CN206424740U - A kind of high-efficient oil smoke piece-rate system - Google Patents
A kind of high-efficient oil smoke piece-rate system Download PDFInfo
- Publication number
- CN206424740U CN206424740U CN201720107725.XU CN201720107725U CN206424740U CN 206424740 U CN206424740 U CN 206424740U CN 201720107725 U CN201720107725 U CN 201720107725U CN 206424740 U CN206424740 U CN 206424740U
- Authority
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- China
- Prior art keywords
- oil smoke
- adsorption tower
- pipeline
- separation circulation
- liquid case
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- 239000000779 smoke Substances 0.000 title claims abstract description 37
- 239000007788 liquid Substances 0.000 claims abstract description 59
- 238000000926 separation method Methods 0.000 claims abstract description 36
- 238000001179 sorption measurement Methods 0.000 claims abstract description 27
- 238000010521 absorption reaction Methods 0.000 claims abstract description 19
- 239000002699 waste material Substances 0.000 claims abstract description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 10
- 241000628997 Flos Species 0.000 claims abstract description 9
- 239000000446 fuel Substances 0.000 claims abstract description 4
- 239000012190 activator Substances 0.000 claims description 10
- 239000012530 fluid Substances 0.000 claims description 3
- 238000004140 cleaning Methods 0.000 abstract description 5
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 238000011084 recovery Methods 0.000 abstract description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 239000007789 gas Substances 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 239000006096 absorbing agent Substances 0.000 description 2
- 239000006233 lamp black Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 238000000889 atomisation Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 235000014121 butter Nutrition 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000005055 memory storage Effects 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 238000007127 saponification reaction Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a kind of high-efficient oil smoke piece-rate system, including adsorption tower and separation circulation liquid case, access has oil smoke inlet attack in the middle of the side wall of adsorption tower, the bottom of adsorption tower is connected to separation circulation liquid case by pipeline, the top of described adsorption tower is connected with cyclone separator by pipeline, the bottom of cyclone separator is connected to separation circulation liquid case by pipeline, the top of cyclone separator is connected with clean air discharge tube, absorption nozzle for liquid is installed, absorption nozzle for liquid is connected to separation circulation liquid case by pipeline and circulating pump in adsorption tower；Activated carbon filter layer is installed in described clean air discharge tube；It is connected with described separation circulation liquid case on waste oil floss hole, waste oil floss hole and fuel outlet valve is installed；Beneficial effect：Practicality, production cost is low, rational in infrastructure, realizes that oil smoke is separated, cleaning efficiency is high, without cleaning, realizes the stable qualified discharge of oil smoke, and the waste oil of recovery can also be comprehensively utilized, and save resource.
Description
Technical field
The utility model is related to a kind of oil-fume separating device, more particularly to a kind of high-efficient oil smoke piece-rate system.
Background technology
Lampblack absorber is the necessary equipment of catering industry, in order to ensure the workplace air quality such as kitchen, it is necessary to operation
During the oil smoke that produces and air mixture be discharged into outdoor, but the directly outer row of oil smoke will bring unfavorable to Outdoor Air Quality again
Influence.It is reported that the oil smoke of light catering industry is 6%~13% to the contribution rate of atmosphere pollution.
Current oil smoke separation equipment has electric smoke abatement, filtering, absorption etc., there is easy fouling, blocking, the cleaning frequency is short, cleans
The defect such as difficulty is big.Actual operational percentage is relatively low, most of periods, and oil smoke is in discharge beyond standards state.
Utility model content
Technical problem to be solved in the utility model is that there is provided a kind of separation of high-efficient oil smoke in view of the shortcomings of the prior art
System.
To achieve these goals, the measure that the utility model is taken：
There is access in the middle of a kind of high-efficient oil smoke piece-rate system, including adsorption tower and separation circulation liquid case, the side wall of adsorption tower
Oil smoke inlet attack, the bottom of adsorption tower is connected to separation circulation liquid case by pipeline, and the top of described adsorption tower passes through pipe
Road is connected with cyclone separator, and the bottom of cyclone separator is connected to separation circulation liquid case by pipeline, cyclone separator it is upper
Portion, which is connected with clean air discharge tube, adsorption tower, is provided with absorption nozzle for liquid, and absorption nozzle for liquid passes through pipeline and circulating pump
It is connected to separation circulation liquid case；
Activated carbon filter layer is installed in described clean air discharge tube；
It is connected with described separation circulation liquid case on waste oil floss hole, waste oil floss hole and fuel outlet valve is installed；
Described separation circulation liquid case is connected with activator solution case by pipeline, and activator pump is provided with the pipeline；
Demister is installed in described adsorption tower；
The setting height(from bottom) of described absorption nozzle for liquid is higher than the height of oil smoke inlet attack, and the setting height(from bottom) of demister is higher than
Adsorb the height of nozzle for liquid.
The beneficial effects of the utility model：Practicality, production cost is low, rational in infrastructure, realizes that oil smoke is separated, cleaning efficiency
Height, without cleaning, realizes the stable qualified discharge of oil smoke, the waste oil of recovery can also be comprehensively utilized, and save resource.
Brief description of the drawings
Fig. 1, planar structure schematic diagram of the present utility model.
Embodiment
Accessed in the middle of a kind of high-efficient oil smoke piece-rate system, including adsorption tower 1 and separation circulation liquid case 7, the side wall of adsorption tower 1
There is an oil smoke inlet attack 9, the bottom of adsorption tower 1 is connected to separation circulation liquid case 7 by pipeline, the top of described adsorption tower 1
Cyclone separator 2 is connected with by pipeline, the bottom of cyclone separator 2 is connected to separation circulation liquid case 7, whirlwind point by pipeline
From device 2 top be connected with clean air discharge tube 10, adsorption tower 1 be provided with absorption nozzle for liquid 11, adsorb nozzle for liquid 11
Separation circulation liquid case 7 is connected to by pipeline and circulating pump 8.
Activated carbon filter layer 3 is installed in described clean air discharge tube 10.
It is connected with described separation circulation liquid case 7 on waste oil floss hole 12, waste oil floss hole 12 and fuel outlet valve 4 is installed.
Described separation circulation liquid case 7 is connected with activator solution case 5 by pipeline, and activator pump is provided with the pipeline
6。
Demister 13 is installed in described adsorption tower 1.
The setting height(from bottom) of described absorption nozzle for liquid 11 is higher than the height of oil smoke inlet attack 9, and the installation of demister 13 is high
Height of the degree higher than absorption nozzle for liquid 11.
The flow direction of oil smoke, air mixture：Oil smoke, the air mixture of lampblack absorber discharge, first, by oil smoke inlet attack
9 enter in adsorption tower 1, the absorbing liquid (separation circulation fluid) of the absorption sprinkling atomization of nozzle for liquid 11 in adsorption tower 1, in mixture
Oil smoke small droplet is absorbed by liquid absorption, and big drop is become by droplet, most of to enter with absorbing liquid in separation circulation liquid case 7.
Still there is a small amount of drop in gas after preliminary oil removing, entered immediately by pipeline in cyclone separator 2, carry out further gas-liquid
Separation, substantially clean gas is after cyclone dust collectors 2 come out, through activated carbon filter layer 3, adsorbs after pernicious gas therein,
The air for becoming clean discharges outdoor by clean air discharge tube 10.
Absorbing liquid (separation circulation fluid) is flowed to：After absorbing liquid is pressurizeed through circulating pump 8, into the adsorption liquid spray in adsorption tower 1
Mouth 11, and absorption nozzle for liquid 11 in be atomized after spray, surface area drastically expands, after contact with oil smoke air mixture, send out
Raw suction-operated, the big portion of liquid after absorption flows downwardly into separation circulation liquid case 7, and the absorbing liquid of fraction leaves absorption with gas
Tower 1, into cyclone separator 2, is separated further, the absorbing liquid being separated is through cyclone separator 2 in cyclone separator 2
The water seal arrangement of bottom, flow back to separation circulation liquid case 7 in, separation circulation liquid case 7 in oil water separator (can using gravity type,
Air-flotation type, centrifugal etc.), the absorbing liquid after separation is again introduced into circulating pump 8 and carried out in next round circulation, separation circulation liquid case 7
Waste oil, through waste oil floss hole 12 periodically reclaim after, saponification liquor, butter etc. can be processed into and reused.
Liquid replenishing function：When liquid level is too low in separation circulation liquid case 7, the activator solution of the memory storage of activator solution case 5,
Entered by activator pump 6 in separation circulation liquid case 7, the supplement suitably matched.
Absorption principle：Activator molecule one end is polar structure (hydrophilic), and another upper end is non-polar conformations (oleophylic), in work
In the presence of agent, oil smoke and part organic exhaust gas and water are combined into emulsion, so as to be absorbed.After oil smoke contact absorbing liquid,
Into oil-in-water (being surrounded around oil droplet by water droplet) or Water-In-Oil (being surrounded around water droplet by oil droplet), the adhesion between drop is significantly
Weaken, and whole system runner is unimpeded straight, therefore scale formation can be eliminated, it need not also clean substantially.
Claims (6)
1. in the middle of a kind of high-efficient oil smoke piece-rate system, including adsorption tower (1) and separation circulation liquid case (7), the side wall of adsorption tower (1)
Access has oil smoke inlet attack (9), and the bottom of adsorption tower (1) is connected to separation circulation liquid case (7) by pipeline, and its feature exists
In：The top of described adsorption tower (1) is connected with cyclone separator (2) by pipeline, and the bottom of cyclone separator (2) passes through pipe
Road is connected to separation circulation liquid case (7), and the top of cyclone separator (2) is connected with clean air discharge tube (10), adsorption tower
(1) absorption nozzle for liquid (11) is installed, absorption nozzle for liquid (11) is connected to separation circulation liquid case by pipeline and circulating pump (8) in
(7)。
2. a kind of high-efficient oil smoke piece-rate system according to claim 1, it is characterised in that：Described clean air delivery pipe
Activated carbon filter layer (3) is installed in road (10).
3. a kind of high-efficient oil smoke piece-rate system according to claim 1 or 2, it is characterised in that：Described separation circulation fluid
It is connected with case (7) on waste oil floss hole (12), waste oil floss hole (12) and fuel outlet valve (4) is installed.
4. a kind of high-efficient oil smoke piece-rate system according to claim 3, it is characterised in that：Described separation circulation liquid case
(7) it is connected with by pipeline on activator solution case (5), the pipeline and activator pump (6) is installed.
5. a kind of high-efficient oil smoke piece-rate system according to claim 4, it is characterised in that：Pacify in described adsorption tower (1)
Equipped with demister (13).
6. a kind of high-efficient oil smoke piece-rate system according to claim 5, it is characterised in that：Described absorption nozzle for liquid (11)
Setting height(from bottom) be higher than the height of oil smoke inlet attack (9), the setting height(from bottom) of demister (13) is higher than absorption nozzle for liquid (11)
Highly.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720107725.XU CN206424740U (en) | 2017-01-22 | 2017-01-22 | A kind of high-efficient oil smoke piece-rate system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720107725.XU CN206424740U (en) | 2017-01-22 | 2017-01-22 | A kind of high-efficient oil smoke piece-rate system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206424740U true CN206424740U (en) | 2017-08-22 |
Family
ID=59591529
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720107725.XU Active CN206424740U (en) | 2017-01-22 | 2017-01-22 | A kind of high-efficient oil smoke piece-rate system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206424740U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107715646A (en) * | 2017-11-23 | 2018-02-23 | 福建福源凯美特气体有限公司 | Waste gas liquid mixture processing unit in reciprocating pump or compressor central cavity |
| CN110433597A (en) * | 2019-07-29 | 2019-11-12 | 杭州鼎飞数控科技有限公司 | A kind of oil smoke prepurifier |
| CN112170427A (en) * | 2020-09-08 | 2021-01-05 | 山西华鑫肥业股份有限公司 | Centrifugal compressor and oil smoke discharge system |
| CN115999293A (en) * | 2022-12-20 | 2023-04-25 | 铜陵市卓翔铜材科技有限公司 | Device and method for reducing emission of dioxin in organic coating pyrolysis flue gas |
| CN121222222A (en) * | 2025-12-01 | 2025-12-30 | 湘潭大学 | A long-term treatment method and equipment for restaurant fumes |
-
2017
- 2017-01-22 CN CN201720107725.XU patent/CN206424740U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107715646A (en) * | 2017-11-23 | 2018-02-23 | 福建福源凯美特气体有限公司 | Waste gas liquid mixture processing unit in reciprocating pump or compressor central cavity |
| CN110433597A (en) * | 2019-07-29 | 2019-11-12 | 杭州鼎飞数控科技有限公司 | A kind of oil smoke prepurifier |
| CN112170427A (en) * | 2020-09-08 | 2021-01-05 | 山西华鑫肥业股份有限公司 | Centrifugal compressor and oil smoke discharge system |
| CN115999293A (en) * | 2022-12-20 | 2023-04-25 | 铜陵市卓翔铜材科技有限公司 | Device and method for reducing emission of dioxin in organic coating pyrolysis flue gas |
| CN121222222A (en) * | 2025-12-01 | 2025-12-30 | 湘潭大学 | A long-term treatment method and equipment for restaurant fumes |
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