CN106390659A - Efficient oil and dust removing device - Google Patents
Efficient oil and dust removing device Download PDFInfo
- Publication number
- CN106390659A CN106390659A CN201611009640.4A CN201611009640A CN106390659A CN 106390659 A CN106390659 A CN 106390659A CN 201611009640 A CN201611009640 A CN 201611009640A CN 106390659 A CN106390659 A CN 106390659A
- Authority
- CN
- China
- Prior art keywords
- dust arrester
- way valve
- entrance
- efficient degreasing
- outlet
- 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.)
- Pending
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/002—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by condensation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/26—Drying gases or vapours
- B01D53/261—Drying gases or vapours by adsorption
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/80—Water
Abstract
The invention provides an efficient oil and dust removing device. The device sequentially comprises an air blower, a condenser, a primary cyclone separator, a primary heater, a primary oil remover, a detector a, a dryer, an electrostatic precipitator, a detector b and a buffer gas holder in a pipeline connection sequence, wherein the bottom of the primary cyclone separator is connected with the chemical oil remover, an outlet of the chemical oil remover is connected with the condenser, multiple stages of waved baffles are arranged in the primary oil remover perpendicularly, surfaces of two sides of each baffle are porous, and superfine nanoscale glass fiber paper is sandwiched between the baffles. The device can effectively remove dust, smoke and other pollutants in exhaust gas and is simple in structure, convenient to operate and wide in application range.
Description
Technical field
The invention belongs to purifier field, especially relates to a kind of efficient degreasing dust arrester.
Background technology
With expanding economy, atmospheric pollution is increasingly serious, contains substantial amounts of particle, powder in the waste gas that industry manufactures
Dirt and oil smoke etc., are directly discharged to the environment of severe exacerbation periphery in air, the life to people and healthy all cause
Harm, so needing it is carried out filtration treatment before waste gas discharge, removes the harmful substance such as dust therein and oil smoke.
Content of the invention
In view of this, the invention is directed to a kind of efficient degreasing dust arrester, to remove dust in removing exhaust gas, oil
The harmful substances such as cigarette, purify air.
For reaching above-mentioned purpose, the technical scheme of the invention is realized in：
A kind of efficient degreasing dust arrester, includes aerator successively according to the pipeline order of connection, condenser, one cyclonic divide
From device, primary heater, one-level grease trap, detection meter a, exsiccator, electrostatic precipitator, detection meter b and buffering air accumulator.
Further, described primary cyclone bottom connects chemical oil remover, and described chemical oil remover outlet connects
Described condenser, the water chemically separated in grease trap is available for condenser and uses as recirculated water, effectively save cost.
Further, described one-level grease trap internal vertical arranges multistage baffle plate, and described baffle plate is waveform, described baffle plate
Both side surface is cellular, and described baffle plate is sandwiched between ultrafine nanometer all-glass paper.
Further, described detection meter a outlet connecting tee valve I, described three-way valve I another two port connects two grades respectively
Grease trap entrance and described exsiccator entrance, arrange some floor height oil-absorbing resins inside described two grades of grease traps, detection meter a can examine
Survey whether in the air oil content residual reaches standard, such as not up to standard value can control three-way valve I and air is passed through two grades of grease traps
Inside purify further.
Further, described exsiccator is at least arranged in series two.
Further, described detection meter b outlet connecting tee valve II, described three-way valve II another two port connects two respectively
Level cyclone inlet and buffering air accumulator entrance, described detection meter b can be carried out to the moisture content of in the air residual and granularity
Detection, if testing result is up to standard, air can be passed through in buffering air accumulator, as below standard in testing result, then pass through threeway
Air is passed through secondary cyclone, after secondary heater, is passed through exsiccator again and electrostatic precipitator is purified by valve II.
Further, described secondary cyclone outlet connects secondary heater entrance, described secondary heater outlet
Connecting tee valve III, described three-way valve III another two port connects exsiccator entrance and three-way valve I respectively.
With respect to prior art, a kind of efficient degreasing dust arrester described in the invention has the advantage that：
(1) a kind of efficient degreasing dust arrester described in the invention can effectively remove dust in removing exhaust gas, oil smoke
Deng pollutant, internal system detection means can ensure that purification produces a desired effect.
(2) a kind of efficient degreasing dust arrester described in the invention is cost-effective, easy to operate, applied widely.
Brief description
The accompanying drawing constituting the part of the invention is used for providing the invention is further understood, and the present invention creates
The schematic description and description made is used for explaining the invention, does not constitute the improper restriction to the invention.?
In accompanying drawing：
Fig. 1 is a kind of efficient degreasing dust arrester structural representation described in the invention embodiment.
Description of reference numerals：
1- aerator；2- condenser；3- primary cyclone；31- chemical oil remover；4- primary heater；5- one-level
Grease trap；51- baffle plate；6- detection meter a；61- three-way valve I；Bis- grades of grease traps of 62-；7- exsiccator；8- electrostatic precipitator；9- examines
Survey meter b；92- three-way valve II；93- secondary cyclone；93- secondary heater；94- three-way valve III；10- buffers air accumulator.
Specific embodiment
It should be noted that in the case of not conflicting, the embodiment in the invention and the feature in embodiment can
To be mutually combined.
To describe the invention below with reference to the accompanying drawings and in conjunction with the embodiments in detail.
A kind of efficient degreasing dust arrester, includes aerator 1, condenser 2, one cyclonic successively according to the pipeline order of connection
Separator 3, primary heater 4, one-level grease trap 5, detection meter a6, exsiccator 7, electrostatic precipitator 8, detection meter b9 and buffering storage
Gas tank 10.
Described primary cyclone 3 bottom connects chemical oil remover 31, and described chemical oil remover 31 outlet connects described
Condenser 2, the water separated from described chemical oil remover 31 is available for described condenser 2 and uses as recirculated water, effectively saves
About cost.
Described one-level grease trap 5 internal vertical arranges multistage baffle plate 51, and described baffle plate 51 is waveform, 51 liang of described baffle plate
Side surface is cellular, and described baffle plate 51 is sandwiched between ultrafine nanometer all-glass paper.
Described detection meter a6 outlet connecting tee valve I 61, described three-way valve I 61 another two port connects two grades of oil removings respectively
Device 62 entrance and described exsiccator 7 entrance, described two grades of grease traps 62 are internal to arrange some floor height oil-absorbing resins, and detection meter a6 can
Whether detection in the air oil content residual reaches standard, as being not up to standard value controllable three-way valve I 61, air is passed through described two
Purify further in level grease trap 62.
Described exsiccator 7 is at least arranged in series two.
Described detection meter b9 outlet connecting tee valve II 91, described three-way valve II 91 another two port connects two grades of rotations respectively
Wind separator 92 entrance and described buffering air accumulator 10 entrance, described detection meter b9 can be to the moisture content of in the air residual and granularity
Detected, if testing result is up to standard, air can be passed through in described buffering air accumulator 10, as below standard in testing result,
Then air is passed through by secondary cyclone 92 by described three-way valve II 91, after secondary heater 93, is passed through described dry again
Dry device 7 and described electrostatic precipitator 8 are purified.
Described secondary cyclone 92 outlet connects secondary heater 93 entrance, and described secondary heater 93 outlet connects
Three-way valve III 94, described three-way valve III 94 another two port connects exsiccator 7 entrance and three-way 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
Solidifying, it is agglomerated into larger particles, afterwards waste gas is passed through primary cyclone 3, the centrifugal force producing in the presence of cyclone can
So that the impurity of heavier mass and drop in waste gas is thrown away and be attached on wall, realize gas-liquid separation, the waste water of discharge passes through to change
Learn grease trap 31 and carry out oil-water separation, the water isolated is passed through condenser 2 and uses as cooling circulating water.Afterwards waste gas is led to
Enter primary heater 4, so that the entrained oil droplet in waste gas is heated and be dispersed into mist of oil shape, be passed through one-level grease trap 5 afterwards, in multistage gear
Under the filtration of plate 51 and ultra-fine fibre glass paper, can effectively remove residual.Pass through oil content residual in detection meter a detected gas afterwards
Whether exceeded, if exceeded, then by controlling three-way valve I 61, gas be passed through in two grades of grease traps 62, carry out further net
Change.Afterwards gas is passed through in exsiccator 7, by molecular sieve etc., the moisture in gas is adsorbed, multiple-stage drier is set,
Can ensure that drying effect.After oil removing eliminating water, gas is passed through electrostatic precipitator 8, 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 is detected, as up to standard in testing result, the clean gas having filtered is passed through in caching air accumulator 10 and preserves, such as detect
Result is below standard, then by three-way valve II 91, gas is passed through after secondary cyclone 92 and secondary heater 93, controls three
Gas is passed through exsiccator 7 by port valve III 94 again and electrostatic precipitator 8 carries out secondary filter.
The foregoing is only the preferred embodiment of the invention, not in order to limit the invention, all this
Within the spirit of innovation and creation and principle, any modification, equivalent substitution and improvement made etc., should be included in the invention
Protection domain within.
Claims (7)
1. a kind of efficient degreasing dust arrester it is characterised in that：Include aerator (1), condensation according to the pipeline order of connection successively
Device (2), primary cyclone (3), primary heater (4), one-level grease trap (5), detection meter a (6), exsiccator (7), electrostatic
Cleaner unit (8), detection meter b (9) and buffering air accumulator (10).
2. a kind of efficient degreasing dust arrester according to claim 1 it is characterised in that：Described primary cyclone
(3) bottom connects chemical oil remover (31), and described chemical oil remover (31) outlet connects described condenser (2).
3. a kind of efficient degreasing dust arrester according to claim 1 it is characterised in that：In described one-level grease trap (5)
Portion is vertically arranged multistage baffle plate (51), and described baffle plate (51) is waveform, and described baffle plate (51) both side surface is cellular, described
Baffle plate (51) is sandwiched between ultrafine nanometer all-glass paper.
4. a kind of efficient degreasing dust arrester according to claim 1 it is characterised in that：Described detection meter a (6) outlet is even
Connect three-way valve I (61), described three-way valve I (61) another two port connects two grades of grease trap (62) entrances and described exsiccator respectively
(7) entrance, arranges some floor height oil-absorbing resins inside described two grades of grease traps (62).
5. a kind of efficient degreasing dust arrester according to claim 1 it is characterised in that：Described exsiccator (7) is at least gone here and there
Connection setting two.
6. a kind of efficient degreasing dust arrester according to claim 1 it is characterised in that：Described detection meter b (9) outlet is even
Connect three-way valve II (91), described three-way valve II (91) another two port connects secondary cyclone (92) entrance and buffering respectively
Air accumulator (10) entrance.
7. a kind of efficient degreasing dust arrester according to claim 1 it is characterised in that：Described secondary cyclone
(92) outlet connection secondary heater (93) entrance, described secondary heater (93) outlet connecting tee valve III (94), described three
Port valve III (94) another two port connects exsiccator (7) entrance and three-way valve I (61) respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611009640.4A CN106390659A (en) | 2016-11-16 | 2016-11-16 | Efficient oil and dust removing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611009640.4A CN106390659A (en) | 2016-11-16 | 2016-11-16 | Efficient oil and dust removing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106390659A true CN106390659A (en) | 2017-02-15 |
Family
ID=59230582
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611009640.4A Pending CN106390659A (en) | 2016-11-16 | 2016-11-16 | Efficient oil and dust removing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106390659A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110835557A (en) * | 2019-12-06 | 2020-02-25 | 中冶焦耐(大连)工程技术有限公司 | Gas oil removing device and process |
| CN111298588A (en) * | 2020-03-06 | 2020-06-19 | 复旦大学 | Ship flue gas condensation cyclone purification device and method |
| CN111939702A (en) * | 2020-08-14 | 2020-11-17 | 李萍萍 | Atomizing attached dust removal device |
| CN113244731A (en) * | 2021-06-30 | 2021-08-13 | 李京耕 | Mining plant dust removal purifier for environmental protection equipment |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0225178A1 (en) * | 1985-11-28 | 1987-06-10 | Aalborg Vaerft A/S | A process for purification, in particular desulphurization, of flue gas |
| EP1849672A2 (en) * | 2006-04-28 | 2007-10-31 | Haldex Brake Products GmbH | Cartridge, compressed air reprocessing plant and method for operating a compressed air reprocessing plant |
| CN201685183U (en) * | 2010-06-09 | 2010-12-29 | 上海理工大学 | Low-temperature cold air generating device used in grinding process of metal |
| CN202724951U (en) * | 2012-07-26 | 2013-02-13 | 杭州日盛净化设备有限公司 | Air purifying device |
| CN203564930U (en) * | 2013-11-22 | 2014-04-30 | 苏州三博士环保科技有限公司 | Controllable circulating waste gas purification device |
| CN105536405A (en) * | 2016-01-11 | 2016-05-04 | 张文国 | Industrial refuse cracking burning tail gas treatment system |
| CN105920965A (en) * | 2016-06-22 | 2016-09-07 | 天津安联天源节能科技有限公司 | Steam-water separator capable of sufficiently separating condensed water |
| CN205650003U (en) * | 2016-03-29 | 2016-10-19 | 陈友昌 | Integrative clarifier of compound oil smoke peculiar smell of wet -type static |
-
2016
- 2016-11-16 CN CN201611009640.4A patent/CN106390659A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0225178A1 (en) * | 1985-11-28 | 1987-06-10 | Aalborg Vaerft A/S | A process for purification, in particular desulphurization, of flue gas |
| EP1849672A2 (en) * | 2006-04-28 | 2007-10-31 | Haldex Brake Products GmbH | Cartridge, compressed air reprocessing plant and method for operating a compressed air reprocessing plant |
| CN201685183U (en) * | 2010-06-09 | 2010-12-29 | 上海理工大学 | Low-temperature cold air generating device used in grinding process of metal |
| CN202724951U (en) * | 2012-07-26 | 2013-02-13 | 杭州日盛净化设备有限公司 | Air purifying device |
| CN203564930U (en) * | 2013-11-22 | 2014-04-30 | 苏州三博士环保科技有限公司 | Controllable circulating waste gas purification device |
| CN105536405A (en) * | 2016-01-11 | 2016-05-04 | 张文国 | Industrial refuse cracking burning tail gas treatment system |
| CN205650003U (en) * | 2016-03-29 | 2016-10-19 | 陈友昌 | Integrative clarifier of compound oil smoke peculiar smell of wet -type static |
| CN105920965A (en) * | 2016-06-22 | 2016-09-07 | 天津安联天源节能科技有限公司 | Steam-water separator capable of sufficiently separating condensed water |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110835557A (en) * | 2019-12-06 | 2020-02-25 | 中冶焦耐(大连)工程技术有限公司 | Gas oil removing device and process |
| CN111298588A (en) * | 2020-03-06 | 2020-06-19 | 复旦大学 | Ship flue gas condensation cyclone purification device and method |
| CN111939702A (en) * | 2020-08-14 | 2020-11-17 | 李萍萍 | Atomizing attached dust removal device |
| CN113244731A (en) * | 2021-06-30 | 2021-08-13 | 李京耕 | Mining plant dust removal purifier for environmental protection equipment |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170215 |
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| WD01 | Invention patent application deemed withdrawn after publication |