CN101648098B - Device and method for purifying and recycling oil, water and dust in flue gas - Google Patents
Device and method for purifying and recycling oil, water and dust in flue gas Download PDFInfo
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- CN101648098B CN101648098B CN2008101391971A CN200810139197A CN101648098B CN 101648098 B CN101648098 B CN 101648098B CN 2008101391971 A CN2008101391971 A CN 2008101391971A CN 200810139197 A CN200810139197 A CN 200810139197A CN 101648098 B CN101648098 B CN 101648098B
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- flue gas
- oil
- baffle plate
- recycle device
- water
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Abstract
The invention relates to a device and a method for purifying and recycling oil, water and dust in a flue gas. The device comprises a bag dust collector (2), a primary draft fan (4), a pipeline (5) and a secondary draft fan (6). The device is characterized in that: a purifying and recycling device (3) is arranged on the device; one end of the primary draft fan (4) is connected with the pipeline (5), while the other end is connected with the purifying and recycling device (3); the purifying and recycling device (3) is connected with the bag dust collector (2) and the secondary draft fan (6) through the pipeline; and the secondary draft fan (6) is connected with a chimney (1). The method comprises the following steps that: the flue gas passes through the pipeline and the primary draft fan first and then enters the purifying and recycling device, and the purifying and recycling device performs primary separation treatment and recycling on the flue gas; and the treated flue gas enters the bag dust collector through the pipeline, the bag dust collector performs secondary treatment on the flue gas, and the secondary draft fan exhausts the flue gas into the chimney. The device has a simple structure, can make the emission of waste flue gases reach the standard and can recycle the oil in the waste flue gases, thereby fundamentally solving the difficult problems of environmental pollutions and generating huge economic and social benefits.
Description
Technical field
Oil, water, dust purification recycle device in the flue gas belong to industrial waste gas and administer with environmental protection, energy-conservation cleaning equipment and processing method field.
Background technology
Enterprise will survive, and realizes sustainable development, environmental improvement and energy-conservation be crucial; Many enterprises do not close, stop, merge and shift because of environmental protection is up to standard.What the flue gas ash removal technology generally adopted now is the cloth-bag type dedusting, and fiber bag precipitator effect for the flue gas of pure dust is very obvious; But except that dust, contain compositions such as oil, water in the present flue gas toward contact.Flue gas generally is high temperature on the one hand, and this just requires the heat-resisting quantity of cloth bag material very good, and existing domestic enterprise adopts the cloth bag of import material usually, and such cloth bag cost is very high; On the other hand, flue gas is through sack cleaner the time, and the oil in the flue gas can make dust removing effects reduction, the lost of life of cloth bag attached to the surface of cloth bag, causes the replacement cycle of cloth bag short, brings heavy financial burden to enterprise; And fume emission is not up to standard, causes the pollution of enterprise to atmospheric environment, brings certain social responsibility burden to enterprise again.
Therefore, research and development a kind of can be effectively with oil, water in the flue gas, dust purification is up to standard and the device that can recycle is very necessary.
Summary of the invention
The technical problem to be solved in the present invention is: overcome the problem that prior art exists, provide a kind of simple in structure, can make useless fume emission up to standard, and oil, water, dust purification recycle device in the flue gas that can recycle the oil in the flue gas.
The technical solution adopted for the present invention to solve the technical problems is: oil in this flue gas, water, the dust purification recycle device, comprise sack cleaner, an air-introduced machine, first pipeline, the secondary air-introduced machine, the purification recycle device is set, No. one time air-introduced machine one end links to each other with first pipeline, the other end links to each other with the purification recycle device, purify recycle device and sack cleaner, the secondary air-introduced machine links to each other by second pipeline, the secondary air-introduced machine connects chimney, it is characterized in that: purify recycle device and comprise shell, reflecting curtain, filter baffle plate, the oil plant collection hole, the oil plant recovery tube, fuel outlet valve, the shell bottom is provided with the oil plant recovery tube, filtering baffle plate is fixed on the shell by lower supporting plate is oblique, on the hypotenuse direction of edge filtration baffle plate, reflecting curtain is installed, reflecting curtain is fixed by upper backup pad, the oil plant collection hole is set on the oil plant recovery tube, and the oil plant recovery tube is divided into the storing fuel tap.
Filter baffle plate and be fixed on the shell by lower supporting plate is oblique, the angle α that filters baffle plate and shell is 30-60 °.The effect of filtering baffle plate is that elaioleucite is dammed, and the effect of reflecting curtain is flue gas to be reflexed to next group baffle plate refilter and dam.
The filtration baffle plate is a half elliptic, and flanging is established at the top, the uniform through hole in top, the uniform pockmark in bottom.
Reflecting curtain is a half elliptic, and the half elliptic reflecting curtain is a corrugated.
Upper backup pad and lower supporting plate are herringbone.The effect of herringbone gripper shoe is with filtration baffle plate and reflecting curtain support fixation in the enclosure.
Filter baffle plate and reflecting curtain mounted in pairs, form the broken line passage.How right can be provided with.
The half elliptic reflecting curtain can also be designed to laterally zygomorphic groove shape.Or be other effective shapes of damming.
Flue gas is at first by pipeline, and an air-introduced machine enters the purification recycle device and carries out the first separation processing, reclaims; Treated flue gas enters the sack cleaner after-treatment through pipeline, enters chimney through the secondary air-introduced machine.
Operation principle
Utilize mechanics principle design, the particle in the flue gas is separated.Through the air-introduced machine pressurization, the elaioleucite in the flue gas can be got to the bottom with certain speed and filter on the baffle plate.Filter baffle plate when mounted, be welded in the shell of equipment with certain angle (30 °-60 ° at α angle), filtering baffle plate top has the equally distributed through hole that varies in size, when flue gas passes through, have the elaioleucite of part to be dammed retaining on the filtration baffle plate, and drippage go down; In the bottom of filtering baffle plate some cellular apertures (not penetrating) are arranged, can the oil that keep off effectively be dammed, the oil droplet that gets off that dammed can up move at the effect lower edge of wind-force filtration baffle plate, oil droplet moves to filtration baffle plate top and can drip through through hole, on the hypotenuse direction of edge filtration baffle plate the top reflecting curtain is installed, the surface of reflecting curtain is a bellows-shaped; Flue gas arrives the top reflecting curtain under through the effect in power after the reflecting curtain, the oil droplet that drips is pooled to oil plant recovery holes place under the effect of the reaction force of top reflecting curtain and self gravitation, flow to again in the oil plant recovery tube, finally flow into oil groove.Through the damming and filters of such multilayer baffle plate, oily effectively being removed in the flue gas, according to the difference of engineering actual conditions, the varying in size of equipment, the number of plies of filtration is difference thereupon also.Flue gas after the oil purification carries out dedusting through sack cleaner again, finally reaches the purpose that purifies flue gas.
Compared with prior art, oil, water, dust purification recycle device and method had in the flue gas of the present invention
Beneficial effect is: device has simple in structure, and processing and fabricating is easy, cost is low.Contained oil has the quilt more than 98% to dam to get off in the treated flue gas, the oil saver of the oily access to plant bottom of getting off of damming carries out recycling, the flue gas of removing oil continues to enter next device sack cleaner under the effect of power, the flue gas that enters sack cleaner on composition substantially based on dust, institute's oil-containing remains little, moisture in the flue gas also turns to steam under 180 ℃ high temperature, so sack cleaner can effectively purify dust last in the flue gas; Flue gas through sack cleaner arrives the secondary air-introduced machine through wind pipe, and flue gas is sent final qualified flue gas into chimney and entered atmosphere under the effect of air-introduced machine.Concrete characteristics are as follows:
1, the flue gas of handling through native system reaches or is better than (GB3095-1996) discharge standard, and atmospheric environment is improved.
2, use this device after, can increase service life of cloth bag greatly, reduced the maintenance cost of enterprise, economic effect is obvious.
3, institute of enterprise discharged flue gas reaches discharge standard, atmospheric environment is administered made contribution, and the social benefit of enterprise promotes.
The use of this device and method will be for curbing environmental pollution, solve present government and enterprise and draw the input lot of manpower and material resources of curbing environmental pollution, but fundamentally the technical barrier of contaminated solution problem can not produce secondary pollution simultaneously, produces huge economic and social benefit.
Description of drawings
Fig. 1 is the device flowage structure schematic diagram of the embodiment of the invention;
Fig. 2 is the internal structure schematic diagram that purifies recycle device;
Fig. 3 is the structural representation that filters baffle plate;
Fig. 4 is the A-A cross-sectional schematic of Fig. 3;
Fig. 5 is the structural representation of reflecting curtain;
Fig. 6 is the B-B cross-sectional schematic of Fig. 5;
Fig. 7 is a herringbone supporting plate structure schematic diagram.
Fig. 1-the 7th, the most preferred embodiment of oil, water, dust purification recycle device and method in the flue gas of the present invention.Wherein: 1 chimney, 2 sack cleaners, 3 dust purification recycle devices, No. 4 air-introduced machines, 5 pipelines, 6 air-introduced machines, 7 upper backup pads, 8 reflecting curtains, 9 filter baffle plate, 10 lower supporting plates, 11 oil plant collection holes, 12 oil plant recovery tubes, 13 fuel outlet valves, 14 shells, 15 flangings, 16 top through holes, 17 bottom pockmarks, 18 ripples.
The specific embodiment
Below in conjunction with accompanying drawing 1-7 oil, water, dust purification recycle device in the flue gas of the present invention are described further:
With reference to Fig. 1
Oil, water, dust purification recycle device in this flue gas are by chimney 1, sack cleaner 2, dust purification recycle device 3, air-introduced machine 4, pipeline 5, secondary air-introduced machine 6, upper backup pad 7, a reflecting curtain 8, filter baffle plate 9, lower supporting plate 10, oil plant collection hole 11, oil plant recovery tube 12, fuel outlet valve 13, shell 14, flanging 15, top through hole 16, bottom pockmark 17, ripple 18 and form.No. one time air-introduced machine 4 one ends link to each other with pipeline 5, the other end with purify recycle device 3 and link to each other, purify recycle device 3 and sack cleaner 2, secondary air-introduced machine 6 and link to each other secondary air-introduced machine 6 connection chimneys 1 by pipeline.
With reference to Fig. 2
Purify recycle device 3 by shell 14, upper backup pad 7, reflecting curtain 8, filter baffle plate 9, lower supporting plate 10, oil plant collection hole 11, oil plant recovery tube 12, fuel outlet valve 13 is formed, shell 14 is a cylindrical shape, the bottom is provided with oil plant recovery tube 12, filter baffle plate 9 by lower supporting plate 10 oblique being fixed in the shell 14, the angle α that filters baffle plate 9 and shell 14 is 30-60 °, on the hypotenuse direction of edge filtration baffle plate 9, top reflecting curtain 8 is installed, reflecting curtain 8 is fixing by upper backup pad 7, oil plant collection hole 11 is set on the oil plant recovery tube 12, and oil plant recovery tube 12 is divided into and is put fuel tap 13.Filter baffle plate 9 and be welded on filtration baffle plate 9 and reflecting curtain 8 mounted in pairs on the shell 14, it is how right that the exhaust gas volumn that can handle as required is provided with, and forms the broken line passage.
The exhaust gas volumn of Chu Liing as required, the angle α that filters baffle plate 9 selects arbitrarily in 30-60 ° scope, also can be designed to be greater than or less than 30-60 ° scope as required.As long as can with angled this design scope that all belongs to of shell, its effect is to put into reflecting curtain 8 with top to form the broken line passages.Flue gas is passed through along the broken line complications.
With reference to Fig. 3-4:
With reference to Fig. 5-6:
Reflecting curtain 8 is a half elliptic, and entire emission baffle plate 8 is a corrugated.Also can be designed as circle or other shapes,
Half elliptic reflecting curtain 8 can also be designed to laterally zygomorphic groove shape.Also can be designed as other effective shapes of damming.
With reference to Fig. 7
Utilize this device as follows to oil in the flue gas, water, dust purification recovery and treatment method:
Through air-introduced machine 4 pressurizations, the elaioleucite that enters in the flue gas that purifies in the recycle device 3 is got on the bottom filtration baffle plate 9 with certain speed.Owing to filter baffle plate 9 when mounted, be welded in the shell 14 of equipment with certain angle (30-60 ° at α angle), filtering baffle plate 9 tops has the equally distributed through hole that varies in size 16, when flue gas by the time, have the elaioleucite of the part retaining that dammed filtering on the baffle plate 9 and drippage goes down; The little pockmark 17 that some cellular (not penetrating) are arranged in the bottom of filtering baffle plate 9, can the oil that keep off effectively be dammed, the oil droplet that gets off that dammed can up move at the effect lower edge of wind-force filtration baffle plate 9, oil droplet moves to filtration baffle plate 9 tops and can drip through through hole 16, on the hypotenuse direction of edge filtration baffle plate 9, top reflecting curtain 8 is installed, because the surface design of reflecting curtain 8 is a bellows-shaped; Flue gas arrives top reflecting curtain 8 under through the effect in power after the reflecting curtain 8, the oil droplet that drips is pooled to oil plant collection hole 11 places under the effect of the reaction force of top reflecting curtain 8 and self gravitation, flow to again in the oil plant recovery tube 12, finally flow into oil groove.Through the damming and filters of such multilayer baffle plate, oily effectively being removed in the flue gas, according to the difference of engineering actual conditions, the varying in size of equipment, the number of plies of filtration is difference thereupon also.Flue gas after the oil purification enters sack cleaner 2 by pipeline, carries out final dusting through sack cleaner 2 again, and secondary air-introduced machine 6 enters chimney 1, finishes a discharge process.
Claims (6)
1. oily in the flue gas, water, the dust purification recycle device, comprise sack cleaner (2), an air-introduced machine (4), first pipeline (5), secondary air-introduced machine (6), be provided with and purify recycle device (3), No. one time air-introduced machine (4) one ends link to each other with first pipeline (5), the other end links to each other with purification recycle device (3), purify recycle device (3) and sack cleaner (2), secondary air-introduced machine (6) links to each other by second pipeline, secondary air-introduced machine (6) connects chimney (1), it is characterized in that: purify recycle device (3) and comprise shell (14), reflecting curtain (8), filter baffle plate (9), oil plant collection hole (11), oil plant recovery tube (12), fuel outlet valve (13), shell (14) bottom is provided with oil plant recovery tube (12), filtering baffle plate (9) is fixed on the shell (14) by lower supporting plate (10) is oblique, on the hypotenuse direction of edge filtration baffle plate (9), reflecting curtain (8) is installed, reflecting curtain (8) is fixing by upper backup pad (7), oil plant collection hole (11) is set on the oil plant recovery tube (12), and oil plant recovery tube (12) is divided into and is put fuel tap (13).
2. oil, water, dust purification recycle device in the flue gas according to claim 1, it is characterized in that: filter baffle plate (9) and be fixed on the shell (14) by lower supporting plate (10) is oblique, the angle α that filters baffle plate (9) and shell (14) is 30-60 °.
3. oil, water, dust purification recycle device in the flue gas according to claim 1 and 2 is characterized in that: filtering baffle plate (9) is half elliptic, and flanging (15) is established at the top, the uniform through hole in top (16), the uniform pockmark in bottom (17).
4. oil, water, dust purification recycle device in the flue gas according to claim 1 is characterized in that: reflecting curtain (8) is a half elliptic, and half elliptic reflecting curtain (8) is a corrugated.
5. oil, water, dust purification recycle device in the flue gas according to claim 1 and 2 is characterized in that: upper backup pad (7) and lower supporting plate (10) are herringbone.
6. oil, water, dust purification recycle device in the flue gas according to claim 1 is characterized in that: filter baffle plate (9) and reflecting curtain (8) mounted in pairs, form the broken line passage.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008101391971A CN101648098B (en) | 2008-08-14 | 2008-08-14 | Device and method for purifying and recycling oil, water and dust in flue gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008101391971A CN101648098B (en) | 2008-08-14 | 2008-08-14 | Device and method for purifying and recycling oil, water and dust in flue gas |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101648098A CN101648098A (en) | 2010-02-17 |
| CN101648098B true CN101648098B (en) | 2011-06-15 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2008101391971A Expired - Fee Related CN101648098B (en) | 2008-08-14 | 2008-08-14 | Device and method for purifying and recycling oil, water and dust in flue gas |
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| CN (1) | CN101648098B (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102225291A (en) * | 2011-05-27 | 2011-10-26 | 南通金坤机械设备有限公司 | Gas-liquid separator |
| CN103977640A (en) * | 2014-05-22 | 2014-08-13 | 江苏甬金金属科技有限公司 | Device for collecting and purifying oil stains |
| CN104436957A (en) * | 2014-11-24 | 2015-03-25 | 江苏新中环保股份有限公司 | Adsorbing and separating device for oil contamination in flue gas for dust remover |
| CN106051800A (en) * | 2016-06-14 | 2016-10-26 | 镇江市电站辅机厂有限公司 | Energy-saving and environment-friendly two-circuit parallel type smoke waste heat recycling device and method |
Citations (6)
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|---|---|---|---|---|
| CN1338969A (en) * | 1999-03-31 | 2002-03-06 | 尼卡西奥·P·莫拉·瓦尔乔 | Device for cleaning a fluid in the form of vapor from a circuit |
| CN1443292A (en) * | 2000-07-28 | 2003-09-17 | 康尼·诺曼 | Device for ventilation system |
| CN1548215A (en) * | 2003-05-12 | 2004-11-24 | 黄清豹 | Oil-burning flue eliminating apparatus |
| CN2902418Y (en) * | 2006-05-19 | 2007-05-23 | 黄将庭 | Oil fume separator |
| CN101185844A (en) * | 2007-08-30 | 2008-05-28 | 明峰 | Ionization, electronic accelerated reaction dual catalytic fathering industrial boiler flue gas pollution method and device |
| CN201267753Y (en) * | 2008-08-14 | 2009-07-08 | 徐志远 | Device for purifying, recycling and using oil, water and powder dust in flue gas |
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2008
- 2008-08-14 CN CN2008101391971A patent/CN101648098B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1338969A (en) * | 1999-03-31 | 2002-03-06 | 尼卡西奥·P·莫拉·瓦尔乔 | Device for cleaning a fluid in the form of vapor from a circuit |
| CN1443292A (en) * | 2000-07-28 | 2003-09-17 | 康尼·诺曼 | Device for ventilation system |
| CN1548215A (en) * | 2003-05-12 | 2004-11-24 | 黄清豹 | Oil-burning flue eliminating apparatus |
| CN2902418Y (en) * | 2006-05-19 | 2007-05-23 | 黄将庭 | Oil fume separator |
| CN101185844A (en) * | 2007-08-30 | 2008-05-28 | 明峰 | Ionization, electronic accelerated reaction dual catalytic fathering industrial boiler flue gas pollution method and device |
| CN201267753Y (en) * | 2008-08-14 | 2009-07-08 | 徐志远 | Device for purifying, recycling and using oil, water and powder dust in flue gas |
Non-Patent Citations (2)
| Title |
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| JP特开2005-279420A 2005.10.13 |
| JP特开平7-275628A 1995.10.24 |
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| CN101648098A (en) | 2010-02-17 |
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