 3 are respectively equipped with heater, and the first above-mentioned adsorption column 7, second adsorption column 8 is fixed bed form, and the 3rd adsorption column 9 is fluid bed form, and three adsorption columns can also, serial conversion.
Claims (4)
1. novel organic exhaust gas adsorption-desorption treating apparatus, is characterized in that: comprise distribution feed system, adsorption reaction system and product separation acquisition system, described distribution feed system comprises the first material device (1), second material device (2), 3 material device (3), work liquid pool (4), distribution tank (5), vaporizer (6), described the first material device (1), second material device (2), 3 material device (3) is connected to distribution tank (5) respectively by pipeline, described work liquid pool (4) is connected to distribution tank (5) by vaporizer (6), the output of described distribution tank (5) is connected to adsorption reaction system, and described adsorption reaction system comprises the first adsorption column (7), second adsorption column (8), 3rd adsorption column (9), primary heater (10), secondary heater (11), 3rd heater (12), described the first adsorption column (7) connects primary heater (10), and the second adsorption column (8) connects secondary heater (11), and the 3rd adsorption column (9) connects the 3rd heater (12), described product separation acquisition system comprises the first cooler (13), the second cooler (14), the 3rd cooler (15), the first collector (16), the second collector (17), the 3rd collector (18), gas after each adsorption column process is connected respectively to the first cooler (13), the second cooler (14) and the 3rd cooler (15), carries out sampling analysis respectively.
2. novel organic exhaust gas adsorption-desorption treating apparatus according to claim 1, is characterized in that: described the first material device (1), the second material device (2), 3 material device (3) are respectively equipped with heater.
3. novel organic exhaust gas adsorption-desorption treating apparatus according to claim 1, it is characterized in that: described the first adsorption column (7), the second adsorption column (8) are fixed bed form, 3rd adsorption column (9) is fluid bed form, and three adsorption columns can also, serial conversion.
4. the novel organic exhaust gas adsorption-desorption treating apparatus according to claim 1 or 3, is characterized in that: the high filler of 12cm is filled in described the first adsorption column (7), the second adsorption column (8) and the 3rd adsorption column (9) inside.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420704535.2U CN204261532U (en) | 2014-11-21 | 2014-11-21 | Novel organic exhaust gas adsorption-desorption treating apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420704535.2U CN204261532U (en) | 2014-11-21 | 2014-11-21 | Novel organic exhaust gas adsorption-desorption treating apparatus |
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| Publication Number | Publication Date |
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| CN204261532U true CN204261532U (en) | 2015-04-15 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420704535.2U Expired - Fee Related CN204261532U (en) | 2014-11-21 | 2014-11-21 | Novel organic exhaust gas adsorption-desorption treating apparatus |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105879575A (en) * | 2016-05-25 | 2016-08-24 | 中北大学 | Experimental device for harmful-gas absorption |
| CN113952822A (en) * | 2021-09-04 | 2022-01-21 | 广州市帝东环保科技有限公司 | Fixed bed and fluidized bed recovery method for VOCS in viscose industry |
| CN114814087A (en) * | 2022-03-29 | 2022-07-29 | 福州大学 | Device for testing circulating adsorption performance of adsorbent to ammonia gas |
-
2014
- 2014-11-21 CN CN201420704535.2U patent/CN204261532U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105879575A (en) * | 2016-05-25 | 2016-08-24 | 中北大学 | Experimental device for harmful-gas absorption |
| CN105879575B (en) * | 2016-05-25 | 2019-02-26 | 中北大学 | A kind of pernicious gas adsorption experimental apparatus |
| CN113952822A (en) * | 2021-09-04 | 2022-01-21 | 广州市帝东环保科技有限公司 | Fixed bed and fluidized bed recovery method for VOCS in viscose industry |
| CN114814087A (en) * | 2022-03-29 | 2022-07-29 | 福州大学 | Device for testing circulating adsorption performance of adsorbent to ammonia gas |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150415 Termination date: 20151121 |
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| EXPY | Termination of patent right or utility model |