CN206381764U - Oil removing dedusting and purifying device - Google Patents
Oil removing dedusting and purifying device Download PDFInfo
- Publication number
- CN206381764U CN206381764U CN201621232056.0U CN201621232056U CN206381764U CN 206381764 U CN206381764 U CN 206381764U CN 201621232056 U CN201621232056 U CN 201621232056U CN 206381764 U CN206381764 U CN 206381764U
- Authority
- CN
- China
- Prior art keywords
- oil
- purifying device
- baffle plate
- oil removing
- triple valve
- 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
- 238000001514 detection method Methods 0.000 claims abstract description 23
- 239000000126 substance Substances 0.000 claims abstract description 12
- 230000003139 buffering effect Effects 0.000 claims abstract description 9
- 230000001413 cellular effect Effects 0.000 claims abstract description 4
- 239000011521 glass Substances 0.000 claims abstract description 4
- 229920005989 resin Polymers 0.000 claims description 3
- 239000011347 resin Substances 0.000 claims description 3
- 239000012717 electrostatic precipitator Substances 0.000 abstract description 8
- 239000000428 dust Substances 0.000 abstract description 7
- 239000000779 smoke Substances 0.000 abstract description 5
- 238000010276 construction Methods 0.000 abstract 1
- 239000003344 environmental pollutant Substances 0.000 abstract 1
- 231100000719 pollutant Toxicity 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 239000002912 waste gas Substances 0.000 description 8
- 238000001816 cooling Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 230000008901 benefit Effects 0.000 description 1
- 239000000872 buffer Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000009881 electrostatic interaction Effects 0.000 description 1
- 230000005713 exacerbation Effects 0.000 description 1
- 239000011152 fibreglass Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Electrostatic Separation (AREA)
Abstract
The utility model provides a kind of oil removing dedusting and purifying device, includes air blower, condenser, primary cyclone, primary heater, one-level oil expeller, detection meter a, drier, electrostatic precipitator, detection meter b and buffering air accumulator successively according to the pipeline order of connection.The primary cyclone bottom connects chemical oil remover, the chemical oil remover outlet connection condenser.The one-level oil expeller internal vertical sets multistage baffle plate, and the baffle plate is waveform, and the baffle plate both side surface is cellular, and the baffle plate is sandwiched between ultrafine nanometer all-glass paper.The pollutants such as dust, the oil smoke described in the utility model effectively gone in removing exhaust gas, it is simple in construction, easy to operate, it is applied widely.
Description
Technical field
The utility model belongs to purifier field, more particularly, to a kind of oil removing dedusting and purifying device.
Background technology
With expanding economy, atmosphere pollution is increasingly serious, contains substantial amounts of suspended particulate, powder in the waste gas of industry manufacture
Dirt and oil smoke etc., are directly discharged to the environment on severe exacerbation periphery in air, life to people and healthy all cause
Harm, so needing to carry out it filtration treatment before waste gas discharge, removes the harmful substances such as dust therein and oil smoke.
The content of the invention
In view of this, the utility model is directed to a kind of oil removing dedusting and purifying device, to remove dust, the oil in removing exhaust gas
The harmful substances such as cigarette, purify air.
To reach above-mentioned purpose, what the technical solution of the utility model was realized in：
Oil removing dedusting and purifying device, air blower, condenser, one cyclonic are included according to the pipeline order of connection and is separated successively
Device, primary heater, one-level oil expeller, detection meter a, drier, electrostatic precipitator, detection meter b and buffering air accumulator.
Further, the primary cyclone bottom connection chemical oil remover, chemical oil remover outlet connection
The condenser, the water chemically separated in oil expeller is available for condenser to be used as recirculated water, effectively save cost.
Further, the one-level oil expeller internal vertical sets multistage baffle plate, and the baffle plate is waveform, the baffle plate
Both side surface is cellular, and the baffle plate is sandwiched between ultrafine nanometer all-glass paper.
Further, the detection meter a outlet connections triple valve I, the another two port of triple valve I connects two grades respectively
Some floor height oil-absorbing resins are set inside oil expeller entrance and the drier entrance, two grades of oil expellers, and detection meter a can be examined
Survey whether oil content residual in air reaches standard, such as not up to standard value can control triple valve I and air is passed through into two grades of oil expellers
Interior further purification.
Further, the drier is at least arranged in series two.
