CN104289054A - Smoke dust hydrator - Google Patents
Smoke dust hydrator Download PDFInfo
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- CN104289054A CN104289054A CN201410520200.XA CN201410520200A CN104289054A CN 104289054 A CN104289054 A CN 104289054A CN 201410520200 A CN201410520200 A CN 201410520200A CN 104289054 A CN104289054 A CN 104289054A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/02—Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath
- B01D47/021—Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath by bubbling the gas through a liquid bath
-
- 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
- B01D53/50—Sulfur oxides
- B01D53/507—Sulfur oxides by treating the gases with other liquids
-
- 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/62—Carbon oxides
-
- 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/01—Engine exhaust gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/12—Methods and means for introducing reactants
- B01D2259/124—Liquid reactants
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Environmental & Geological Engineering (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Combustion & Propulsion (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
The invention relates to a smoke dust hydrator. The smoke dust hydrator comprises a first container, a main gas inlet pipe, a flow splitting chamber, a plurality of gas inlet branch pipes, a first barrel-shaped foam intercepting net, an umbrella-shaped foam intercepting net, first tapered pipes, first dust deposition pipes and a first gas outlet pipe, wherein the main gas inlet pipe penetrates through and is fixedly connected with the top of the first container; the flow splitting chamber is of a hollow cavity and an opening at the top of the flow splitting chamber is connected with the main gas inlet pipe and extends to one end of the inner part of the first container; a plurality of openings are formed in the bottom of the flow splitting chamber and are connected with the upper ends of the plurality of gas inlet branch pipes; the lower ends of the plurality of gas inlet branch pipes are connected with the first barrel-shaped foam intercepting net; the umbrella-shaped foam intercepting net is arranged at the peripheries of the gas inlet branch pipes above the first barrel-shaped foam intercepting net; the lower end of the first barrel-shaped foam intercepting net is connected with an upper-end large opening of the corresponding first tapered pipe and a lower-end small opening of the first tapered pipe is connected with the corresponding first dust deposition pipe; the lower ends of the plurality of first dust deposition pipes are combined and extend to a dust deposition chamber below the first container; and one end of the first gas outlet pipe is fixedly connected with the top of the first container. The smoke dust hydrator has high efficiency of filtering smoke dust, and is complete in purification, low in cost and rapid in effect.
Description
Technical field
The invention relates to filed of flue gas purification, relate to a kind of water that utilizes especially and carry out the smoke dust hydrator of all fume treatment such as boiler dusting and gasoline and diesel engine tail gas clean-up with cutting to indulge in serfing the Net.
Background technology
As everyone knows, at present, atmosphere pollution is day by day serious, often there is haze weather, soot dust granule and carbon dioxide are that main greenhouse gases and other various harmful substances are discharged in a large number in air, its consequence is troubling, and its pollution sources are mainly from various boiler smoke, vehicle exhaust, house owed by a citizen kitchen smoke and various dust etc.
Although the mankind are constantly finding the plan of solution, take thousand and one way, also have received significant effect, but the PM2.5 value that can enter lung but remains high all the time, with regard to current techniques and methods, gas is changed except advocating coal, oil changes electricity and changes gas, or limited production, decreasing pollution of restricting driving discharges, better way is not also had to deal with, even if motor vehicle and boiler adopt natural gas and battery in a large number in the future, but for a comparatively long period of time, coal is as fuel, oil will play subjective role as the strong impetus of engine, and, also can along with the raising of the development of society and national life level, demand can grow with each passing day, following State of Air pollution will be more serious, even if family's air purifier and mouth mask are also difficult keep off the atmosphere pollution existed everywhere, the most effective way still thoroughly cuts off pollution sources from source.
Following way and defect is mainly contained at present in control atmosphere pollution:
1, in boiler dusting, the dirt of employing cloth bag dry method filter in the past, facts have proved that its effect is very limited because of easy network blocking, now mainly by spraying and spraying and moisture film method solves, also have in addition and adopt Swashing type dust collection method, this wet method depositing dust is really very effective, the composition of sulphur reduces greatly, the particle of carbon also greatly reduces, it is no longer that black smoke billows that great majority filter the cigarette come up, but become white cigarette, but white cigarette in fact still flue gas and micronic dust (PM2.5 molecule), though dust particale is little, very harmful, this illustrates and adopts this kind of method still defectiveness, be difficult to thorough dedusting, this is because profit in this way dedusting time, gas is very active, speed is exceedingly fast, and gas chance water can produce bubble, flue dust wraps up by bubble, a part of flue dust is made to escape spray or spray and cause dedusting thorough not.
2, in purifying vehicle exhaust, adopt ternary catalyzing unit more, by redox reaction, make pernicious gas CO, HC and NOX be oxidized to CO
2and water vapour, and just helpless for the dust particale thing as PM2.5, install in the vehicle exhaust of ternary catalyzing unit and constantly discharge carbon dioxide, and the result that carbon dioxide is on the increase forms greenhouse effects.
Although CH, CO, CO of diesel vehicle
2discharge capacity is lower than gasoline car; but NOX and PM2.5 of discharge is far above gasoline car; ternary catalyzing unit cannot be installed again; tail gas particle catcher can only be installed for removing bulky grain carbon distribution; cause residual dust particale thing severe contamination air, in addition, the tail gas of many diesel vehicles blows to ground; produce airborne dust, further contaminated environment.
Although had remarkable progress at present in oil product upgrading, be proposed again state four gasoline, also just CO is down to 1.5, CH compound by 2.1 is down to 0.25, NO by 0.66
22.0 are down to by 5.0, PM is down to 0.22 by 0.1, smoke intensity is down to 0.15 by 0.8, and can't be applicable to all engine models, as can be seen here, utterly destroy the source of atmospheric pollution, still having very long and the road of hardships will be walked, according to currently used dedusting way, is that boiler or motor-vehicle tail-gas improvement aspect are also all not ideal enough, fundamentally cannot thoroughly solve dust polluting environment problem, human life's health faces threat.
As can be seen here, above-mentioned existing smoke and dust purifier with in use in structure, obviously still has inconvenience and defect, and is urgently further improved.In order to solve above-mentioned Problems existing, relevant manufactures there's no one who doesn't or isn't seeks solution painstakingly, but have no applicable design for a long time to be completed by development, and common product does not have appropriate structure to solve the problem, this is obviously the anxious problem for solving of relevant dealer always.
Summary of the invention
The object of the invention is to overcome passive catching type spray or the dust collection method such as moisture film and Swashing type in existing dust collection method a part of flue dust is sneaked off cause the halfway defect of dedusting, and provide a kind of can thoroughly dedusting, smoke abatement smoke dust hydrator.
The object of the invention is to realize by the following technical solutions.The present invention proposes a kind of smoke dust hydrator, and it comprises: the first container, main air inlet pipe, diffluence room, multiple air inlet are in charge of, umbrella cut indulge in serfing the Net, the first tubular cut indulge in serfing the Net, the first conical pipe, the first heavy ash pipe and the first escape pipe; Wherein said main air inlet pipe is passed and is fixed in the top of described first container, and its one end extends to the first internal tank, and the other end extends to the first external container; Described diffluence room is the cavity of hollow, and the opening at its top connects one end that described main air inlet pipe extends to the first internal tank, and the multiple openings bottom it connect the upper end that described multiple air inlet is in charge of; The lower end that described multiple air inlet is in charge of all is connected with described first tubular and cuts and indulge in serfing the Net, and the air inlet that this first tubular cuts top of indulging in serfing the Net is in charge of and is arranged with described umbrella and cuts and indulge in serfing the Net outward; Described first tubular cuts the upper end great Kou that the lower end of indulging in serfing the Net connects described first conical pipe, the lower end osculum of described first conical pipe connects the described first heavy ash pipe, and the lower end of the multiple first heavy ash pipe is merged into a pipeline and extends to the heavy grey room below described first container; One end of described first escape pipe is fixed in the top of described first container, and the other end extends to the outside of described first container.
Object of the present invention also can be applied to the following technical measures to achieve further.
Preferably, aforesaid smoke dust hydrator, it also comprises: second container, the second tubular cut indulge in serfing the Net, the second conical pipe, the second heavy ash pipe and the second escape pipe; Wherein said second container is arranged at the side of described first container; One end that described first escape pipe extends to described first external container is passed and is fixed in the top of described second container and extends to described second container inside, this one end extending to described second container inside is connected with the second tubular and cuts and indulge in serfing the Net, this second tubular cuts the upper end great Kou that lower end of indulging in serfing the Net connects the second conical pipe, and the lower end osculum of described second conical pipe connects the described second heavy ash pipe; One end of described second escape pipe is fixed in the top of described second container, and it is outside that the other end extends to described second container; Described second tubular cuts the height of indulging in serfing the Net and described first tubular and cuts the height of indulging in serfing the Net and maintain an equal level.
Preferably, aforesaid smoke dust hydrator, it also comprises: the 3rd container, the 3rd tubular cut indulge in serfing the Net, triconic pipe, the 3rd heavy ash pipe and the 3rd escape pipe; The 3rd wherein said container is arranged at the top of described first container, and the top of described first container becomes the bottom of described 3rd container; Described first escape pipe is positioned at described 3rd internal tank, and in inverted U, its one end connection the 3rd tubular extending to described first external container cuts indulges in serfing the Net, 3rd tubular cuts the upper end great Kou that lower end of indulging in serfing the Net connects triconic pipe, and the lower end osculum of this triconic pipe connects the described 3rd heavy ash pipe; One end of described 3rd escape pipe is fixed in the top of described 3rd container, and the other end extends to described 3rd external container; Described main air inlet pipe through the top of described 3rd container, then is passed and is fixed in the top of described first container.
Preferably, aforesaid smoke dust hydrator, it also comprises: the 4th container, the 4th tubular cut indulge in serfing the Net, the 4th conical pipe, the 4th heavy ash pipe and the 4th air inlet pipe; Wherein said 4th container is arranged at the opposite side of described first container; Described 4th air inlet pipe is passed and is fixed in the top of described 4th container, its one end extends to the outside of the 4th container, the other end extends to the 4th internal tank, one end that described 4th air inlet pipe extends to the 4th internal tank is connected with the 4th tubular and cuts and indulge in serfing the Net, 4th tubular cuts the upper end great Kou that lower end of indulging in serfing the Net connects the 4th conical pipe, and the lower end osculum of the 4th conical pipe connects the described 4th heavy ash pipe; One end that described main air inlet pipe extends to the first external container is fixed in the top of described 4th container; The bottom of described first container, second container and the 4th container all with described first container below the conducting of heavy grey room.
Preferably, aforesaid smoke dust hydrator, is provided with outlet pass between wherein said first container and second container; Heavy grey room below described first container is divided into left heavy grey room and the right side to sink grey room, and the lower end of the multiple first heavy ash pipe merges into a pipeline and the left side extended to below described first container sinks grey room.
Preferably, aforesaid smoke dust hydrator, the outside of the 3rd wherein said container is provided with water-level gauge, and the water level in the 3rd container cuts the upper end of indulging in serfing the Net higher than described 3rd tubular.
Preferably, aforesaid smoke dust hydrator, the level height that wherein said umbrella cuts lower end of indulging in serfing the Net does not cut the level height of lower end of indulging in serfing the Net higher than described first tubular.
Preferably, aforesaid smoke dust hydrator, the outside of the first wherein said container is provided with water-level gauge, and the water level in the first container cuts the upper end of indulging in serfing the Net higher than described umbrella.
Preferably, aforesaid smoke dust hydrator, is provided with blowoff valve bottom the heavy grey room below the first wherein said container.
Preferably, aforesaid smoke dust hydrator, wherein said main air inlet pipe, the first escape pipe, air inlet are in charge of and the upper end of the first heavy ash pipe is equipped with flange.
By technique scheme, smoke dust hydrator of the present invention at least has following advantages and beneficial effect:
1, from agent structure, several container, which floor cuts is indulged in serfing the Net, and the air pressure of power from engine cylinder and the blast of air-introduced machine of cigarette are entered in air inlet, power source all uses, be ready-made, the water of injection is cheap especially, and cost is low, effective, easy for installation, user takes like a shot, and easily promotes the use of.
2, from principle and effect, in smoke dust hydrator detailed catalogue cut and indulge in serfing the Net on minute aperture can rack all bubbles, water can absorb all dust particale things, and or it can be helped to react with many composition generation chemical reactions, makes the SO in harmful components
2and CO
2become sulfurous acid and carbonic acid innocuous substance respectively, therefore say, this method dedusting is more thorough, is the optimal path really realizing zero-emission.Flue gas track route remains a kind of complete open conduit, moreover there is special Air supply facility on engine He in boiler thorax, so blast pipe and smoke exhaust pipe insert in more shallow water, also engine and boiler can not be suppressed and go out, still can continue normal work, both effect of engine and boiler and air-introduced machine can not have been reduced, also their life-span can not be damaged, but also the huge temperature difference of other end You Ji Baidu because of smoke dust hydrator one end and engine and boiler, negative pressure is formed in smoke dust hydrator one end, not only counteract the resistance to boiler smoke and motor exhaust of water in container, also improve draft, more be conducive to the Thorough combustion of boiler, make burner hearth more prosperous, and, after the high-temperature flue gas of boiler one end enters the cold water in smoke dust hydrator, the cooling globule that congeals into incorporates in water, all particles such as soot and ashes also can only disappear in water owing to losing this carrier of gas, thus reach the object of smoke dispersal, dust removal and desulphurization, simultaneously, also CO is solved
2greenhouse gas emission problem.Again because the water in smoke dust hydrator has sealed Boiler smoke tube gas outlet completely, make burner hearth heat unlikely lost, be actually the effect served as burner hearth insulation, improve the thermal efficiency and energy utilization rate, for useful contribution has been made in energy-saving and emission-reduction, use apparatus of the present invention not only there is no negative interaction, but also significantly can reduce set noise.
3, from the economic and social benefit produced, invest little, instant effect.Meanwhile, the greasy dirt filtered out and other compound also recoverable, turn waste into wealth.
Above-mentioned explanation is only the general introduction of technical solution of the present invention, in order to technological means of the present invention can be better understood, and can be implemented according to the content of description, and can become apparent to allow above and other object of the present invention, feature and advantage, below especially exemplified by preferred embodiment, and coordinate accompanying drawing, be described in detail as follows.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of the first embodiment of smoke dust hydrator of the present invention.
Fig. 2 is the schematic diagram of the second embodiment of smoke dust hydrator of the present invention.
Fig. 3 is the schematic diagram of the 3rd embodiment of smoke dust hydrator of the present invention.
Fig. 4 is the schematic diagram of the 4th embodiment of smoke dust hydrator of the present invention.
[main element symbol description]
1: the first container 2: main air inlet pipe
3: diffluence room 4: air inlet is in charge of
5: umbrella is cut 6: the first tubulars of indulging in serfing the Net and cut and indulge in serfing the Net
The heavy ash pipe of 7: the first conical pipe 8: the first
9: the first escape pipes 10: heavy grey room
10 ': left heavy grey room 10 ": right heavy grey room
11: flange 12: access hole
13: sewage pump 14: blowoff valve
15: support column 16: water level
17: water-level gauge 18: water filling port
19: extension tube 20: second container
21: the second tubulars cut 22: the second conical pipes of indulging in serfing the Net
23: the second heavy ash pipe 24: the second escape pipes
25: outlet pass 26: discharging valve
27: the three container 28: the three tubulars cut indulges in serfing the Net
The heavy ash pipe of 29: the triconic pipe 30: the three
31: the three escape pipes 33: water filling port
34: water level 35: water-level gauge
36: the four container 37: the four air inlet pipe
38: the four tubulars cut 39: the four conical pipes of indulging in serfing the Net
40: the four heavy ash pipes 41: blow-off pipe
42: filter net type conveyer belt 43: filtering ponds
Detailed description of the invention
For further setting forth the present invention for the technological means reaching predetermined goal of the invention and take and effect, below in conjunction with accompanying drawing and preferred embodiment, to a kind of detailed description of the invention of smoke dust hydrator proposed according to the present invention, structure, feature and effect thereof, be described in detail as follows.
Referring to Fig. 1, is the first embodiment of smoke dust hydrator of the present invention.In this embodiment, smoke dust hydrator comprises: the first container 1, main air inlet pipe 2, diffluence room 3, multiple air inlet are in charge of 4, umbrella is cut the 5, first tubular of indulging in serfing the Net and cut the indulge in serfing the Net heavy ash pipe 8 of the 6, first conical pipe 7, first and the first escape pipe 9.The below of the first container 1 is provided with heavy grey room 10, and main air inlet pipe 2 is passed and is fixed in the top of the first container 1, and therefore, one end of main air inlet pipe 2 extends to the first container 1 inside, and it is outside that the other end extends to the first container 1.Diffluence room 3 is the cavity of hollow, its top is provided with opening to connect one end that main air inlet pipe 2 extends to the first container 1 inside, multiple opening is provided with to connect the upper end that multiple air inlet is in charge of 4 bottom it, diffluence room 3 Main Function reduces powerful air pressure and blast in unit are, to the pressure of water in container and impulsive force, to avoid occurring channeling water problem.The lower end that air inlet is in charge of 4 is connected with the first tubular and cuts and indulge in serfing the Net 6, first tubular cuts to indulge in serfing the Net and 6 can weld some stainless steel strips by the lower end being in charge of 4 in air inlet, as rack, the first tubular cut indulge in serfing the Net 6 around steel bar closed be wrapped in peripheral a week of steel bar rack and formed.This first tubular cut the air inlet of indulging in serfing the Net above 6 be in charge of 4 outside be arranged with umbrella and cut and indulge in serfing the Net 5, the level height that this umbrella cuts 5 lower ends of indulging in serfing the Net is set to not cut higher than the first tubular the level height of 6 lower ends of indulging in serfing the Net, and umbrella cut indulge in serfing the Net 5 and first the tubular angle that cuts 6 formation of indulging in serfing the Net be 30 degree about-60 degree and be advisable, cutting to make umbrella indulges in serfing the Net 5 cuts the first tubular to indulge in serfing the Net in umbrella and 6 to cover, such setting cuts indulges in serfing the Net, further filtration can either be played, be unlikely to network blocking again, and the power of channeling water can be weakened.For making clean-up effect better, umbrella is cut 5 peripheries can being in charge of 4 in air inlet of indulging in serfing the Net and is arranged multilayer, but be advisable with 1-2 layer, because umbrella cut indulge in serfing the Net 5 and first tubular cut to indulge in serfing the Net and 6 be detailed catalogue and cut and indulge in serfing the Net, mainly with stainless steel or other corrosion resistant metals or plastic mesh for material, be advisable about mesh about 50 order-60 order, it has splendid interception bubble, the effect of filtering smoke.First tubular cut indulge in serfing the Net 6 lower end connect the upper end great Kou of the first conical pipe 7, the lower end osculum of the first conical pipe 7 connects the first heavy ash pipe 8, the lower end of many first heavy ash pipes 8 is merged into a pipeline and extends in the heavy grey room 10 below the first container, and the angle that the tube wall that the tubular of domatic and its upper vertical of other first conical pipe 7 tube wall cuts frame of indulging in serfing the Net is formed and first below it sink the camber of ash pipe 8 and be advisable to be no more than about 150 degree.Hole (not shown) can be provided with, when clearing up lime-ash sediment, being filled in by giant in hole, utilizing the impulsive force of water to carry out washing away cleaning in the appropriate location of heavy grey room 10 shell.Bottom heavy grey room 10, be also provided with blowoff valve 14 and sewage pump 13, blowoff valve 14 is for discharging water and scarfing cinder, and sewage pump 13 is for extracting out the dirt inside heavy grey room 10.If container is comparatively large, heavy ash pipe end-to-end distance is indulged in serfing the Net far away from cutting, and bubble not easily from the heavy ash pipe end of bottom out, then separately can not establish heavy grey room, and direct bottom sewage pump 13 being placed in the first container 1.Appropriate location outside the first container 1 also establishes water-level gauge 17 to show the water level of the first container 1 inside.Above the first container 1, appropriate location can be provided with water filling port 18, in order to the first container 1 internal water flooding.First container 1 housing should be designed to vertical cylinder shape, the upper part of cylindrical shell can be set to end cap or flat cover shape, the lower part of cylindrical shell is arranged to taper (infundibulate), enters in the heavy grey room 10 of bottom along the slope of the first container 1 lower taper to make cutting from the first tubular the particle, sediment, dust etc. that the gas of to indulge in serfing the Net 6 out precipitates through water purification.Many heavy ash pipes also can directly vertically insert in the heavy grey room 10 below it through the first container 1 lower hopper shape bullet, to make particle enter heavy grey room 10 more swimmingly, prevent from blocking heavy ash pipe.The lower outside of the first container 1 is also provided with support column 15, in order to support whole container.In the first heavy ash pipe 8 lower end welding extension tube 19 perpendicular to ground level, extend on the slope of the first container 1 bottom below it, as the bracing frame of global facility above it, to play stabilization, if in the first heavy ash pipe 8 vertically inserts below it heavy grey room 10 or indentation sink ash pipe near time domatic bottom infundibulate cone inwall; do not need to arrange extension tube 19.One end of first escape pipe 9 is fixed in the top of the first container 1, and the other end extends to the outside of the first container 1, and the gas passed into, through the purification of the first container 1 inside, is then discharged from the first escape pipe 9, obtained smokeless, dustless pure air.
Above-mentioned smoke dust hydrator is mainly used in the purification of the boiler smoke with existing desulfurizer, because the catharsis of existing purifier is not thorough, after smoke dust hydrator in first embodiment is arranged on existing purifier, existing purifier alleviates purification burden for smoke dust hydrator of the present invention, and smoke dust hydrator of the present invention then can play the effect of thoroughly purification on this basis.The quantity that the size specification of the first container 1 and air inlet are in charge of 4 can make according to the exhaust smoke level of boiler, in order to repair or replace the device of the first container 1 inside, the top of the first container 1 is preferably set to demountable lid, such as flange can be set at the first container 1 top, with the first container top for convenience detach, also access hole 12 can be provided with in the side of the first container 1, and in main air inlet pipe 2, first escape pipe 9, air inlet is in charge of 4, the upper end of the first heavy ash pipe 8 is equipped with flange 11, when more draping and maintenance activity, it is inner that operating personnel enters the first container 1 from access hole 12.To change device, then optionally can pull down main air inlet pipe 2, first escape pipe 9, air inlet is in charge of 4 and first flanges 11 on heavy ash pipe 8, to change corresponding device or to take out maintenance.
Concrete, smoke dust hydrator in this first embodiment is as follows to the purification process passing into flue gas: first, by water filling port 18 to water filling in the first container 1, water level 16 need exceed uppermost umbrella and cut and indulge in serfing the Net 5, stove cigarette enters diffluence room 3 by main air inlet pipe 2, and then be in charge of 4 by air inlet and cut through the first tubular and indulge in serfing the Net 6, the larger particles being greater than mesh in stove cigarette directly sinks in the heavy grey room 10 below it through the first conical pipe 7 and the first heavy ash pipe 8, flue gas meets the bubble that water is formed, cut from the first tubular in the process of to indulge in serfing the Net in 6 out by the first tubular cut indulge in serfing the Net 6 and umbrella cut to indulge in serfing the Net and 5 all to rack, particle in bubble incorporates in water completely, and precipitate gradually, slope through the first container 1 lower side enters in the heavy grey room 10 of bottom.Gas after being finally cleaned is discharged from the first gas outlet 9.
Refer to Fig. 2, for the second embodiment of the present invention, it adds first auxiliary purification device on the basis of the first embodiment, and (part that the present embodiment is identical with the first embodiment is no longer repeated, just the place different to it is described in detail), this first auxiliary purification device comprises: second container 20, second tubular cuts the indulge in serfing the Net heavy ash pipe 23 of the 21, second conical pipe 22, second and the second escape pipe 24.Wherein second container 20 is arranged at the side of the first container 1 and is provided with outlet pass 25 therebetween.Bottom second container 20, side is provided with discharging valve 26.First escape pipe 9 of the first container 1 passes second container 20 top and fixes in relevant position and second container 20 top seal, then second container 20 is extended into inner, one end that first escape pipe 9 extends into second container 20 inside connects the second tubular and cuts and indulge in serfing the Net 21, second tubular cuts the upper end great Kou that 21 lower ends of indulging in serfing the Net connect the second conical pipe 22, and the lower end osculum of the second conical pipe 22 connects the second heavy ash pipe 23.One end of second escape pipe 24 is fixed in second container 20 top, and the other end extends to the outside of second container 20.In the present embodiment, second tubular cut indulge in serfing the Net 21 level height and the first tubular cut indulge in serfing the Net 6 level height maintain an equal level, therefore, the water injected by water filling port 18 flow into second container 20 through outlet pass 25, when uppermost umbrella during water level 16 is higher than the first container 1 cut indulge in serfing the Net 5 time, water level 16 also must cut higher than the second tubular in second container 20 and indulge in serfing the Net 21, and make the water level of two containers keep balance, gas can reach good clean-up effect in two containers.
Smoke dust hydrator in second embodiment is mainly used for the gas cleaning of gasoline and diesel engine tail gas and the less coal stove or house owed by a citizen kitchen smoke etc. of smoke which, therefore the first container 1 in the present embodiment and second container more than 20 are made into square, the cuboid of traverse, cylindrical shape or ellipse etc., so that be placed on the appropriate location on automobile as ternary catalyzing unit or automotive oil tank.It should be noted that, what adopt in Fig. 2 is the rectangular shape of traverse, but the present embodiment is not restricted to this shape.Cut for the diffluence room of the smoke dust hydrator of gasoline and diesel engine tail gas clean-up, tubular indulge in serfing the Net, umbrella cuts and to indulge in serfing the Net and conical pipe, heavy ash pipe all can link together with the lid of container top, take off the screw on lid, all parts inside it just together can be brought up with container lid, facilitate draping and maintenance.Smoke dust hydrator in the present embodiment is much little relative to the smoke dust hydrator specification in the first embodiment, therefore, do not need to be provided with access hole, not be used in air inlet yet and be in charge of 4 and first heavy ash pipe 8 arranges flange, and external container does not need to arrange support column again to support.And just because of specification is little, highly low, so be easy to occur channeling water phenomenon, therefore in a second embodiment, heavy grey room below first container 1 is preferably improved to left heavy grey room 10 ' and the right side further and sinks grey room 10 "; many first heavy ash pipe 8 lower ends are combined into a pipeline and extend in left heavy grey room 10 '; left heavy grey room 10 ' is except being provided with the opening for heavy ash pipe; all the other places are all closed; therefore; even if there is bubble to enter left heavy grey room 10 ' from heavy ash pipe, also can not returns on the water surface in the first container 1 and run away.Right heavy grey room 10 " top be also provided with an opening, 6 gases out of indulging in serfing the Net are cut through water purification from the first tubular, residue in the impurity in water, dusts etc. sink to the bottom of the first container 1, and by right heavy grey room 10 " opening at top and enter right heavy grey room 10 " in, even if at this moment there is bubble to enter right heavy grey room 10 " in, also be the product after purification, emerge and be also safe from harm, and to be entered in the water of second container 20 by the first escape pipe 9 through the inner purified gas of the first container 1 and again purify, the gas that final purification is clean is discharged from the second escape pipe 24.
Refer to Fig. 3, for the third embodiment of the present invention, it adds second auxiliary purification device on the basis of the first embodiment, and (part that the present embodiment is identical with the first embodiment is no longer repeated, just the place different to it is described in detail), be mainly used in the purification of large smoke which boiler smoke.This second auxiliary clean room comprises: the 3rd container 27, the 3rd tubular cut and indulge in serfing the Net 28, triconic pipe 29, the 3rd heavy ash pipe 30 and the 3rd escape pipe 31.Wherein, the 3rd container 27 is arranged at the top of the first container 1, and the top of the first container 1 is as the bottom of the 3rd container 27, and the joint of the first container 1 and the 3rd container 27 can fix (not shown) with Flange joint.It is inner that first escape pipe 9 is positioned at the 3rd container 27, and in inverted U, its one end connection the 3rd tubular extending to the first container 1 outside cuts indulges in serfing the Net 28,3rd tubular cuts the upper end great Kou that 28 lower ends of indulging in serfing the Net connect triconic pipe 29, the lower end osculum of triconic pipe 29 connects the 3rd heavy ash pipe 30, in the 3rd container 27, the 3rd tubular cuts 28 lower ends of indulging in serfing the Net also can not establish triconic pipe 29 and the 3rd heavy ash pipe 30, even must not arrange lid.One end of 3rd escape pipe 31 is fixed in the top of the 3rd container 27, and it is outside that the other end extends to the 3rd container 27.Main air inlet pipe 2 through the top of the 3rd container, then is passed and is fixed in the top of the first container 1.The outside of the 3rd container 27 is provided with water-level gauge 35, and top is provided with water filling port 33, and also by the 3rd gas outlet 31 water filling, and do not arrange water filling port 33, below is provided with discharging valve 26.
During work, from water filling port 18 and water filling port 33 to water filling in container, and make the water level 34 in the 3rd container 27 higher than the 3rd tubular cut indulge in serfing the Net 28 upper end, water level 16 in first container 1 higher than umbrella cut indulge in serfing the Net 5 upper end, after flue gas enters the interior purification (purification process of flue gas in the first container 1 please refer to the first embodiment) of the first container 1 from main air inlet pipe 2, entered by the first escape pipe 9 in the water of the 3rd container 27 again and again purify, the harmless clean gas of final dustless and smokeless colorless and odorless is discharged from the 3rd escape pipe 31.
Refer to Fig. 4, for the fourth embodiment of the present invention, it adds a primary purifying device on the basis of second embodiment of the invention two-step purification, and (part that the present embodiment is identical with the second embodiment is no longer repeated, just the place different to it is described in detail), this primary purifying device and the first auxiliary purification device similar, it comprises: the 4th container 36, the 4th tubular cut the 38, the 4th conical pipe 39 of indulging in serfing the Net, the 4th heavy ash pipe 40 and the 4th air inlet pipe 37.4th container 36 is arranged at the opposite side of the first container 1, 4th air inlet pipe 37 is passed and is fixed in the top of the 4th container 36, its one end extends to the outside of the 4th container 36 and is connected with boiler induced-draft fan pipe, it is inner that the other end extends to the 4th container 36, one end that 4th air inlet pipe 37 extends to the 4th container 36 inside is connected with the 4th tubular and cuts and indulge in serfing the Net 38, 4th tubular cuts the upper end great Kou that 38 lower ends of indulging in serfing the Net connect the 4th conical pipe 39, the lower end osculum of the 4th conical pipe 39 connects the 4th heavy ash pipe 40, one end that main air inlet pipe 2 extends to the first container 1 outside is fixed in the top of the 4th container 36.The bottom of the first container 1, second container 20 and the 4th container 36 all with the first container 1 below heavy grey room 10 conducting, so that the particle be melted in water after purification is converged in the heavy grey room 10 below the first container 1 from the bottom of the first container 1, second container 20 and the 4th container 36 respectively.
The above-described fourth embodiment of the present invention is mainly used in the purification of large-sized boiler, three grades of purifiers, though therefore add a primary purifying device on the basis of the second embodiment two-step purification, but because the purposes of the 4th embodiment and the second embodiment is different, therefore the two is also different on form-factor, instead of increase a primary purifying device simply.Such as, in the fourth embodiment, the profile of the first container 1, second container 20 and the 4th container 36 is in fact the same with the profile of the first container 1 in the first embodiment, bottom is taper (infundibulate), and having support column 15 for supporting, its volume is also identical or similar with the first container 1 in the first embodiment.The bottom of the first container 1, second container 20 and the 4th container 36 all with the first container 1 below heavy grey room 10 conducting.The upper end that main air inlet pipe 2, first escape pipe 9, air inlet are in charge of the 4, first heavy ash pipe 8 all can be provided with flange.
The purification process of the 4th embodiment is as follows, first flue gas is passed into the 4th air inlet pipe 37, through the primary purifying of the 4th container 36 inside, mainly play cooling, decompression and remove the primary purifying effect of part particle, then the flue gas after primary purifying enters the first container 1 inside by main air inlet pipe 2 and carries out main purification, is cut the SO indulging in serfing the Net and purge finely ground particles with the acting in conjunction of water and remove in flue dust by detailed catalogue
2etc. harmful components, without any particle in gas out, but furnace temperature is lower during ignition of the boiler or coal, smoke which is larger, gas may be remained by a little residual cigarette, the residual cigarette of this little remains gas and finally purifies by second container 20 again, finally just becomes as pure air from the second escape pipe 24 gas out, and clean-up effect almost absolutely.Generally, only can reach absolutely clean-up effect by the first container 1 and second container 20 or the first container 1 and the 3rd container 27 two-step purification process, therefore, second embodiment and the 3rd embodiment are most preferred embodiments, its compact conformation, act on identical therewith, effect is all very desirable.
As shown in Figure 4, sewage in heavy grey room 10 and ashes are also extracted out by sewage pump 13, sewage is fed to filter net type conveyer belt 42 and filtering ponds 43 purified treatment further by blow-off pipe 41, Ash Water Separator is realized by filter net type conveyer belt 42, particle is transported to assigned address by filter net type conveyer belt 42, water flows in the filtering ponds 43 below conveyer belt 42, sand, boiler ash sediment or lime stone is placed in filtering ponds 43, process clean water can also be injected into internal tank of the present invention and recycle, and plays the effect of environmental protection.
Because the first, the 3rd and the 4th embodiment all purifies as relatively large boiler, containers size is larger, be not easy to occur channeling water problem, it is just passable that therefore a heavy grey room 10 is set, and heavy grey room, two, left and right need not be divided into as the second embodiment to prevent channeling water.
The present invention's produced problem in actual application can adopt following methods to solve:
1, adopt cutting in hydraulic giant and ethanol, washed with methanol container to indulge in serfing the Net, and keep there is the water covering and cut and indulge in serfing the Net in container, in case net gets rusty.Because the water in container always makes the water in apparatus of the present invention be in rapid flow state under the effect of gases at high pressure, cutting moment of indulging in serfing the Net is in the state of being washed, and therefore, mesh is not easily plugged in a state of use.
2, for the smoke dust hydrator of gasoline and diesel engine, in the winter time, a little anti-icing fluid can be put in the north in apparatus of the present invention, waste water raffinate after purifying vehicle exhaust is preferably poured in cinder pond or the filtering ponds that are placed with quick lime refilter and enter sewer, or in Pang Jian waste water treatment plant, through-traffic highway, and recycling is refined to useful component, avoid secondary pollution.
The above, it is only preferred embodiment of the present invention, not any pro forma restriction is done to the present invention, although the present invention discloses as above with preferred embodiment, but and be not used to limit the present invention, any those skilled in the art, do not departing within the scope of technical solution of the present invention, make a little change when the technology contents of above-mentioned announcement can be utilized or be modified to the Equivalent embodiments of equivalent variations, in every case be the content not departing from technical solution of the present invention, according to any simple modification that technical spirit of the present invention is done above embodiment, equivalent variations and modification, all still belong in the scope of technical solution of the present invention.
Claims (10)
1. a smoke dust hydrator, it is characterized in that, it comprises: the first container (1), main air inlet pipe (2), diffluence room (3), (4) are in charge of in multiple air inlet, umbrella cuts indulge in serfing the Net (5), the first tubular cuts indulge in serfing the Net (6), the first conical pipe (7), the first heavy ash pipe (8) and the first escape pipe (9); Wherein
Described main air inlet pipe (2) is passed and is fixed in the top of described first container (1), and it is inner that its one end extends to the first container (1), and it is outside that the other end extends to the first container (1);
The cavity that described diffluence room (3) is hollow, the opening at its top connects described main air inlet pipe (2) and extends to the inner one end of the first container (1), and the multiple openings bottom it connect the upper end that (4) are in charge of in described multiple air inlet;
The lower end that (4) are in charge of in described multiple air inlet is all connected with described first tubular and cuts indulge in serfing the Net (6), and the air inlet that this first tubular cuts (6) top of indulging in serfing the Net is in charge of and is arranged with described umbrella outside (4) and cuts indulge in serfing the Net (5);
Described first tubular cuts the upper end great Kou of described first conical pipe (7) of lower end connection of indulge in serfing the Net (6), the lower end osculum of described first conical pipe (7) connects the described first heavy ash pipe (8), and the lower end of the multiple first heavy ash pipe (8) is merged into a pipeline and extends to the heavy grey room (10) of described first container (1) below;
One end of described first escape pipe (9) is fixed in the top of described first container (1), and the other end extends to the outside of described first container (1).
2. smoke dust hydrator according to claim 1, it is characterized in that, it also comprises: second container (20), the second tubular cut indulge in serfing the Net (21), the second conical pipe (22), the second heavy ash pipe (23) and the second escape pipe (24); Wherein
Described second container (20) is arranged at the side of described first container (1);
Described first escape pipe (9) extends to the outside one end of described first container (1) and passes and be fixed in the top of described second container (20) and extend to described second container (20) inside, this one end extending to described second container (20) inside is connected with the second tubular and cuts indulge in serfing the Net (21), this second tubular cuts the upper end great Kou that (21) lower end of indulging in serfing the Net connects the second conical pipe (22), and the lower end osculum of described second conical pipe (22) connects the described second heavy ash pipe (23);
One end of described second escape pipe (24) is fixed in the top of described second container (20), and it is outside that the other end extends to described second container (20);
Described second tubular cuts the height that the height of indulge in serfing the Net (21) and described first tubular cut indulge in serfing the Net (6) and maintains an equal level.
3. smoke dust hydrator according to claim 1, it is characterized in that, it also comprises: the 3rd container (27), the 3rd tubular cut indulge in serfing the Net (28), triconic pipe (29), the 3rd heavy ash pipe (30) and the 3rd escape pipe (31); Wherein
The 3rd described container (27) is arranged at the top of described first container (1), and the top of described first container (1) becomes the bottom of described 3rd container (27);
It is inner that described first escape pipe (9) is positioned at described 3rd container (27), and in inverted U, its one end connection the 3rd tubular extending to described first container (1) outside cuts indulge in serfing the Net (28), 3rd tubular cuts the upper end great Kou that (28) lower end of indulging in serfing the Net connects triconic pipe (29), and the lower end osculum of this triconic pipe (29) connects the described 3rd heavy ash pipe (30);
One end of described 3rd escape pipe (31) is fixed in the top of described 3rd container (27), and it is outside that the other end extends to described 3rd container (27);
Described main air inlet pipe (2) through the top of described 3rd container (27), then is passed and is fixed in the top of described first container (1).
4. smoke dust hydrator according to claim 2, characterized by further comprising: the 4th container (36), the 4th tubular cut indulge in serfing the Net (38), the 4th conical pipe (39), the 4th heavy ash pipe (40) and the 4th air inlet pipe (37); Wherein
Described 4th container (36) is arranged at the opposite side of described first container (1);
Described 4th air inlet pipe (37) is passed and is fixed in the top of described 4th container (36), its one end extends to the outside of the 4th container (36), it is inner that the other end extends to the 4th container (36), described 4th air inlet pipe (37) extends to the inner one end of the 4th container (36) and is connected with the 4th tubular and cuts indulge in serfing the Net (38), 4th tubular cuts the upper end great Kou that (38) lower end of indulging in serfing the Net connects the 4th conical pipe (39), and the lower end osculum of the 4th conical pipe (39) connects the described 4th heavy ash pipe (40);
Described main air inlet pipe (2) extends to the top that the outside one end of the first container (1) is fixed in described 4th container (36);
The bottom of described first container (1), second container (20) and the 4th container (36) all with heavy grey room (10) conducting of described first container (1) below.
5. smoke dust hydrator according to claim 2, is characterized in that, is provided with outlet pass (25) between described first container (1) and second container (20); The heavy grey room of described first container (1) below is divided into left heavy grey room (10 ') and the right side to sink grey room (10 "), and the lower end of the multiple first heavy ash pipe (8) merges into a pipeline and the left side extended to below described first container (1) sinks grey room (10 ').
6. smoke dust hydrator according to claim 3, it is characterized in that, the outside of the 3rd described container (27) is provided with water-level gauge (35), and the water level (34) in the 3rd container (27) cuts the upper end of indulge in serfing the Net (28) higher than described 3rd tubular.
7. the smoke dust hydrator according to any one of claim 1 to 5, is characterized in that, the level height that described umbrella cuts (5) lower end of indulging in serfing the Net does not cut the level height of (6) lower end of indulging in serfing the Net higher than described first tubular.
8. the smoke dust hydrator according to any one of claim 1 to 5, it is characterized in that, the outside of described the first container (1) is provided with water-level gauge (17), and the water level (16) in the first container (1) cuts the upper end of indulge in serfing the Net (5) higher than described umbrella.
9. the smoke dust hydrator according to any one of Claims 1-4, is characterized in that, is provided with blowoff valve (14) bottom the heavy grey room of described the first container (1) below.
10. smoke dust hydrator according to claim 1, it is characterized in that, the upper end that described main air inlet pipe (2), the first escape pipe (9), air inlet are in charge of (4) and the first heavy ash pipe (8) is equipped with flange.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410520200.XA CN104289054A (en) | 2014-09-30 | 2014-09-30 | Smoke dust hydrator |
| CN201510071988.5A CN104667672B (en) | 2014-09-30 | 2015-02-11 | A kind of smoke dust hydrator |
| CN201520100469.2U CN204582833U (en) | 2014-09-30 | 2015-02-11 | A kind of smoke dust hydrator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410520200.XA CN104289054A (en) | 2014-09-30 | 2014-09-30 | Smoke dust hydrator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN104289054A true CN104289054A (en) | 2015-01-21 |
Family
ID=52309144
Family Applications (3)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410520200.XA Pending CN104289054A (en) | 2014-09-30 | 2014-09-30 | Smoke dust hydrator |
| CN201510071988.5A Expired - Fee Related CN104667672B (en) | 2014-09-30 | 2015-02-11 | A kind of smoke dust hydrator |
| CN201520100469.2U Withdrawn - After Issue CN204582833U (en) | 2014-09-30 | 2015-02-11 | A kind of smoke dust hydrator |
Family Applications After (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510071988.5A Expired - Fee Related CN104667672B (en) | 2014-09-30 | 2015-02-11 | A kind of smoke dust hydrator |
| CN201520100469.2U Withdrawn - After Issue CN204582833U (en) | 2014-09-30 | 2015-02-11 | A kind of smoke dust hydrator |
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| Country | Link |
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| CN (3) | CN104289054A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104941353A (en) * | 2015-07-10 | 2015-09-30 | 河南五星科技有限公司 | Purifier |
| CN109276984A (en) * | 2018-10-11 | 2019-01-29 | 蔡璟 | A kind of stage aluminium alloy smelting pollution processing neutralized system |
| CN117205753A (en) * | 2023-11-07 | 2023-12-12 | 上海汇舸环保科技集团股份有限公司 | Marine diesel engine exhaust gas dust removal and desulfurization equipment and application method thereof |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104289054A (en) * | 2014-09-30 | 2015-01-21 | 牟继才 | Smoke dust hydrator |
| CN105688547A (en) * | 2015-06-23 | 2016-06-22 | 魏中振 | Complete desulfurization, denitrification and dedusting |
| CN106838883B (en) * | 2016-12-23 | 2018-10-30 | 徐州立骏诚品服饰有限公司 | The no-pollution heat supplying device of non-exhaust emission |
| CN106705093B (en) * | 2016-12-23 | 2018-10-09 | 杭州悦山科技有限公司 | The good heating equipment of heating effect |
| CN109140423B (en) * | 2016-12-23 | 2020-02-11 | 上海碳索能源服务股份有限公司 | Heat supply method |
| CN106693584A (en) * | 2017-01-11 | 2017-05-24 | 靖江市易得力环保设备有限公司 | Wet-type dust collector |
| CN108644799A (en) * | 2018-04-16 | 2018-10-12 | 谢中 | A kind of circular form filter cigarette water heater |
| CN113813717A (en) * | 2021-10-19 | 2021-12-21 | 潘珍金 | Slow-flow type industrial waste gas purification device |
| CN114733303B (en) * | 2022-03-17 | 2023-09-19 | 南京宇清环境科技有限公司 | Medical waste instrument burns smoke and dust pollution-free processing apparatus |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2072864U (en) * | 1990-04-09 | 1991-03-13 | 国营江阳化工厂 | Self-cleaning shower dust remover |
| CN2077746U (en) * | 1990-12-04 | 1991-05-29 | 岳铭五 | High efficiency soak type water saving dust remover |
| CN103111142A (en) * | 2013-03-05 | 2013-05-22 | 牟继才 | Smoke dust hydrator |
| CN104289054A (en) * | 2014-09-30 | 2015-01-21 | 牟继才 | Smoke dust hydrator |
-
2014
- 2014-09-30 CN CN201410520200.XA patent/CN104289054A/en active Pending
-
2015
- 2015-02-11 CN CN201510071988.5A patent/CN104667672B/en not_active Expired - Fee Related
- 2015-02-11 CN CN201520100469.2U patent/CN204582833U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104941353A (en) * | 2015-07-10 | 2015-09-30 | 河南五星科技有限公司 | Purifier |
| CN109276984A (en) * | 2018-10-11 | 2019-01-29 | 蔡璟 | A kind of stage aluminium alloy smelting pollution processing neutralized system |
| CN117205753A (en) * | 2023-11-07 | 2023-12-12 | 上海汇舸环保科技集团股份有限公司 | Marine diesel engine exhaust gas dust removal and desulfurization equipment and application method thereof |
| CN117205753B (en) * | 2023-11-07 | 2024-02-06 | 上海汇舸环保科技集团股份有限公司 | Marine diesel engine exhaust gas dust removal and desulfurization equipment and application method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104667672A (en) | 2015-06-03 |
| CN204582833U (en) | 2015-08-26 |
| CN104667672B (en) | 2016-11-16 |
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Application publication date: 20150121 |