CN206045657U - Superfine micronic dust is filtered and acid-base neutralization system - Google Patents
Superfine micronic dust is filtered and acid-base neutralization system Download PDFInfo
- Publication number
- CN206045657U CN206045657U CN201620736153.7U CN201620736153U CN206045657U CN 206045657 U CN206045657 U CN 206045657U CN 201620736153 U CN201620736153 U CN 201620736153U CN 206045657 U CN206045657 U CN 206045657U
- Authority
- CN
- China
- Prior art keywords
- air inlet
- acid
- cooling tube
- inlet pipe
- base neutralization
- Prior art date
- 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
Links
- 239000000428 dust Substances 0.000 title claims abstract description 30
- 238000006386 neutralization reaction Methods 0.000 title claims abstract description 26
- 238000001816 cooling Methods 0.000 claims abstract description 55
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 43
- 238000010521 absorption reaction Methods 0.000 claims abstract description 24
- 238000009434 installation Methods 0.000 claims abstract description 11
- 238000000889 atomisation Methods 0.000 claims abstract description 9
- 239000007788 liquid Substances 0.000 claims description 14
- 125000004122 cyclic group Chemical group 0.000 claims description 11
- 230000000241 respiratory effect Effects 0.000 claims description 8
- 239000002253 acid Substances 0.000 claims description 6
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 claims description 5
- 229930006000 Sucrose Natural products 0.000 claims description 5
- 238000009835 boiling Methods 0.000 claims description 5
- 239000005720 sucrose Substances 0.000 claims description 5
- 230000037431 insertion Effects 0.000 claims description 3
- 238000003780 insertion Methods 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 8
- 238000009833 condensation Methods 0.000 abstract description 7
- 230000005494 condensation Effects 0.000 abstract description 7
- 239000000779 smoke Substances 0.000 abstract description 7
- 239000003595 mist Substances 0.000 abstract description 4
- 230000015572 biosynthetic process Effects 0.000 abstract description 3
- 238000002156 mixing Methods 0.000 abstract description 3
- 239000002585 base Substances 0.000 description 16
- 238000001914 filtration Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 231100000252 nontoxic Toxicity 0.000 description 2
- 230000003000 nontoxic effect Effects 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 210000003437 trachea Anatomy 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000003513 alkali Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
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- Separation Of Particles Using Liquids (AREA)
Abstract
This utility model is related to cleaner field, and specifically superfine micronic dust is filtered and acid-base neutralization system, including atomization condensing means, cooling back installation, absorption plant and acid-base neutralization device.Atomization condensing means include air inlet pipe, cooling tube, exhaustor, steam generator and air pump；The air inlet of cooling tube is connected with the gas outlet of air inlet pipe, and its gas outlet is connected with the air inlet of exhaustor；The middle part of air inlet pipe is passed through in a hole from cooling tube figure of eight helix；The output port of steam generator is connected with air inlet pipe, steam generator be used for produce steam and with gas mixing to be clean.Cooling back installation is coupled with cooling tube.Acid-base neutralization device is coupled with absorption plant.This utility model imitates the formation of mist in meteorology, is initially formed water smoke using small dust as the nuclei of condensation, then water smoke is condensed into water, dust and water is combined and is discharged, and the system principle is simple, and dust removing effects substantially, can be recycled, and cost is relatively low, is easy to promote.
Description
Technical field
This utility model is related to cleaner field, and specifically superfine micronic dust is filtered and acid-base neutralization system.
Background technology
The dust in air is filtered using filtration mesh screen more than existing dust arrester, to realize grit from gas
In separate the purpose for reaching purify air.Due to the filter effect for filtering the mesh screen granule dust minimum to diameter it is limited,
Dust of such as granule less than 0.005mm, it is difficult to reach the requirement of environment protection emission；In addition, traditional filter type is due to relying on
Filter is filtered to dust, it is ensured that certain filter effect, needs to change filter on time, even can after cleaning
The filter of recycling still has the number of times requirement of recycling, and the undoubtedly purification to air increases cost, and acid or alkali
The gas of property is filtered more unrealistic by screen cloth.
Utility model content
For technical problem of the prior art, this utility model provides superfine micronic dust and filters and acid-base neutralization system,
The system imitates the formation of mist in meteorology, is initially formed water smoke using small dust as the nuclei of condensation, then water smoke is condensed into water, make
Dust and water are combined and are discharged, and the system principle is simple, and dust removing effects substantially, can be recycled, and cost is relatively low, are easy to promote.
This utility model solves the technical scheme adopted by its technical problem：Superfine micronic dust is filtered and acid-base neutralization system
System, including atomization condensing means, cooling back installation, absorption plant and acid-base neutralization device.Set inside described absorption plant
Absorbing liquid, and the liquid level of absorbing liquid are equipped with less than the height of absorption plant inner chamber.
Described atomization condensing means include air inlet pipe, cooling tube, exhaustor, steam generator and air pump；Described is cold
But pipe is linear in three-dimensional spiral, and the top view of cooling tube is in the figure of eight, the air inlet of cooling tube and the gas outlet company of air inlet pipe
Connect, and the gas outlet of cooling tube is connected with the air inlet of exhaustor, the air inlet of the cooling tube is located above gas outlet；It is described enter
The middle part of trachea is passed through in a hole from cooling tube figure of eight helix, and the air to sucking first is preheated, air inlet pipe
Head end be provided with air pump, and air inlet pipe end is provided with steam generator；Described aerofluxuss pipe end insertion absorption plant
In absorbing liquid, for collecting and absorbing the waste liquid of condensation, and aerofluxuss pipe end is in toroidal, makes absorption more thorough；Described
The output port of steam generator is connected with air inlet pipe, steam generator be used for produce steam and with gas mixing to be clean.
Described cooling back installation is coupled with cooling tube.
Described acid-base neutralization device is coupled with absorption plant, input channel that acid-base neutralization device includes being sequentially connected,
Acid respiratory box, alkaline respiratory box and output channel；Described input channel is connected with the delivery outlet of absorption plant.
Preferably, described cooling back installation includes external pipeline, water pump, cyclic water tank and dividing plate；Described is external
Pipeline is passed through in another hole from cooling tube figure of eight helix, and the two ends of the external pipeline are connected with cyclic water tank respectively
It is logical；Described water pump is arranged on external pipeline；Described dividing plate is arranged in cyclic water tank and is separated into multiple connections
Cell, be easy to the cooling of water in cyclic water tank.
Preferably, aqueous sucrose solution is loaded with inside described steam generator, for improving the boiling point of water so that steam
Temperature is higher, so cause unit volume in steam content it is higher, the steam generator output port is provided with and prevents boiling water from splashing
Enter the guard of air inlet pipe, it is to avoid boiling water is combined with dust rear and flows back to steam generator, and the nontoxic cost of aqueous sucrose solution
It is low, and container will not be corroded.
The beneficial effects of the utility model are：
(1) superfine micronic dust of the present utility model is filtered and acid-base neutralization system, and the system imitates the formation of mist in meteorology, will
Small dust is initially formed water smoke as the nuclei of condensation, then water smoke is condensed into water, dust and water is combined and is discharged, and the system is former
Reason is simple, and dust removing effects substantially, can be recycled, and cost is relatively low, is easy to promote；
(2) superfine micronic dust of the present utility model is filtered and acid-base neutralization system, air to be clean with steam it
Before, first from cooling tube hub through energy exchange is carried out, to reach the effect of cooling tube cooling and air preheat to be clean,
On the one hand make capacity usage ratio higher, on the other hand, when after air preheat to be clean with steam, the range of decrease at a temperature of steam
Degree reduces, it is to avoid mixed gas are atomized too early, is formed after the globule is attached to tube wall and is flowed in steam generator；
(3) superfine micronic dust of the present utility model is filtered and acid-base neutralization system, and cooling tube is designed to " 8 " word, facilitates air inlet
Pipe and external pipeline are passed through, and avoid the energy exchange between both.
Description of the drawings
With reference to the accompanying drawings and examples this utility model is further illustrated.
Fig. 1 is structural representation of the present utility model；
In figure：Atomization condensing means (1), cooling back installation (2), absorption plant (3), acid-base neutralization device (4), air inlet
Pipe (11), cooling tube (12), exhaustor (13), steam generator (14), air pump (15), external pipeline (21), water pump (22), follow
Ring water tank (23), dividing plate (24), input channel (41), acid respiratory box (42), alkaline respiratory box (43), output channel (44),
Guard (141).
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 specific embodiment, and this utility model is expanded on further.
Such as Fig. 1, the superfine micronic dust of the present embodiment is filtered and acid-base neutralization system, including atomization condensing means 1, circulating cooling
Device 2, absorption plant 3 and acid-base neutralization device 4.Described absorption plant 3 is internally provided with absorbing liquid, and the liquid level of absorbing liquid
Highly less than the height of 3 inner chamber of absorption plant.
Described atomization condensing means 1 include air inlet pipe 11, cooling tube 12, exhaustor 13, steam generator 14 and air pump
15；Described cooling tube 12 is linear in three-dimensional spiral, and the top view of cooling tube 12 is in the figure of eight, the air inlet of cooling tube 12
It is connected with the gas outlet of air inlet pipe 11, and the gas outlet of cooling tube 12 is connected with the air inlet of exhaustor 13, the cooling tube 12
Air inlet is located above gas outlet；Wear in a hole from 12 figure of eight helix of cooling tube at the middle part of the air inlet pipe 11
Cross, the air to sucking first is preheated, and the head end of air inlet pipe 11 is provided with air pump 15, and 11 end of air inlet pipe is provided with steam
Generator 14；In the absorbing liquid of described 13 end of exhaustor insertion absorption plant, for collecting and absorbing the waste liquid of condensation, and
13 end of exhaustor is in toroidal, makes absorption more thorough；The output port of described steam generator 14 is connected with air inlet pipe 11
It is logical, steam generator 14 be used to producing steam and with gas mixing to be clean, be loaded with sucrose water inside steam generator 14
Solution, the nontoxic low cost of aqueous sucrose solution, and container will not be corroded, the boiling point of water can be improved so that vapor (steam) temperature is more
Height, and then cause vapour density bigger, the water smoke density of condensation also can be bigger, and 14 output port of steam generator is provided with anti-
Defervescence water is splashed into the guard 141 of air inlet pipe 11.
Described cooling back installation 2 is coupled with cooling tube 12, cooling back installation 2 include external pipeline 21, water pump 22,
Cyclic water tank 23 and dividing plate 24；Described external pipeline 21 is passed through in another hole from 12 figure of eight helix of cooling tube,
The two ends of the external pipeline 21 are connected with cyclic water tank 23 respectively；Described water pump 22 is arranged on external pipeline 21；Described
Dividing plate 24 is arranged in cyclic water tank 23 and is separated into the cell of multiple connections, is easy to the cooling of water in cyclic water tank 23.
Input channel 41 that described acid-base neutralization device 4 includes being sequentially connected, acid respiratory box 42, alkaline respiratory box 43
With output channel 44；Described input channel 41 is connected with the delivery outlet of absorption plant 3.
The superfine micronic dust of embodiment filter and acid-base neutralization system when in use, air to be clean by air pump 15 be pressed into into
In trachea 11, before with steam, first pass through from 12 center of cooling tube, due to the temperature of cooling tube 12 it is higher, it is to be clean
Air carry out energy exchange with the gas mixed in cooling tube 12, with reach cooling tube cooling and air preheat to be clean
Effect, when after air preheat to be clean with steam, at a temperature of steam range of decrease degree reduce, it is to avoid the too early mist of mixed gas
Change, formed after the globule is attached to tube wall and flowed in steam generator；21 internal flow of external pipeline of cooling back installation 2 cold
Water, is made the water vapor condensation in cooling tube 12 and is combined with dust, is then flowed in absorption plant 3；The outfan of absorption plant 3
Acid-base neutralization device 4 is added, the acid or alkaline gas in gas can be neutralized.
Ultimate principle of the present utility model, principal character and advantage has been shown and described above.The technical staff of the industry
It should be appreciated that this utility model is not restricted to the described embodiments, the description in above-mentioned embodiment and description is to say
Bright principle of the present utility model, on the premise of without departing from this utility model spirit and scope, this utility model also has various
Changes and improvements, these changes and improvements are both fallen within the claimed scope of this utility model.This utility model is claimed
Scope is by appending claims and its equivalent thereof.
Claims (3)
1. superfine micronic dust is filtered and acid-base neutralization system, it is characterised in that：Including atomization condensing means (1), cooling back installation
(2), absorption plant (3) and acid-base neutralization device (4)；Wherein：
Described absorption plant (3) is internally provided with absorbing liquid, and the liquid level of absorbing liquid less than absorption plant (3) inner chamber
Highly；
Described atomization condensing means (1) include air inlet pipe (11), cooling tube (12), exhaustor (13), steam generator (14)
With air pump (15)；Described cooling tube (12) is linear in three-dimensional spiral, and the top view of cooling tube (12) is in the figure of eight, is cooled down
The air inlet of pipe (12) is connected with the gas outlet of air inlet pipe (11), and the air inlet of the gas outlet of cooling tube (12) and exhaustor (13)
Mouth connection, the air inlet of the cooling tube (12) are located above gas outlet；The middle part of the air inlet pipe (11) is from cooling tube (12) " 8 "
Pass through in a hole in font helix, the head end of air inlet pipe (11) is provided with air pump (15), and air inlet pipe (11) end sets
It is equipped with steam generator (14)；In the absorbing liquid of described exhaustor (13) end insertion absorption plant, and exhaustor (13) end
End is in toroidal；The output port of the steam generator (14) is connected with air inlet pipe (11)；
Described cooling back installation (2) is coupled with cooling tube (12)；
Described acid-base neutralization device (4) is coupled with absorption plant (3), and acid-base neutralization device (4) is including the input being sequentially connected
Pipeline (41), acid respiratory box (42), alkaline respiratory box (43) and output channel (44)；Described input channel (41) and absorption
The delivery outlet connection of device (3).
2. superfine micronic dust according to claim 1 is filtered and acid-base neutralization system, it is characterised in that：Described circulating cooling
Device (2) includes external pipeline (21), water pump (22), cyclic water tank (23) and dividing plate (24)；Described external pipeline (21) from
Pass through in another hole in cooling tube (12) figure of eight helix, the two ends of the external pipeline (21) respectively with cyclic water tank
(23) connect；Described water pump (22) is arranged on external pipeline (21)；Described dividing plate (24) is arranged on cyclic water tank (23)
Cell that is interior and being separated into multiple connections.
3. superfine micronic dust according to claim 1 is filtered and acid-base neutralization system, it is characterised in that：Described steam generation
Aqueous sucrose solution is loaded with inside device (14), the steam generator (14) output port is provided with and prevents boiling water to be splashed into air inlet pipe
(11) guard (141).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620736153.7U CN206045657U (en) | 2016-07-13 | 2016-07-13 | Superfine micronic dust is filtered and acid-base neutralization system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620736153.7U CN206045657U (en) | 2016-07-13 | 2016-07-13 | Superfine micronic dust is filtered and acid-base neutralization system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206045657U true CN206045657U (en) | 2017-03-29 |
Family
ID=58377259
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620736153.7U Expired - Fee Related CN206045657U (en) | 2016-07-13 | 2016-07-13 | Superfine micronic dust is filtered and acid-base neutralization system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206045657U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106039883A (en) * | 2016-07-13 | 2016-10-26 | 方龙旺 | Ultrafine micro dust filtering and acid-base neutralizing system |
| CN107051121A (en) * | 2017-05-27 | 2017-08-18 | 佛山市三水万瑞达环保科技有限公司 | A kind of gas humidification purifier |
-
2016
- 2016-07-13 CN CN201620736153.7U patent/CN206045657U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106039883A (en) * | 2016-07-13 | 2016-10-26 | 方龙旺 | Ultrafine micro dust filtering and acid-base neutralizing system |
| CN107051121A (en) * | 2017-05-27 | 2017-08-18 | 佛山市三水万瑞达环保科技有限公司 | A kind of gas humidification purifier |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170329 Termination date: 20170713 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |