CN108006687A - Middle ballast power saturation type flue dust collecting device - Google Patents
Middle ballast power saturation type flue dust collecting device Download PDFInfo
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- CN108006687A CN108006687A CN201610981855.6A CN201610981855A CN108006687A CN 108006687 A CN108006687 A CN 108006687A CN 201610981855 A CN201610981855 A CN 201610981855A CN 108006687 A CN108006687 A CN 108006687A
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- Prior art keywords
- flue dust
- water
- steam
- pipe
- saturation
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
- F23J15/04—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material using washing fluids
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chimneys And Flues (AREA)
Abstract
The present invention relates to a kind of middle ballast power saturation type flue dust collecting device, it is made of feed pump (15), secondary water pump (16) and (17), spiral water nozzle (2), strong fan (3), oblique covering nozzles (4), saturation flue dust mixing rotation water pipe (5), residual air pipe (7), combustor (8), helicoidal stream pipe (9), steam conversion tank (12), air-introduced machine (11), large area filter cotton tank (14), it is characterized in that：Flue dust cools down through some spiral nozzles (2) and desulfurization, flue dust is introduced to lower section (6) region of oblique covering nozzles (4) under the action of wind turbine (3), water is close to saturation when the water of oblique covering nozzles (4) enters saturation flue dust mixed conduit (5), pressed in being formed under longer gravity up and down and closely sweep along flue dust and be collected in alkaline water, a small amount of gas is had at this time, pernicious gas is cracked totally by the Pintsch process of combustor (8) after residual air pipe (7), heat and micro cigarette are introduced jet chimney progress steam taste removal and entered back into by air-introduced machine (11) again and thickeies filter cotton tank (14) discharge clean gas.
Description
Technical field
The present invention relates to a kind of middle ballast power saturation type flue dust collecting device, belong to house refuse environmental protection treatment technical field and
Chimney pollution thing recycles control technology field, is received suitable for the discharge of existing chimney pollution, suitable for middle-size and small-size waste incineration flue dust
Collection.
Background technology
The exhaust emission of current various smoke stack emission pollutions and bulky refuse incineration plant arrived very serious stage,
What the pollution of smoke stack emission can not administer just closes down, and builds bulky refuse incineration plant and is also protested strongly by the local masses, so
The sound development of our thermal technology's industry can be influenced by going down, for this present invention follow flue dust be with existing for object, we by object with
The economical mode of environmental protection recycles all right, avoids away the not smart old road of imitation.
Technology contents
The technical problem to be solved in the invention is to provide a kind of flue dust that can collect existing smoke stack emission, can combine
Flue dust caused by burning is collected in middle-size and small-size waste incineration.
The technical problem of the present invention can be solved by following measure：Middle ballast power saturation type flue dust collecting device, including three
A water tank, device are characterized in：Flue dust enters downward slanting flue, if arterial highway spiral water nozzle carries out first time cooling and desulfurization；
Under strong fan and oblique covering nozzles flow action, flue dust enter the lower section of the moisture film area of coverage, the wind pressure by powerful inertia
The weight for entering that the mixing of saturation flue dust rotates water pipe, the saturation flue dust lengthened mixing rotates the existing inertia of water pipe is swept along with current
Power but have certain pressure, can by insoluble in it is broken, realize being sufficiently mixed for liquid medicine and flue dust；Remaining micro flue dust passes through residual air
Pipe enters high-temp combustion pipeline, totally, in high-temperature pipe sets pernicious gas cracking under the high-temp combustion effect of burner
Put a spiral steam pipe, steam pipe water inlet from top to bottom stream, will from top to down in the high-temp combustion of high-temp combustion machine
Helix tube in water it is boiled produce steam, steam and hot water flow into steam conversion tank, steam flows up into last trace gas
Body pipeline, minimum gas together enter water tank together with hot water after steam taste removal boiling again, are set in the end of water tank
Gas filtration cotton tank, the ectosome of filter cotton layer of one large area have detachable shell, to make clean gas orderly
Discharge, gas outlet set it is a set of can remotely and short range monitor harmful gas detection, alarm instrument.
The technical problem of the present invention is repaid principal can be by taking following measure to solve：
Flue dust strength is sent into the moisture film area of coverage by flue dust with after first time buck desulfurization by cooling down by strong fan
Position, the moisture film area of coverage are in the big following small funnel-form in top, under the action of strong fan and oblique covering nozzles current, cigarette
Dirt is swept along to bring into saturation flue dust mixing rotation water pipe (5), saturation flue dust mixing rotation water pipe is in lengthening fine strip shape, flue dust
With liquid medicine in the water pipe (5) with water in the case where realizing pressure and gravity and rotation multiple action close in the state of saturation by cigarette
The bubble that dirt produces is crushed, realized in water pipe (5) from a point mixing.
Cracked after the middle mixed trace harmful gases of pressure enter residual air pipe by the high-temp combustion of combustor, is harmful
Minimum gas be cleaved totally, in order to using heat, remaining tracheal strips set steam pipe spiral from top to bottom, a steam
Pipe intakes from upper end, when quantitative water flow through when long long pipeline enters end be just burned flame it is boiled, so as to lower end generation
Steam.
Pollutant after being cracked by high-temp combustion recycles air inlet by residual air under the graviational interaction of air-introduced machine and enters
Last one of steam deodorizing sterilizing mixing duct.
Set large area to thicken filter cotton tank in the afterbody of water tank, be equipped with one in the outside of filter cotton tank and can facilitate
The radome fairing of dismounting, to facilitate clean gas to discharge in order, the top of radome fairing be equipped with it is a set of can remotely with short range monitoring report
Alarm device.
The present invention has the advantages that：
1st, the present invention is to realize flue dust collecting purpose from point mixing by flue dust and liquid medicine.
2nd, flue dust import 1 of the invention may be coupled to the existing chimney for having pollution and directly retain flue dust satisfies to middle ballast power
With effectively collected in formula flue dust collecting device.
3rd, the present invention can be directly connected at the smoke evacuation of middle-size and small-size waste incinerator, and will burn away the refuse caused flue dust
Effectively collected, and by the middle-size and small-size waste incinerator for smokelessly emitting non-wastewater discharge be placed in campus, rural area, small towns,
The local environmental protection treatment rubbish on the spot of ten thousand populations of the 4-6 such as army, cell, reduce garbage classification and landfill, the embarrassment of Jian great factories
Situation.
4th, beneficial effects of the present invention also reside in small investment, quick, use cost is low, can be received by users,
Economic benefit and social benefit are realized as early as possible.
Drawing explanation：
Fig. 1 is the side structure schematic view of the embodiment of the present invention 1.
Preferred embodiment：
Fig. 1 forms the embodiment of the present invention 1.The present embodiment includes three closed tanks, and flue dust tilts down import 1, spiral shell
Churning mouth 2, strong fan 3, oblique covering nozzles 4, the flue dust area of coverage 6 of funnel, in thin and long middle ballast power is satisfied pipe
5th, it is micro useless after residual air pipe 7, micro flue dust high-temp combustion cracking burner 8, helicoidal stream water pipe 9, steam conversion tank 12, cracking
Thing is entered in steam pipe 10 by the effect of air-introduced machine 11 to carry out the mixing of taste removal again and is discharged into lower part water tank, and process is a variety of mixed three times
Flue dust and pernicious gas after unification kind of Pintsch process are collected totally, again by the large area of the filter cotton tank 14 of water tank upper end
Filtering, clean gas flow direction is external under the action of kuppe.
In the present embodiment：
Flue dust enters in the flue 1 tilted down, if flue dust will pass through arterial highway umbrella shape under the suction of strong fan 3
Spiral nozzle 2 spray alkaline water cooling and desulfurization but strong fan 3 outwards blow under the action of by flue dust strength push to
If the position of the moisture film area of coverage 6, due to the oblique covering nozzles 4 Jing Guo multilayer moisture film covering, flue dust into again be difficult to
Upper return, for this present invention i.e. have powerful suction have not only crunch at the same time but also have smoothly saturation sweep along power flue dust nowhere may be used
Escape.
The moisture film area of coverage 6 lays the small funnel-form in side so that the flue dust for entering moment has mixing in top in the present embodiment
Digestion time, pipeline 5 long in thin below the moisture film area of coverage, the purpose is to will revolve flue dust close in the state of full water
Inertia-gravity will be produced when turning the movement of the mode swept along to lower band, in pipe so as to produce certain pressure, by flue dust and water
Bubble crushing is sufficiently mixed so as to be formed caused by mixing.
The test philosophy of the present invention is described below in conjunction with the accompanying drawings：
As shown in Figure 1, if arterial highway alkaline water film removing harmful substance and drop will be passed through when flue dust enters first of flue
Temperature, be that the pipeline for having inertial pressure swept along into lengthening is rotating by strong current when flue dust enters second flue
It is interior carry out Forced Mixing, after remaining micro noxious fume enters residual air pipe 7 be burned machine high-temp combustion cracking totally afterwards,
Discarded object after micro cracking be sucked into again steam mixing duct carry out deodorizing sterilizing remix, for make afterbody discharge gas more
Add cleaning, afterbody sets filter cotton tank, the gas after filtering for thickening increasing vapor permeation area to reach completely on water tank
To more clean gas.
Since smart structural design, flue dust collecting are efficient.
Since cost simple in structure is relatively low and utilization rate is high.
Since water is that repeats itself does not have waste water outwards to discharge.
Since no flue dust is outwards discharged so not setting chimney.
, can be to the various boilers of existing fire coal and various heat source chimney pollution sources due to being the complete set of equipments that can individually operate
It is attached, flue dust is effectively collected.
Claims (5)
- Ballast power saturation type flue dust collecting device in 1., including three closed tanks, it is characterized in that：Flue dust enters downward slanting cigarette Road (1) if, arterial highway spiral water nozzle (2) carry out first time cooling and desulfurization；In strong fan (3) and oblique covering nozzles (4) Flow action under, flue dust enters the lower section of the moisture film area of coverage (6), swept along by the wind pressure of powerful inertia and current and lower enter saturation Flue dust mixing rotation water pipe (5), the saturation flue dust mixing lengthened rotate the gravity of water pipe (5) existing inertia and have certain pressure Power, can by flue dust bubble grinding crushing not soluble in water, realize being sufficiently mixed for liquid medicine and flue dust；Remaining micro flue dust is through excess enthalpy Tracheae (7) enters high-temp combustion pipeline, cracks pernicious gas totally, in high temperature under the high-temp combustion effect of burner (8) The water inlet of spiral a steam pipe (9), steam pipe (9) is set to flow from top to bottom in pipeline, the height in high-temp combustion machine (8) Boiled steam, steam and the hot water of producing of water in helix tube from top to down is flowed into steam conversion tank (12), steam by temperature burning Flow up into last minimum gas pipeline, minimum gas together enters water after steam taste removal boiling again together with hot water Case, in the end of water tank, the gas filtration cotton tank (14) of one large area is set, the ectosome of filter cotton layer have it is detachable Shell, to make clean gas discharge in order, gas outlet set it is a set of can remotely and short range detect pernicious gas Detect warning instrument (13).
- 2. middle ballast power saturation type flue dust collecting device according to claim 1, it is characterized in that：Flue dust is by cooling and first Flue dust strength is sent into by the position of the moisture film area of coverage (6) by strong fan after secondary buck desulfurization, the moisture film area of coverage is in that top is big Following small funnel-form, the saturation flue dust mixing rotation water pipe under the action of strong fan (3) and oblique covering nozzles (4) current (5) in, saturation flue dust mixing rotation water pipe in lengthen fine strip shape, flue dust and liquid medicine in water pipe (5) with water close to saturation In the state of realize pressure and gravity and rotate the bubble crushing for producing flue dust under multiple action, realize in the water pipe (5) From a point mixing.
- 3. middle ballast power saturation type flue dust collecting device according to claim 1, it is characterized in that：Pressed in mixed micro- Measure the minimum gas quilt for cracking, being harmful to by the high-temp combustion of combustor (8) after entering residual air pipe (7) to pernicious gas during lower end Crack totally, for utilization heat, one steam pipe (9) spiral from top to bottom, steam pipe (9) of setting in residual air pipe (7) From upper end water inlet, when the pipeline that quantitative water flows through long length enters end just be burned flame it is boiled, so as to lower end generation Steam.
- 4. middle ballast power saturation type flue dust collecting device according to claim 1, it is characterized in that：After being cracked by high-temp combustion Pollutant air inlet (10) recycled by residual air under the graviational interaction of air-introduced machine (11) disappear into last one of steam taste removal Malicious mixing duct.
- 5. middle ballast power saturation type flue dust collecting device according to claim 1, it is characterized in that：One is set in the afterbody of water tank Seat large area thickeies filter cotton tank (14), one is equipped with the outside of (14) can conveniently the radome fairing of dismounting, to facilitate clean gas Body discharges in order, be equipped with the top of radome fairing it is a set of can remotely and short range monitoring alarm device (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610981855.6A CN108006687B (en) | 2016-11-02 | 2016-11-02 | Medium-pressure gravity saturation type smoke collector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610981855.6A CN108006687B (en) | 2016-11-02 | 2016-11-02 | Medium-pressure gravity saturation type smoke collector |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN108006687A true CN108006687A (en) | 2018-05-08 |
| CN108006687B CN108006687B (en) | 2020-02-14 |
Family
ID=62048611
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610981855.6A Active CN108006687B (en) | 2016-11-02 | 2016-11-02 | Medium-pressure gravity saturation type smoke collector |
Country Status (1)
| Country | Link |
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| CN (1) | CN108006687B (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2258584Y (en) * | 1996-04-17 | 1997-07-30 | 北京市机电研究院环境保护技术研究所 | Exhausting treatment equipment after rubish incineration |
| WO2001073359A1 (en) * | 2000-03-24 | 2001-10-04 | Mengqiu Yan | Hot-water furnace |
| CN101324370A (en) * | 2008-07-30 | 2008-12-17 | 张亚玉 | High-efficiency energy-saving environmental protection boiler |
| CN203571755U (en) * | 2013-11-18 | 2014-04-30 | 山东巨亚环保设备有限公司 | Harmless and comprehensive rubbish treating and utilizing system |
| CN105757677A (en) * | 2016-03-21 | 2016-07-13 | 安徽未名生物环保有限公司 | Intelligent garbage treatment system with multiple gas circulation function |
-
2016
- 2016-11-02 CN CN201610981855.6A patent/CN108006687B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2258584Y (en) * | 1996-04-17 | 1997-07-30 | 北京市机电研究院环境保护技术研究所 | Exhausting treatment equipment after rubish incineration |
| WO2001073359A1 (en) * | 2000-03-24 | 2001-10-04 | Mengqiu Yan | Hot-water furnace |
| CN101324370A (en) * | 2008-07-30 | 2008-12-17 | 张亚玉 | High-efficiency energy-saving environmental protection boiler |
| CN203571755U (en) * | 2013-11-18 | 2014-04-30 | 山东巨亚环保设备有限公司 | Harmless and comprehensive rubbish treating and utilizing system |
| CN105757677A (en) * | 2016-03-21 | 2016-07-13 | 安徽未名生物环保有限公司 | Intelligent garbage treatment system with multiple gas circulation function |
Also Published As
| Publication number | Publication date |
|---|---|
| CN108006687B (en) | 2020-02-14 |
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| TA01 | Transfer of patent application right | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20190712 Address after: 226601 Enlightenment Software Park B Block 2-F, No. 8 Yingbin Road, Haian Development Zone, Nantong City, Jiangsu Province Applicant after: Ding Yirong Address before: 510700 South No. 2 Yagang Avenue, Yagang Village, Shimen Street, Baiyun District, Guangzhou City, Guangdong Province Applicant before: Guangzhou Huasheng environmental protection product design Co., Ltd. |
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Effective date of registration: 20200119 Address after: 318055 No. 588, Jixin Road, Xinqiao Town, Luqiao District, Taizhou City, Zhejiang Province Applicant after: Zhejiang runtiankangdi Environmental Protection Technology Co., Ltd Address before: 226601 Enlightenment Software Park B Block 2-F, No. 8 Yingbin Road, Haian Development Zone, Nantong City, Jiangsu Province Applicant before: Ding Yirong |
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