CN2613310Y - Hyperbolic pipe high-efficient fume purifier - Google Patents
Hyperbolic pipe high-efficient fume purifier Download PDFInfo
- Publication number
- CN2613310Y CN2613310Y CN 03215902 CN03215902U CN2613310Y CN 2613310 Y CN2613310 Y CN 2613310Y CN 03215902 CN03215902 CN 03215902 CN 03215902 U CN03215902 U CN 03215902U CN 2613310 Y CN2613310 Y CN 2613310Y
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- Prior art keywords
- curve
- dirt pocket
- main body
- dedusting
- water fender
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Abstract
The utility model is a hyperbolic pipe highly effective flue gas purifying device for the boiler flue gas purification, which comprises a dedusting main body (1), a dedusting chamber (2), and a dehydrating chamber (3), wherein the dedusting main body (1) is provided with a curve collapsible tube (5), a curve divergent pipe (7), and a honeycomb duct (8) and the like, the dedusting main body (1) is equipped in the dedusting chamber (2), the boiler flue gas enters from the curve collapsible tube (5) and mist mixes with the water solution adding with desulfurizer, under the action of the curve collapsible tube (5) and the curve divergent pipe (7), the flue gas absorbs the water fog and fully mixes, and then after sulfur reduction entering into the dedusting chamber (2) and the dehydrating chamber (3) through the honeycomb duct (8) for dedusting, thereby having the characteristics of simple structure, convenient manufacture and installment, good purifying effect, thereby being not easily second polluted.
Description
One, affiliated technical field
The utility model is a kind of device that is mainly used in boiler flue gas purification, is a kind ofly to collect dedusting and desulfurization is the smoke eliminator of one.
Two, background technology
Present domestic smoke eliminator kind is a lot, with regard to wet desulfurization dust-removing device, mainly contains moisture film fiber crops stone clarifier, and impulse moisture film clarifier, Venturi tube moisture film clarifier etc. differ from one another.But these clarifiers exist complex structure, make inconvenience is installed, and clean-up effect is undesirable, easily produces shortcomings such as secondary pollution.
Three, summary of the invention
The purpose of this utility model provide a kind of simple in structure, make easy for installation, the efficient smoke eliminator of hyperbolic spool of good purification.
The technical solution of the utility model is: designed a hyp dedusting main body, utilized the variation of flue gas cross-sectional area in the dedusting main body and make change in flow, flue gas is fully fully mixed with the water smoke that is added with desulfurizing agent, reached the purpose of desulfurization, dedusting.Be that the utility model is made up of dedusting main body, dirt pocket, dewatering station etc.The dedusting main body is connected successively from top to bottom by curve collapsible tube, trunnion, curve anemostat, mozzle etc. and forms.Curve collapsible tube suitable for reading big, young down, the curve anemostat last young, end opening is big.Top in the curve collapsible tube is provided with spray thrower, and the garden perisporium of mozzle is provided with threaded hole, and the end opening of threaded hole is communicated with the end opening of mozzle.The dedusting main body is installed in the dirt pocket, the curve collapsible tube of dedusting main body upper end stretches out dirt pocket, suitable for reading and the boiler exhaust gas mouth of curve collapsible tube is communicated with, the spray thrower of curve collapsible tube is communicated with the water source that is added with desulfurizing agent, the end opening of dedusting main body lower end mozzle puts in the water of dirt pocket bottom, and the suitable for reading and dirt pocket of the threaded hole of mozzle is communicated with.Dewatering station is installed in a side of dirt pocket, is provided with smoke hole II between the top of dewatering station and dirt pocket, and dirt pocket is communicated with dewatering station (3) by smoke hole II.
Be to improve dust removing effects, can be in dirt pocket, be provided with dividing plate I between dedusting main body and the smoke hole II, the middle part of dividing plate is provided with smoke hole I.Be provided with water fender I in the dewatering station, water fender II; The upper end of water fender I is fixed on the upside of smoke hole II, and the lower end of water fender I is fixed on the bottom of dewatering station, and the bottom of water fender I is provided with smoke hole III.Water fender II is no less than 2, and water fender II is provided with smoke hole IV, and each water fender II is installed in the top of dewatering station and the smoke hole IV mutual dislocation on each water fender II in parallel to each other.The upper end of dewatering station is provided with outlet flue, and dewatering station is communicated with chimney by its outlet flue, also can be communicated with chimney by blower fan.Smoke hole I, smoke hole II, smoke hole III, smoke hole IV can be macropores, also can be many row's apertures.
When using the utility model, the flue gas of boiler is entered by the curve collapsible tube of dedusting main body upper end, spray thrower is the ejection of water smoke shape to the aqueous solution that is added with desulfurizing agent simultaneously, mix with flue gas, flue gas Via linear shrinkage pipe, trunnion is to the curve anemostat, the flow velocity that utilizes flue gas is with the curve collapsible tube, the variation of curve anemostat cross section and changing, make that flue gas and water smoke are more abundant to be mixed, desulfurizing agent in the water smoke and the sulfide in the flue gas are fully reacted, reach the purpose of desulfurization, and behind the material and the impurity absorption water in the flue gas that the reaction back generates, volumetric expansion, it is heavy that weight becomes, be convenient to dedusting, flue gas carries out the impulse washing through mozzle by the curve anemostat to the water of bottom, this moment, a large amount of heavier impurity just was trapped in the water, and flue gas is routed up from water, threaded hole on the mozzle perisporium is direction of rotation and enters dirt pocket, again by dirt pocket through smoke hole II, enter dewatering station, discharge by dewatering station again, flue gas is at dirt pocket, in the dewatering station, utilize the inertia force of flue gas, centrifugal force condenses upon each dividing plate with impurity in the flue gas and moisture content, each sidewall, on the water fender, reach the purpose of dedusting and fume-dehydrating effectively.
Therefore, the utlity model has simple in structurely, to make easy for installationly, characteristics such as good purification, flue gas after being purified be difficult for to produce secondary pollution.
Four, description of drawings
Accompanying drawing is the utility model schematic diagram.
Five, the specific embodiment
The utility model is made up of dedusting main body 1, dirt pocket 2, dewatering station 3 etc.Dedusting main body 1 includes curve collapsible tube 5, trunnion 6, curve anemostat 7, mozzle 8 etc.Curve collapsible tube 5, trunnion 6, curve anemostat 7, mozzle 8 connect from top to bottom successively.Curve collapsible tube 5 suitable for reading big, young down, that curve anemostat 7 is then gone up is young, end opening is big, tops in the curve collapsible tube 5 are provided with spray thrower 4, and spray thrower 4 is communicated with clear water reserviors in the sedimentation basin by noncorrosive pump, adds desulfurizing agent (as: lime etc.) in the clear water in clear water reserviors.Suitable for reading and the boiler exhaust gas mouth of curve collapsible tube 5 is communicated with.The end opening of mozzle 8 inserts in the water of dirt pocket 2 bottoms, and the garden perisporium on mozzle 8 tops is provided with threaded hole, and the quantity of threaded hole can determine as required that the end opening of threaded hole is communicated with the end opening of mozzle 8, and the suitable for reading and dirt pocket 2 of threaded hole is communicated with.Dewatering station 3 is fixed on a side of dirt pocket 2, is provided with smoke hole II between dewatering station 3 and dirt pocket 2, and dirt pocket 2 is communicated with dewatering station 3 by smoke hole II.Water is equipped with in dirt pocket 2 bottoms, is provided with dividing plate 11 in dirt pocket 2, between dedusting main body 1 and the smoke hole II, and the middle part of dividing plate 11 is provided with smoke hole I, is provided with water fender I9, water fender II10 in dewatering station 3.Upside, the lower end that the upper end of water fender I9 is fixed on smoke hole II is fixed on the bottom of dewatering station 3.The bottom of water fender I9 is provided with smoke hole III, and water fender II10 is two, also is provided with smoke hole IV on the water fender II10, two top that is fixed on dewatering station 3 and its smoke hole IV mutual dislocation that water fender II10 is parallel to each other.Dewatering station 3 upper ends are provided with outlet flue, and dewatering station 3 is communicated with chimney by outlet flue, also can be communicated with chimney by blower fan.
The flue gas that boiler is discharged is entered by curve collapsible tube 5, the water that is added with desulfurizing agent simultaneously is vaporific adding by spray thrower 4, flue gas and water smoke Via linear shrinkage pipe 5, trunnion 6, curve anemostat 7 enters mozzle 8, and fully mixed, sulfide and desulfurizing agent fully react neutralization in the flue gas, and flue gas enters the impurity that carries out in the water of mozzle 8 lower ends in the impulse washing flue gas and just is trapped in the water, carry out rough dusting, then along the threaded hole of mozzle in the shape of a spiral shape enter dirt pocket 2, impurity is at inertia force in the flue gas, under the action of centrifugal force with dividing plate 11, the sidewall collision cohesion of dirt pocket 2 is along dividing plate 11, the sidewall sedimentation obtains further dedusting.Flue gas again through smoke hole I, smoke hole II, enter dewatering station 3, under water fender I9 in dewatering station 3, the effect of water fender II10, further dedusting, dehydration, outlet flue by dewatering station 3 is discharged, and the water of dirt pocket 2 bottoms can flow into sedimentation basin and carries out precipitation process, and the clear water after the precipitation process flows in the clear water reserviors of sedimentation basin for reuse.
Because the utility model has guaranteed the gas-liquid contact to greatest extent, used multiple dust-removal and desulfurizing technology such as spray, collision cohesion, inertia force, centrifugal force, impulse Xian Di dexterously, realized simple in structurely, made easy for installation, good purification is difficult for causing characteristics such as secondary pollution.
Claims (3)
1, a kind of efficient smoke eliminator of hyperbolic spool that includes dirt pocket (2), dewatering station (3) is characterized in that also including dedusting main body (1); Dedusting main body (1) is connected successively from top to bottom by curve collapsible tube (5), trunnion (6), curve anemostat (7), mozzle (8) and forms; Top in the curve collapsible tube (5) is provided with spray thrower (4), and the garden perisporium of mozzle (8) is provided with threaded hole, and the end opening of threaded hole is communicated with the end opening of mozzle (8); Dedusting main body (1) is installed in the dirt pocket (2), the curve collapsible tube (5) of dedusting main body (1) upper end stretches out dirt pocket (2), the end opening of dedusting main body (1) lower end mozzle (8) puts in the water of dirt pocket (2) bottom, suitable for reading and the dirt pocket (2) of the threaded hole of mozzle (8) is communicated with, dewatering station (3) is installed in a side of dirt pocket (2), be provided with smoke hole II between the top of dewatering station (3) and dirt pocket (2), dirt pocket (2) is communicated with dewatering station (3) by smoke hole II.
2, according to the efficient smoke eliminator of the said hyperbolic spool of claim 1, it is characterized in that in dirt pocket (2), be provided with dividing plate (11) between dedusting main body (1) and the smoke hole II, the middle part of dividing plate (11) is provided with smoke hole I.
3,, it is characterized in that being provided with in the dewatering station (3) water fender I (9), water fender II (10) according to the efficient smoke eliminator of the said hyperbolic spool of claim 1; The upper end of water fender I (9) is fixed on the upside of smoke hole II, and the lower end of water fender I (9) is fixed on the bottom of dewatering station (3), and the bottom of water fender I (9) is provided with smoke hole III; Water fender II (10) is no less than 2, water fender II (10) be provided with smoke hole IV (, each water fender II (10) is installed in the top of dewatering station (3) and the smoke hole IV mutual dislocation on each water fender II (10) in parallel to each other; The upper end of dewatering station (3) is provided with outlet flue.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 03215902 CN2613310Y (en) | 2003-03-20 | 2003-03-20 | Hyperbolic pipe high-efficient fume purifier |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 03215902 CN2613310Y (en) | 2003-03-20 | 2003-03-20 | Hyperbolic pipe high-efficient fume purifier |
Publications (1)
Publication Number | Publication Date |
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CN2613310Y true CN2613310Y (en) | 2004-04-28 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 03215902 Expired - Fee Related CN2613310Y (en) | 2003-03-20 | 2003-03-20 | Hyperbolic pipe high-efficient fume purifier |
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CN (1) | CN2613310Y (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111617635A (en) * | 2020-06-16 | 2020-09-04 | 浙江天地环保科技股份有限公司 | Novel denitration reductant directly spout and mix device |
CN111874909A (en) * | 2020-07-29 | 2020-11-03 | 山西诺凯化工技术有限公司 | Integrated oxygen-heating method calcium carbide gas combined production method |
-
2003
- 2003-03-20 CN CN 03215902 patent/CN2613310Y/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111617635A (en) * | 2020-06-16 | 2020-09-04 | 浙江天地环保科技股份有限公司 | Novel denitration reductant directly spout and mix device |
CN111874909A (en) * | 2020-07-29 | 2020-11-03 | 山西诺凯化工技术有限公司 | Integrated oxygen-heating method calcium carbide gas combined production method |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |