CN202066840U - Active carboncoal absorbent absorption performance test device - Google Patents
Active carboncoal absorbent absorption performance test device Download PDFInfo
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- CN202066840U CN202066840U CN2011201250792U CN201120125079U CN202066840U CN 202066840 U CN202066840 U CN 202066840U CN 2011201250792 U CN2011201250792 U CN 2011201250792U CN 201120125079 U CN201120125079 U CN 201120125079U CN 202066840 U CN202066840 U CN 202066840U
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Abstract
The utility model discloses an active carboncoal absorbent absorption performance test device, which comprises a nitrogen tank, an oxygen tank, a plurality of valves, a plurality of rotor flow meters, a plurality of buffering bottles, a dryer, a volatile organic compounds (VOCs) gas generator, a sealing water bottle, a constant-temperature water-bath tank, a fixed bed adsorption device and a gas chromatograph; the nitrogen tank is sequentially connected with one valve and one rotor flow meter, the oxygen tank is sequentially connected with another valve and another rotor flow meter, two rotor flow meters are collectively connected with the buffering bottle, the buffering bottle is connected with the dryer, the dryer is respectively connected with the VOCs gas generator, the sealing water bottle and another buffering bottle through the valve and the rotor flow meter, the VOCs gas generator is connected with the other buffering bottle through the valve, the other buffering bottle is connected with the fixed bed absorption device through the valve and the rotor flow meter, the gas chromatograph is connected with two sides with the fixed bed adsorption device and the rotor flow meter which is connected with the fixed bed adsorption device in parallel.
Description
Technical field
The utility model relates to a kind of proving installation, especially relates to a kind of proving installation of active carbocoal adsorbents adsorb performance.
Background technology
The active carbocoal manufacturing process is simple, cost is low, absorption property is suitable with activated charcoal, cheap, become adsorbent with very big market attractiveness.The performance that can be the active carbocoal purifying volatile organic gas (VOCs) after the modification is tested, determine the performance of active carbocoal catalytic purification VOCs, and adsorption penetration time, adsorption capacity and temperature and air speed provide foundation to the influence of adsorption process for measuring best industrialization operating parameter and process conditions.
Numerous enterprise gives off in process of production and contains benzene series VOCs in a large number, the waste gas processing method that these enterprises adopt is active carbon adsorption mostly, at present, because activated charcoal in use exists a lot of problems in aspects such as adsorption capacity, regeneration, cost, operation, enterprise presses for novel waste gas treatment process and method.
Summary of the invention
The utility model provides a kind of proving installation that can test the absorption property of active carbocoal adsorbent quickly and easily in order to solve the defective that exists in the demand and the prior art.
For achieving the above object, the present invention has adopted following technical scheme:
A kind of proving installation of active carbocoal adsorbents adsorb performance, it is characterized in that, comprising: nitrogen pot (1), oxygen tank (2), a plurality of valve (3), a plurality of spinner-type flowmeter (4), a plurality of surge flask (5), exsiccator (6), VOCs gas generator (7), sealing water bottle (8), constant water bath box (9), ADSORPTION IN A FIXED BED device (10) and gas chromatograph (11); Wherein, nitrogen pot (1) is connected with a spinner-type flowmeter successively with a valve, oxygen tank (2) is connected with another spinner-type flowmeter successively with another valve, two spinner-type flowmeters are connected with a surge flask jointly, this surge flask is connected with exsiccator (6), this exsiccator (6) is respectively by valve and spinner-type flowmeter and VOCs gas generator (7), sealing water bottle (8), another surge flask connects, VOCs gas generator (7) is connected by another surge flask of valve and this, this another surge flask is connected with ADSORPTION IN A FIXED BED device (10) with spinner-type flowmeter by valve, and gas chromatograph (11) is connected in the both sides of ADSORPTION IN A FIXED BED device (10) and the spinner-type flowmeter that is connected with ADSORPTION IN A FIXED BED device (10) in parallel.
Described ADSORPTION IN A FIXED BED device is a test tube shape glass apparatus.
The diameter of described test tube shape glass apparatus is 16 millimeters, and length is 220 millimeters.
Glass mesh (12) aperture of described test tube shape glass apparatus is 1.5 millimeters.
In the described drying tube silica gel is housed.
Described VOCs gas generator (7) places thermostat water bath, to change the concentration of VOCs by the temperature of regulating thermostat water bath.
Also be provided with T-valve and be used to the mixed gas of taking a sample before and after described ADSORPTION IN A FIXED BED device, described sampling mixed gas input gas chromatograph (11) carries out the mensuration of absorption property.
The beneficial effects of the utility model are: adopted fixed-bed quartz reactor and gas chromatograph on-line analysis means, in 80～150 ℃ of scopes, carried out the test of absorption property with the VOCs that simulates.Greatly reduced the operating cost of present purifying VOCs, avoided secondary pollution, realized the zero-emission of pollutant, the semicoke product is carried out product chain to be extended, accomplish the active carbocoal after saturated, its fugitive constituent and thermal value increase, and can mix the fuel as Circulating Fluidized Bed Boiler with coal, avoid the secondary pollution that repeated regeneration produced, simplified technology greatly.The semicoke of solved in Shanxi, economizing in Shaanxi, Inner Mongol, Guizhou etc. is piled up problem, the aftertreatment and the secondary pollution of avoiding adsorbing saturated semicoke,
Description of drawings
Fig. 1 is the structural representation of the utility model proving installation.
Fig. 2 is the structural representation of ADSORPTION IN A FIXED BED device.
Embodiment
Below, the utility model is described in further detail in conjunction with the accompanying drawings and embodiments.
A kind of proving installation of active carbocoal adsorbents adsorb performance comprises: nitrogen pot (1), oxygen tank (2), a plurality of valve (3), a plurality of spinner-type flowmeter (4), a plurality of surge flask (5), exsiccator (6), VOCs gas generator (7), sealing water bottle (8), constant water bath box (9), ADSORPTION IN A FIXED BED device (10) and gas chromatograph (11); Wherein, nitrogen pot (1) is connected with a spinner-type flowmeter successively with a valve, oxygen tank (2) is connected with another spinner-type flowmeter successively with another valve, two spinner-type flowmeters are connected with a surge flask jointly, this surge flask is connected with exsiccator (6), this exsiccator (6) is respectively by valve and spinner-type flowmeter and VOCs gas generator (7), sealing water bottle (8), another surge flask connects, VOCs gas generator (7) is connected by another surge flask of valve and this, this another surge flask is connected with ADSORPTION IN A FIXED BED device (10) with spinner-type flowmeter by valve, and gas chromatograph (11) is connected in the both sides of ADSORPTION IN A FIXED BED device (10) and the spinner-type flowmeter that is connected with ADSORPTION IN A FIXED BED device (10) in parallel.
Described ADSORPTION IN A FIXED BED device is a test tube shape glass apparatus, and its diameter is 16 millimeters, and length is 220 millimeters, and the glass mesh aperture is 1.5 millimeters.In the described drying tube silica gel is housed.Described VOCs gas generator (7) places thermostat water bath, to change the concentration of VOCs by the temperature of regulating thermostat water bath.Also be provided with T-valve and be used to the mixed gas of taking a sample before and after described ADSORPTION IN A FIXED BED device, described sampling mixed gas input gas chromatograph (11) carries out the mensuration of absorption property.
Claims (7)
1. the proving installation of an active carbocoal adsorbents adsorb performance, it is characterized in that, comprising: nitrogen pot (1), oxygen tank (2), a plurality of valve (3), a plurality of spinner-type flowmeter (4), a plurality of surge flask (5), exsiccator (6), VOCs gas generator (7), sealing water bottle (8), constant water bath box (9), ADSORPTION IN A FIXED BED device (10) and gas chromatograph (11); Wherein, nitrogen pot (1) is connected with a spinner-type flowmeter successively with a valve, oxygen tank (2) is connected with another spinner-type flowmeter successively with another valve, two spinner-type flowmeters are connected with a surge flask jointly, this surge flask is connected with exsiccator (6), this exsiccator (6) is respectively by valve and spinner-type flowmeter and VOCs gas generator (7), sealing water bottle (8), another surge flask connects, VOCs gas generator (7) is connected by another surge flask of valve and this, this another surge flask is connected with ADSORPTION IN A FIXED BED device (10) with spinner-type flowmeter by valve, and gas chromatograph (11) is connected in the both sides of ADSORPTION IN A FIXED BED device (10) and the spinner-type flowmeter that is connected with ADSORPTION IN A FIXED BED device (10) in parallel.
2. the proving installation of active carbocoal adsorbents adsorb performance as claimed in claim 1 is characterized in that, described ADSORPTION IN A FIXED BED device is a test tube shape glass apparatus.
3. the proving installation of active carbocoal adsorbents adsorb performance as claimed in claim 2 is characterized in that, the diameter of described test tube shape glass apparatus is 16 millimeters, and length is 220 millimeters.
4. the proving installation of active carbocoal adsorbents adsorb performance as claimed in claim 2 is characterized in that, glass mesh (12) aperture of described test tube shape glass apparatus is 1.5 millimeters.
5. the proving installation of active carbocoal adsorbents adsorb performance as claimed in claim 1 is characterized in that, in the described drying tube silica gel is housed.
6. the proving installation of active carbocoal adsorbents adsorb performance as claimed in claim 1 is characterized in that, described VOCs gas generator (7) places thermostat water bath, to change the concentration of VOCs by the temperature of regulating thermostat water bath.
7. the proving installation of active carbocoal adsorbents adsorb performance as claimed in claim 1, it is characterized in that, also be provided with T-valve and be used to the mixed gas of taking a sample before and after described ADSORPTION IN A FIXED BED device, described sampling mixed gas input gas chromatograph (11) carries out the mensuration of absorption property.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201250792U CN202066840U (en) | 2011-04-26 | 2011-04-26 | Active carboncoal absorbent absorption performance test device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201250792U CN202066840U (en) | 2011-04-26 | 2011-04-26 | Active carboncoal absorbent absorption performance test device |
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| CN202066840U true CN202066840U (en) | 2011-12-07 |
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| CN2011201250792U Expired - Fee Related CN202066840U (en) | 2011-04-26 | 2011-04-26 | Active carboncoal absorbent absorption performance test device |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102288689A (en) * | 2011-04-26 | 2011-12-21 | 广东工业大学 | Device and method for testing adsorption property of activated semi-coke adsorbent |
| CN104360024A (en) * | 2014-11-19 | 2015-02-18 | 山西新华化工有限责任公司 | Dynamic evaluation method of adsorbing material for removing NO2 in polluted air |
| CN106226468A (en) * | 2015-02-13 | 2016-12-14 | 福建省鑫森炭业股份有限公司 | A kind of adsorbent test device |
| CN111578275A (en) * | 2020-04-03 | 2020-08-25 | 乐清市亿得利燃烧器有限公司 | Combustor with low emission of nitrogen oxides |
-
2011
- 2011-04-26 CN CN2011201250792U patent/CN202066840U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102288689A (en) * | 2011-04-26 | 2011-12-21 | 广东工业大学 | Device and method for testing adsorption property of activated semi-coke adsorbent |
| CN104360024A (en) * | 2014-11-19 | 2015-02-18 | 山西新华化工有限责任公司 | Dynamic evaluation method of adsorbing material for removing NO2 in polluted air |
| CN104360024B (en) * | 2014-11-19 | 2017-01-25 | 山西新华化工有限责任公司 | Dynamic evaluation method of adsorbing material for removing NO2 in polluted air |
| CN106226468A (en) * | 2015-02-13 | 2016-12-14 | 福建省鑫森炭业股份有限公司 | A kind of adsorbent test device |
| CN106226468B (en) * | 2015-02-13 | 2018-06-19 | 福建省鑫森炭业股份有限公司 | A kind of adsorbent test device |
| CN111578275A (en) * | 2020-04-03 | 2020-08-25 | 乐清市亿得利燃烧器有限公司 | Combustor with low emission of nitrogen oxides |
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Legal Events
| Date | Code | Title | Description |
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| 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: 20111207 Termination date: 20130426 |