Further, the detection meter b outlet connections triple valve II, the another two port of triple valve II connects two respectively
Level cyclone inlet and buffering air accumulator entrance, the detection meter b can be carried out to the moisture content and granularity remained in air
Air, if testing result is up to standard, can be passed through in buffering air accumulator, such as testing result is below standard, then passes through threeway by detection
Air is passed through after secondary cyclone, secondary heater by valve II, and drier is passed through again and electrostatic precipitator is purified.
Further, the secondary cyclone outlet connection secondary heater entrance, the secondary heater outlet
Triple valve III is connected, the another two port of triple valve III connects drier entrance and triple valve I respectively.
Relative to prior art, oil removing dedusting and purifying device described in the utility model has the advantage that：
(1) dirt such as dust, oil smoke that oil removing dedusting and purifying device described in the utility model can be effectively gone in removing exhaust gas
Thing is contaminated, internal system detection means can ensure that purification produces a desired effect.
(2) oil removing dedusting and purifying device described in the utility model is cost-effective, easy to operate, applied widely.
Brief description of the drawings
Constitute a part of accompanying drawing of the present utility model to be used for providing further understanding to of the present utility model, this practicality is new
The schematic description and description of type is used to explain the utility model, does not constitute to improper restriction of the present utility model.
In accompanying drawing：
Fig. 1 is the oil removing dedusting and purifying device structural representation described in the utility model embodiment.
Description of reference numerals：
1- air blowers；2- condensers；3- primary cyclones；31- chemical oil removers；4- primary heaters；5- one-levels
Oil expeller；51- baffle plates；6- detection meters a；61- triple valves I；Bis- grades of oil expellers of 62-；7- driers；8- electrostatic precipitator；9- is examined
Survey meter b；92- triple valves II；93- secondary cyclones；93- secondary heaters；94- triple valves III；10- buffers air accumulator.
Embodiment
It should be noted that in the case where not conflicting, the feature in embodiment and embodiment in the utility model can
To be mutually combined.
Describe the utility model in detail below with reference to the accompanying drawings and in conjunction with the embodiments.
Oil removing dedusting and purifying device, air blower 1, condenser 2, one cyclonic are included according to the pipeline order of connection and is separated successively
Device 3, primary heater 4, one-level oil expeller 5, detection meter a6, drier 7, electrostatic precipitator 8, detection meter b9 and buffering air accumulator
10。
The bottom of primary cyclone 3 connects chemical oil remover 31, and the outlet of chemical oil remover 31 connection is described
Condenser 2, the water separated from the chemical oil remover 31 is available for the condenser 2 to be used as recirculated water, effectively section
About cost.
The internal vertical of one-level oil expeller 5 sets multistage baffle plate 51, and the baffle plate 51 is waveform, 51 liang of the baffle plate
Side surface is cellular, and the baffle plate 51 is sandwiched between ultrafine nanometer all-glass paper.
The detection meter a6 outlet connections triple valve I 61, the another two port of triple valve I 61 connects two grades of oil removings respectively
The entrance of device 62 and the entrance of the drier 7, the inside of two grades of oil expellers 62 set some floor height oil-absorbing resins, and detection meter a6 can
Whether oil content residual reaches standard in detection air, such as not up to standard value controllable triple valve I 61 air is passed through as described in two
Further purified in level oil expeller 62.
The drier 7 is at least arranged in series two.
The detection meter b9 outlet connections triple valve II 91, the another two port of triple valve II 91 connects two grades of rotations respectively
The entrance of wind separator 92 and the entrance of buffering air accumulator 10, the detection meter b9 can be to the moisture content and granularity that are remained in air
Detected, if testing result is up to standard, air can be passed through in the buffering air accumulator 10, such as testing result is below standard,
Then air is passed through after secondary cyclone 92, secondary heater 93 by the triple valve II 91, is passed through again described dry
Dry device 7 and the electrostatic precipitator 8 are purified.
The outlet of the secondary cyclone 92 connection entrance of secondary heater 93, the outlet of secondary heater 93 connection
Triple valve III 94, the another two port of triple valve III 94 connects the entrance of drier 7 and triple valve I 61 respectively.
The workflow of the present embodiment：
Waste gas is passed through in condenser 2, EGT is reduced by cooling circulating water, makes the mist of oil water smoke in waste gas etc. cold
It is solidifying, larger particles are agglomerated into, waste gas is passed through primary cyclone 3 afterwards, the centrifugal force produced in the presence of cyclone can
The impurity and drop of heavier mass in waste gas is thrown away and is attached on wall, realize gas-liquid separation, the waste water of discharge is by changing
Learn oil expeller 31 and carry out water-oil separating, the water isolated is passed through condenser 2 and used as cooling circulating water.Waste gas is led to afterwards
Enter primary heater 4, heat the entrained oil droplet in waste gas and be dispersed into mist of oil shape, one-level oil expeller 5 is passed through afterwards, in multistage gear
Under the filtering of plate 51 and ultra-fine fibre glass paper, residual can be effectively removed.Afterwards by detecting that meter a detects that Oil in circulating gas part is remained
It is whether exceeded, if exceeded, then by controlling triple valve I 61 that gas is passed through in two grades of oil expellers 62, carry out further net
Change.Gas is passed through in drier 7 afterwards, the moisture in gas adsorbed by molecular sieve etc., multiple-stage drier is set,
It can ensure that drying effect.Gas is passed through electrostatic precipitator 8 after oil removing water removal, by electrostatic interaction by the dust granules in gas
Be adsorbed onto on minus plate and positive plate, effectively remove dust granules in gas, enter afterwards detection meter b to the moisture content in gas and
Micronic dust detected, as testing result is up to standard, and the clean gas filtered is passed through in caching air accumulator 10 and preserved, is such as detected
As a result it is below standard, then gas is passed through after secondary cyclone 92 and secondary heater 93 by triple valve II 91, control three
Gas is passed through drier 7 by port valve III 94 again and electrostatic precipitator 8 carries out secondary filter.
Preferred embodiment of the present utility model is the foregoing is only, it is all at this not to limit the utility model
Within the spirit and principle of utility model, any modification, equivalent substitution and improvements made etc. should be included in the utility model
Protection domain within.
Claims (7)
1. oil removing dedusting and purifying device, it is characterised in that：Include air blower (1), condenser successively according to the pipeline order of connection
(2), primary cyclone (3), primary heater (4), one-level oil expeller (5), detection meter a (6), drier (7), electrostatic are removed
Dirt device (8), detection meter b (9) and buffering air accumulator (10).
2. oil removing dedusting and purifying device according to claim 1, it is characterised in that：Primary cyclone (3) bottom
Portion's connection chemical oil remover (31), chemical oil remover (31) the outlet connection condenser (2).
3. oil removing dedusting and purifying device according to claim 1, it is characterised in that：Hung down inside the one-level oil expeller (5)
Straight to set multistage baffle plate (51), the baffle plate (51) is waveform, and baffle plate (51) both side surface is cellular, the baffle plate
(51) it is sandwiched between ultrafine nanometer all-glass paper.
4. oil removing dedusting and purifying device according to claim 1, it is characterised in that：Detection meter a (6) outlet connection three
Port valve I (61), (61) another two port of triple valve I connects two grades of oil expeller (62) entrances and the drier (7) respectively
Some floor height oil-absorbing resins are set inside entrance, two grades of oil expellers (62).
5. oil removing dedusting and purifying device according to claim 1, it is characterised in that：The drier (7) is at least connected and set
Put two.
6. oil removing dedusting and purifying device according to claim 1, it is characterised in that：Detection meter b (9) outlet connection three
Port valve II (91), (91) another two port of triple valve II connects secondary cyclone (92) entrance and buffering gas storage respectively
Tank (10) entrance.
7. oil removing dedusting and purifying device according to claim 6, it is characterised in that：The secondary cyclone (92) goes out
Mouth connection secondary heater (93) entrance, secondary heater (93) the outlet connection triple valve III (94), the triple valve III
(94) another two port connects drier (7) entrance and triple valve I (61) respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621232056.0U CN206381764U (en) | 2016-11-16 | 2016-11-16 | Oil removing dedusting and purifying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621232056.0U CN206381764U (en) | 2016-11-16 | 2016-11-16 | Oil removing dedusting and purifying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206381764U true CN206381764U (en) | 2017-08-08 |
Family
ID=59487013
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621232056.0U Expired - Fee Related CN206381764U (en) | 2016-11-16 | 2016-11-16 | Oil removing dedusting and purifying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206381764U (en) |
-
2016
- 2016-11-16 CN CN201621232056.0U patent/CN206381764U/en not_active Expired - Fee Related
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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: 20170808 Termination date: 20171116 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |