CN206008380U - A kind of organic liquid volatile matter withdrawer for air dry oven - Google Patents
A kind of organic liquid volatile matter withdrawer for air dry oven Download PDFInfo
- Publication number
- CN206008380U CN206008380U CN201620907601.5U CN201620907601U CN206008380U CN 206008380 U CN206008380 U CN 206008380U CN 201620907601 U CN201620907601 U CN 201620907601U CN 206008380 U CN206008380 U CN 206008380U
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- Prior art keywords
- air
- dry oven
- water tank
- air dry
- withdrawer
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- 239000007788 liquid Substances 0.000 title claims abstract description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 38
- 239000000428 dust Substances 0.000 claims abstract description 14
- 230000005587 bubbling Effects 0.000 claims abstract description 10
- 238000012805 post-processing Methods 0.000 claims abstract description 6
- 229910001111 Fine metal Inorganic materials 0.000 claims abstract description 5
- 239000002699 waste material Substances 0.000 claims abstract description 4
- 239000012530 fluid Substances 0.000 claims description 6
- 230000002950 deficient Effects 0.000 claims description 3
- 238000009434 installation Methods 0.000 claims description 3
- 239000007789 gas Substances 0.000 abstract description 30
- 238000000034 method Methods 0.000 abstract description 11
- 230000008569 process Effects 0.000 abstract description 10
- 239000000126 substance Substances 0.000 abstract description 9
- 239000000203 mixture Substances 0.000 abstract description 4
- 239000002912 waste gas Substances 0.000 abstract description 4
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 238000002474 experimental method Methods 0.000 abstract description 3
- 235000011194 food seasoning agent Nutrition 0.000 abstract description 2
- 238000004064 recycling Methods 0.000 abstract description 2
- 238000010521 absorption reaction Methods 0.000 description 6
- 238000001035 drying Methods 0.000 description 5
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 4
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000000498 ball milling Methods 0.000 description 3
- 239000000919 ceramic Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000013467 fragmentation Methods 0.000 description 3
- 238000006062 fragmentation reaction Methods 0.000 description 3
- 230000000630 rising effect Effects 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000002604 ultrasonography Methods 0.000 description 2
- 235000010044 Hernandia moerenhoutiana Nutrition 0.000 description 1
- 244000084296 Hernandia moerenhoutiana Species 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000003491 array Methods 0.000 description 1
- 238000010923 batch production Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
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- Drying Of Solid Materials (AREA)
Abstract
The utility model discloses a kind of organic liquid volatile matter withdrawer for air dry oven, it is related to dry and field of Environment Protection, it is connected on air dry oven air vent, by dust filter unit, pressurizing air air pump and vertical water tank composition, threeway airway is provided between the dust filter unit and air dry oven air vent, in line gas switch and post-treatment gas switch is respectively equipped with the escape pipe of threeway airway, post processing airway is provided between the dust filter unit and pressurizing air air pump, the inner bottom of the vertical water tank is provided with multigroup bubbling gas disk, each bubbling gas disk is connected with pressurizing air air pump by pressure soft air-guide pipe accordingly, in the inside of the vertical water tank, upside is provided with multilamellar fine metal mesh, top is provided with the steam vent for connecing outdoor exhaust fan and the water inlet pipe for being passed through absorbing liquid, bottom is provided with waste liquid drain pipe.This utility model is realized being reclaimed via air dry oven discharge at low cost containing a series of water-soluble common flammable Organic substances; and prevent above-mentioned gas from being directly discharged in air, it is relate suitable to the waste gas produced environmental protection recycling of hot-air seasoning process in the experiment of above-mentioned substance.
Description
Technical field：
This utility model is related to dry and field of Environment Protection, and in particular to a kind of organic liquid for air dry oven volatilizees
Thing withdrawer.
Background technology：
Air dry oven is the conventional drying equipment of the specialized laboratories of subject such as current chemistry, material, and which has drying
The features such as speed is fast, drying efficiency is high, adaptability is extensive, as equipment composition is relatively simple, operation and maintenance cost are relatively low,
Therefore all it is requisite equipment in a lot of laboratorys.
Traditional air dry oven is mainly by casing, resistive heater, blower motor fan and electronic control unit
Deng composition, which operationally sucks air by blower fan of casing foot and forms air-flow upwards, and by heating electricity
After resistance silk makes air be heated to predetermined temperature so as to flow through the sample for being placed in top, hot air sample is so that sample
In volatile substances vaporization, and with flowing hot-air via casing top exhaustor discharge casing outside.
Traditional air dry oven is that the above-mentioned air containing harmful volatile organic gas is directly discharged to air
In, it is impossible to above-mentioned volatile material is reclaimed, thus is unfavorable for reducing production cost and environmental conservation.Much testing
In (most typical example is exactly prepared by function ceramics), volatile organic ball milling agent (ethanol, acetone, butanone will be often used
Etc.), and the large usage quantity of these ball milling agents, the ceramic slurry after the completion of ball milling is using the drying of above-mentioned air dry oven
During, as the gas of these material volatilizations is inflammable, therefore experiment and some related small batch production process are had larger
Potential safety hazard, and some volatilization gas toxic to human body (various ketones), therefore existing technology can not solve above-mentioned
Problem of the material gases in drying course to the pollution and recovery of environment.
Utility model content：
Technical problem to be solved in the utility model is to provide a kind of waste gas processed produced by air dry oven
And the supporting retracting device that can realize reclaiming organic substance in waste gas.
Technical problem to be solved in the utility model is realized using following technical scheme：
A kind of organic liquid volatile matter withdrawer for air dry oven, is connected on air dry oven air vent, by
Dust filter unit, pressurizing air air pump and vertical water tank composition, is provided between the dust filter unit and air dry oven air vent
Threeway airway, is respectively equipped with line gas switch and post-treatment gas switch, the dust on the escape pipe of threeway airway
Post processing airway is provided between filter and pressurizing air air pump, and the inner bottom of the vertical water tank is provided with multigroup bubbling gas
Disk, each bubbling gas disk are connected with pressurizing air air pump by pressure soft air-guide pipe accordingly, in the inside of the vertical water tank on
Side is provided with multilamellar fine metal mesh, and top is provided with the steam vent for connecing outdoor exhaust fan and the water inlet pipe for being passed through absorbing liquid, and bottom sets
There is waste liquid drain pipe.
The pressure soft air-guide pipe is provided with flow-stop valve, and the flow-stop valve has multiple, and is combined into the form of array.
The quantity of the pressure soft air-guide pipe and internal diameter are according to air dry oven model joined together and the difference of capacity
And adjust accordingly.
The vertical water tank is additionally provided with dipperstick, ultrasonic transducer and impeller-agitator.
The installation site of the pressurizing air air pump prevents from absorbing during fluid stopping defective valve higher than the liquid level in vertical water tank
Liquid pours in down a chimney in pump.
Operation principle of the present utility model：
By the setting of threeway airway, in order to realize the in line conversion with post processing two ways of gas.Vertical water tank
It is the main body of equipment realization recovery function, the wherein trend of gas is bottom in and top out formula, and the trend of absorbing liquid is in contrast.
Before the procedure should first from above water tank, water inlet pipe imports absorption water, or dissolved certain absorbent or reactant
Absorbing liquid, to water level properly after open pressurizing air air pump be evacuated, bring into operation air dry oven afterwards；In forced air drying
In case running, the hot-air containing organic volatile is entered in water tank, via bubbling via pressure soft air-guide pipe, flow-stop valve
The fragmentation of decomposing of gas disk is acted on and produces multigroup superfine bubble stream, and bubble is fully contacted with water during rising, is completed
The absorption process of wherein organic substance, the aqueous solution after absorption process terminates can be taken out by drain pipe below water tank and be distilled
Reclaim.
The beneficial effects of the utility model are：Discharged via air dry oven in order to reclaim by this device at low cost
Containing a series of water-soluble common flammable Organic substance (ethanol, acetone, butanone etc.), and prevent above-mentioned gas from directly arranging
Enter in air, be relate suitable to hot-air seasoning process in the experiment (especially function ceramics preparation) of above-mentioned substance waste gas produced
Environmental protection recycling.
Description of the drawings：
Fig. 1 is structural representation of the present utility model；
Wherein：1- air dry ovens；2- dust filter units；3- pressurizing air air pumps；4- vertical water tanks；5- threeway airways；
The in line gas switch of 6-；7- post-treatment gas are switched；8- post processing airways；9- bubbling gas disks；10- is pressure soft air-guide pipe；11-
Fine metal mesh；12- steam vents；13- water inlet pipes；14- drain pipies；15- fluid stopping valve arrays；16- dippersticks；17- ultrasounds
Wave transducer；18- impeller-agitators.
Specific embodiment：
In order that technological means, creation characteristic, reached purpose and effect that this utility model is realized are easy to understand, under
Face combines and is specifically illustrating, and specific embodiment of the present utility model is expanded on further.
As shown in figure 1, a kind of organic liquid volatile matter withdrawer for air dry oven, is connected to air dry oven 1
On air vent, it is made up of dust filter unit 2, pressurizing air air pump 3 and vertical water tank 4.Dust filter unit and air dry oven aerofluxuss
Threeway airway 5 is provided between mouthful, in line gas switch 6 is respectively equipped with the escape pipe of threeway airway and post-treatment gas are opened
7 are closed, post processing airway 8 between dust filter unit and pressurizing air air pump, is provided with.Allowed when wherein dust filter unit works
Gas flow rate can not be too slow, can otherwise increase the work load of pressurizing air air pump.The inner bottom of vertical water tank is provided with multigroup drum
Bubble gas disk 9, each bubbling gas disk is connected with pressurizing air air pump by pressure soft air-guide pipe 10 accordingly, and vertical water tank top is provided with
The steam vent 12 for connecing outdoor exhaust fan and the water inlet pipe 13 for being passed through absorbing liquid, bottom is provided with waste liquid drain pipe 14.Pressure inducing QI is soft
Pipe is provided with fluid stopping valve array 15, and fluid stopping valve array is the array of multiple flow-stop valves grafting side by side.Pressure soft air-guide pipe can
Need to increase to 8～10 according to actual design, and internal diameter is between 3-5mm.The installation site of pressurizing air air pump is higher than vertical
Liquid level in formula water tank, when preventing fluid stopping defective valve, absorbing liquid is poured in down a chimney in pump.Water inlet draining for convenience, vertical water tank
Water route be upper intake lower outlet type, and dipperstick 16 can should be installed on water tank.And gas circuit is then bottom in and top out formula, gas leads to
Decomposing fragmentation effect and producing multigroup superfine bubble stream for bubbling gas disk is spent, bubble is abundant with absorbing liquid during rising
Contact, completes the absorption process of wherein organic substance, makes absorption process not to prevent bubble from merging during rising
Fully, upside arranging multiplayer fine metal mesh 11 as needed in water tank, when bubble runs into silk screen in uphill process then by
Splitting, rises to.In order to strengthen the general effect of operation, should
Equipment still has the space of extension, can install a series of adnexa, such as ultrasonic transducer 17 and impeller-agitator 18, in order to
Realize the recirculation containing micro-content organism bubble and the process such as air bubble ultrasound wave fragmentation, it is also possible to further extend this kind of gas with
The time of water contact, strengthen absorption process；Can be contained with install sensor, real-time monitoring temperature, gas flow, Organic substance in water matter
Amount etc..
Ultimate principle of the present utility model and principal character and advantage of the present utility model has been shown and described above.One's own profession
The technical staff of industry it should be appreciated that this utility model is not restricted to the described embodiments, described in above-described embodiment and description
Principle of the present utility model is described simply, on the premise of without departing from this utility model spirit and scope, this utility model is also
Various changes and modifications are had, these changes and improvements are both fallen within the range of claimed this utility model.This utility model
Claimed scope is by appending claims and its equivalent thereof.
Claims (5)
1. a kind of organic liquid volatile matter withdrawer for air dry oven, it is characterised in that：It is connected to air dry oven row
In QI KOU, it is made up of dust filter unit, pressurizing air air pump and vertical water tank, the dust filter unit and air dry oven air vent
Between be provided with threeway airway, be respectively equipped with the escape pipe of threeway airway in line gas switch and post-treatment gas switch,
It is provided with post processing airway between the dust filter unit and pressurizing air air pump, the inner bottom of the vertical water tank is provided with multigroup
Bubbling gas disk, each bubbling gas disk are connected with pressurizing air air pump by pressure soft air-guide pipe accordingly, the vertical water tank interior
In portion, upside is provided with multilamellar fine metal mesh, and top is provided with the steam vent for connecing outdoor exhaust fan and the water inlet pipe for being passed through absorbing liquid,
Bottom is provided with waste liquid drain pipe.
2. the organic liquid volatile matter withdrawer for air dry oven according to claim 1, it is characterised in that：Described
Pressure soft air-guide pipe is provided with flow-stop valve, and the flow-stop valve has multiple, and is combined into the form of array.
3. the organic liquid volatile matter withdrawer for air dry oven according to claim 1, it is characterised in that：Described
The quantity of pressure soft air-guide pipe and internal diameter are adjusted accordingly according to the difference of air dry oven model joined together and capacity.
4. the organic liquid volatile matter withdrawer for air dry oven according to claim 1, it is characterised in that：Described
Vertical water tank is additionally provided with dipperstick, ultrasonic transducer and impeller-agitator.
5. the organic liquid volatile matter withdrawer for air dry oven according to claim 1, it is characterised in that：Described
The installation site of pressurizing air air pump higher than the liquid level in vertical water tank, when preventing fluid stopping defective valve, pour in down a chimney into pump by absorbing liquid
Interior.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620907601.5U CN206008380U (en) | 2016-08-20 | 2016-08-20 | A kind of organic liquid volatile matter withdrawer for air dry oven |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620907601.5U CN206008380U (en) | 2016-08-20 | 2016-08-20 | A kind of organic liquid volatile matter withdrawer for air dry oven |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206008380U true CN206008380U (en) | 2017-03-15 |
Family
ID=58250082
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620907601.5U Expired - Fee Related CN206008380U (en) | 2016-08-20 | 2016-08-20 | A kind of organic liquid volatile matter withdrawer for air dry oven |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206008380U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108261867A (en) * | 2018-01-25 | 2018-07-10 | 深圳汇呈环保科技有限公司 | A kind of industrial dedusting device |
-
2016
- 2016-08-20 CN CN201620907601.5U patent/CN206008380U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108261867A (en) * | 2018-01-25 | 2018-07-10 | 深圳汇呈环保科技有限公司 | A kind of industrial dedusting device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20170315 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |