CN201643975U - Spraying device of circulating slurry for desulfurizing flue gas - Google Patents
Spraying device of circulating slurry for desulfurizing flue gas Download PDFInfo
- Publication number
- CN201643975U CN201643975U CN2010201336144U CN201020133614U CN201643975U CN 201643975 U CN201643975 U CN 201643975U CN 2010201336144 U CN2010201336144 U CN 2010201336144U CN 201020133614 U CN201020133614 U CN 201020133614U CN 201643975 U CN201643975 U CN 201643975U
- Authority
- CN
- China
- Prior art keywords
- spray
- flue gas
- circulating slurry
- layer
- absorption tower
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Images
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model relates to a spraying device of circulating slurry for desulfurizing flue gas, which is arranged in an absorption tower (4) in a layered way, wherein each layer of spraying device is in a reticular structure comprising at least one main spraying pipe (1), a plurality of branch spraying pipes (2) separated out from both ends of the main spraying pipe (1) and a plurality of spray nozzles (3) separated out from both sides of each branch spraying pipe (2), and the main spraying pipe (1) is fixed on the absorption tower (4). The utility model overcomes the problems of deficient mixing of the flue gas and the circulating slurry of a traditional spraying device, no uniformity of a flow field in the absorption tower, larger resistance of the flue gas and the like. Compared with the traditional spraying device, the utility model lowers the energy consumption greatly and has convenient and quick construction and low cost.
Description
Technical field
The utility model relates to the circulating slurry sprinkling device that uses at the limestone-gypsum wet method fume desulfurizing system.More particularly it is a kind of circulating slurry sprinkling device for desulfurization of flue gas.
Background technology
Most power plant of China and industrial boiler adopt coal, wet goods fossil fuel usually, because the fossil fuel source is unstable, quality is unstable, sulfur content is higher, can produce harmful substances such as a large amount of sulfur dioxide in combustion process.In order to remove the sulfur dioxide in the boiler smoke, large-scale coal fired power plant is extensive use of the limestone-gypsum wet desulfurization system and carries out flue gas desulfurization.The absorption tower is one of most important device in this desulphurization system.One of most important equipment is exactly a spray equipment in the absorption tower.The tradition spray equipment generally has two kinds, and a kind of is the alloy shower, and a kind of is the fiberglass shower.Use the steel alloy shower, involve great expense, and because the shower irrational distribution, the shower internal pressure is unbalanced, cause the grout distribution inequality that sprays out, slurries easily precipitate, utilization rate is not high.Some sulfur-containing smoke gas can not fully be sprayed, and it is unclean to cause sulphur content to remove, and desulfuration efficiency remains further to be improved.For reaching clean cigarette purpose, must increase sprinkling equipment or increase spray time, the power consumption of recycle slurry liquid pump is significantly improved; Use the fiberglass shower, cost is cheaper, it is also more reasonable to spray, but because glass-reinforced plastic material insufficient rigidity, need to establish beam separately in tower and support, can cause the flow field inhomogeneous because beam is set on the one hand, local sulfur-containing smoke gas can not fully be sprayed, it is unclean to cause sulphur content to remove, and desulfuration efficiency remains further to be improved.For reaching clean cigarette purpose, must increase sprinkling equipment or increase spray time, the power consumption of recycle slurry liquid pump is significantly improved, because beam is set runner is formed extra obstacle on the one hand, cause whole flue gas system resistance to rise, must increase the pressure head of booster fan, make the power consumption of booster fan significantly promote.
Summary of the invention
The purpose of this utility model provides the circulating slurry sprinkling device that a kind of fume desulfurating absorption tower uses, and solve flue gas and loop slurry undercompounding, desulfuration efficiency and remain further raising, and problem such as the absorption tower flow field is inhomogeneous, and flue gas resistance is bigger.
The purpose of this utility model reaches by following measure: circulating slurry sprinkling device for desulfurization of flue gas, it is stratified and set in the absorption tower, it is characterized in that every layer of spray equipment is mainly by at least one spray person in charge, be responsible for a plurality of spray arms that two ends are told from spray, form from a plurality of nozzles that each spray arm both sides is told, described spray is responsible for and is fixed on the absorption tower.
In technique scheme, described spray is responsible for and is internal layer and the outer carbon steel pipe that is lined with the butyl rubber layer.
In technique scheme, described spray arm is to be internal layer and the outer glass reinforced plastic pipe that is lined with the wear-and corrosion-resistant layer.
In technique scheme, described spray arm is responsible for spray and is connected by flange.
In technique scheme, twine also bonding between described nozzle and the spray arm by fiberglass cloth.
In technique scheme, the end of described spray arm is arranged on the saddle bracket on the inwall of absorption tower.
In technique scheme, described nozzle is unidirectional downward spray structure or two-way spray structure, and the nozzle of unidirectional downward spray structure is positioned at the top layer spraying layer, and the nozzle of two-way spray structure is positioned at the below of top layer spraying layer.
1., energy consumption greatly reduces compare with the spray equipment of routine, the utility model has following beneficial effect:.Owing to do not need to be provided with in addition brace summer, make the absorption tower flow field more even on the one hand, reduced the dead angle of spray, make spray efficient improve greatly, greatly reduce the power consumption of recycle slurry liquid pump, compare with the spraying layer that is provided with brace summer, reaching under the condition of identical desulfuration efficiency, the energy consumption of recycle slurry liquid pump reduces by 3%; Make that on the other hand the absorption tower inner flow passage is more unobstructed, compare with the spraying layer that is provided with brace summer that it is about 6% that the absorption tower has been reduced the resistance of flue gas, the energy consumption of booster fan has reduced about 2%.2., construction is convenient.Spraying layer supporting construction of the present utility model is reasonable, and spray is responsible for and is directly fixed on the absorption tower, because rigidity own is enough big, so do not need to be provided with brace summer, makes that whole spraying layer is simple for structure.In the spraying layer spray be responsible for the spray arm between for flange is connected, this interface is arranged so that easy construction, quick, working face is little, is convenient to processing and manufacturing and scene installation.3., with low cost.Be lined with the carbon steel pipe material of butyl rubber inside and outside spray is responsible for and is adopted in the spraying layer of the present utility model, inside and outside adopting, the spray arm is lined with the glass reinforced plastic pipe material of wear-and corrosion-resistant layer, the slurries spray adopts sintered sic to make with nozzle, nozzle adopts the winding bonding way to be connected with shower, whole cost reduces greatly, investment is also reduced significantly, and its spraying layer cost has only the less than 20% of alloy material, hangs down about 10% than the spraying layer cost that fiberglass is responsible for.
Description of drawings
Fig. 1 is the structural representation of the utility model circulating slurry sprinkling device for desulfurization of flue gas (individual layer).
Fig. 2 sprays the connection diagram of being responsible for the absorption tower (the local amplification) in the utility model.
Fig. 3 is the saddle bracket schematic diagram of spray arm in the utility model.
Fig. 4 is the position view of the utility model spray equipment (bilayer) in the absorption tower.
1. sprays are responsible among the figure, 2. spray arm, 3. nozzle, 4. absorption tower.5. saddle bracket 6. from slurry circulating pump, 7. from flue gas system, 8. removes flue gas system.
The specific embodiment
Describe performance of the present utility model in detail below in conjunction with accompanying drawing, but they do not constitute to qualification of the present utility model, only do for example.Simultaneously by illustrating that advantage of the present utility model will become clear more and understanding easily.
Consult accompanying drawing as can be known: the utility model circulating slurry sprinkling device for desulfurization of flue gas, it is stratified and set in the absorption tower 4, every layer of spray equipment mainly is responsible for 1 (two or the more spray person in charge can be set as required) by at least one spray, be responsible for a plurality of spray arms 2 that 1 two ends are told from spray, form from a plurality of nozzles 3 that each spray arm 2 both sides is told, described spray is responsible for 1 and is fixed on (as Fig. 1, Fig. 2, shown in Figure 4) on the absorption tower 4.
Spray is responsible for 1 and is internal layer and the outer carbon steel pipe that is lined with the butyl rubber layer.Spray arm 2 is to be internal layer and the outer glass reinforced plastic pipe that is lined with the wear-and corrosion-resistant layer.Spray arm 2 and the spray person in charge 1 are connected by flange.Twine also bonding between nozzle 3 and the spray arm 2 by fiberglass cloth.
The end of spray arm 2 is arranged on the saddle bracket 5 on 4 inwalls of absorption tower (as shown in Figure 3).
The utility model is arranged in the flue gas desulfur device absorption tower, arranging multiplayer as required, the sprayed slurry of using is the lime stone slurry in the stock tank of absorption tower, or the mixed serum of lime stone slurry and gypsum slurries, sprayed slurry flows to the spray arm by being responsible for, flow to nozzle by the spray arm again, by spraying to the flue gas that flows after the nozzle atomization from bottom to top.Its effect is with the mixed serum atomizing, increases the contact area of slurries and flue gas, better flue gas is washed.
Every layer of spraying layer is provided with a recycle slurry liquid pump provides sprayed slurry for spray equipment, extracts slurries in the slush pump self-absorption tower stock tank, is responsible for---spraying arm---nozzle via spray, is conical ejection.
Claims (7)
1. circulating slurry sprinkling device for desulfurization of flue gas, it is stratified and set in the absorption tower (4), it is characterized in that every layer of spray equipment is mainly by at least one spray person in charge (1), be responsible for a plurality of spray arms (2) that (1) two ends are told from spray, form from a plurality of nozzles (3) that each spray arm (2) both sides is told, described spray is responsible for (1) and is fixed on the absorption tower (4).
2. circulating slurry sprinkling device for desulfurization of flue gas according to claim 1 is characterized in that it is internal layer and the outer carbon steel pipe that is lined with the butyl rubber layer that described spray is responsible for (1).
3. circulating slurry sprinkling device for desulfurization of flue gas according to claim 1 is characterized in that described spray arm (2) is to be internal layer and the outer glass reinforced plastic pipe that is lined with the wear-and corrosion-resistant layer.
4. circulating slurry sprinkling device for desulfurization of flue gas according to claim 1 is characterized in that the described spray arm (2) and the spray person in charge (1) are connected by flange.
5. circulating slurry sprinkling device for desulfurization of flue gas according to claim 1 is characterized in that twining by fiberglass cloth between described nozzle (3) and the spray arm (2) also bonding.
6. according to claim 3 or 4 described circulating slurry sprinkling device for desulfurization of flue gas, the end that it is characterized in that described spray arm (2) is arranged on the saddle bracket (5) on the inwall of absorption tower (4).
7. circulating slurry sprinkling device for desulfurization of flue gas according to claim 5, it is characterized in that described nozzle (3) is unidirectional downward spray structure or two-way spray structure, the nozzle of unidirectional downward spray structure (3) is positioned at the top layer spraying layer, and the nozzle of two-way spray structure (3) is positioned at the below of top layer spraying layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201336144U CN201643975U (en) | 2010-03-16 | 2010-03-16 | Spraying device of circulating slurry for desulfurizing flue gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201336144U CN201643975U (en) | 2010-03-16 | 2010-03-16 | Spraying device of circulating slurry for desulfurizing flue gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201643975U true CN201643975U (en) | 2010-11-24 |
Family
ID=43109171
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010201336144U Expired - Lifetime CN201643975U (en) | 2010-03-16 | 2010-03-16 | Spraying device of circulating slurry for desulfurizing flue gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201643975U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104174283A (en) * | 2014-09-10 | 2014-12-03 | 北京国能中电节能环保技术有限责任公司 | Bicirculating desulfuration system |
| CN105169915A (en) * | 2015-09-18 | 2015-12-23 | 江苏华星电力环保设备有限公司 | Novel desulphurization absorption tower |
| CN111408257A (en) * | 2020-04-14 | 2020-07-14 | 大唐环境产业集团股份有限公司 | Novel pipeline supporting structure |
-
2010
- 2010-03-16 CN CN2010201336144U patent/CN201643975U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104174283A (en) * | 2014-09-10 | 2014-12-03 | 北京国能中电节能环保技术有限责任公司 | Bicirculating desulfuration system |
| CN105169915A (en) * | 2015-09-18 | 2015-12-23 | 江苏华星电力环保设备有限公司 | Novel desulphurization absorption tower |
| CN111408257A (en) * | 2020-04-14 | 2020-07-14 | 大唐环境产业集团股份有限公司 | Novel pipeline supporting structure |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100450587C (en) | Circulating slurry sprinkling device for desulfurization of flue gas | |
| CN204911218U (en) | Desulfurization system is absorbed in circulation of dan tashuan district | |
| CN104857836A (en) | Flue gas desulfurization absorber interactive spray system | |
| CN102423619A (en) | Composite seawater desulfurization apparatus | |
| CN201643975U (en) | Spraying device of circulating slurry for desulfurizing flue gas | |
| CN202569948U (en) | Absorption device for wet-process smoke desulfurization and denitrification | |
| CN107837625A (en) | Flue gas desulfurization and dedusting spray equipment | |
| CN104888594B (en) | Closed multilevel water curtains desulphurization system | |
| CN206295798U (en) | A kind of wet desulphurization device with float valve sieve aperture combined tray | |
| CN201880465U (en) | Seawater desulfurizing spray tower | |
| CN207899165U (en) | Flue gas desulfurization and dedusting spray equipment | |
| CN202638199U (en) | Biomass fuel gas purification multi-stage sprayer | |
| CN203777931U (en) | Device for improving desulphurization efficiency of desulfurization spray tower and desulfurization spray tower | |
| CN2894805Y (en) | Flue gas desulfurizing circulating seriflux spraying apparatus | |
| CN203355603U (en) | Smoke purification system adopting wet method | |
| CN204865511U (en) | A desulfurization dust remover for brickfield | |
| CN101138697A (en) | Wet flue gas desulfurizing absorptive tower | |
| CN205127726U (en) | Double tower is two -way to spray multicycle desulfurization absorption tower | |
| CN204563884U (en) | A kind of desulfurizing tower | |
| CN204672130U (en) | The interactive spray system of fume desulfurating absorption tower | |
| CN207786322U (en) | A kind of novel Flue Gas Desulfurization with Pyrolusite Pulp apparatus and system | |
| CN203549873U (en) | Rice husk ash spraying collection device | |
| CN206837799U (en) | A kind of desulfurizing tower is with without dead angle spray structure | |
| CN201772472U (en) | Smoke wet desulphurization chimney | |
| CN205886582U (en) | Wet flue gas desulfurization lime stone supplies thick liquid device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20101124 |