CN2936407Y - Spray tube in smoke desulfurizing process - Google Patents
Spray tube in smoke desulfurizing process Download PDFInfo
- Publication number
- CN2936407Y CN2936407Y CN 200620077437 CN200620077437U CN2936407Y CN 2936407 Y CN2936407 Y CN 2936407Y CN 200620077437 CN200620077437 CN 200620077437 CN 200620077437 U CN200620077437 U CN 200620077437U CN 2936407 Y CN2936407 Y CN 2936407Y
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- CN
- China
- Prior art keywords
- blade
- flue gas
- boss
- absorption tower
- gas desulfurization
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Abstract
The utility model discloses a demister of absorption tower which is used in flue gas desulfurization process, belonging to a part of limestone/lime - gypsum wet method flue gas desulfurization process in coal fired power plant. The utility model is characterized in that the work surface of the blade is provided with at least one boss. The blade is strip-shaped, the boss is arranged on the edge of both sides in blade width direction, and is distributed on the upper and lower surfaces of the blade. The boss outstands blade surface in spherical surface or round table or cylindrical or prismoid or prism shape. The blade shows curved face in width direction. The utility model greatly increases demisting efficiency of coal-fired power plant, enables the whole desulfurization system to be more perfect.
Description
Technical field
The utility model belongs to the part of thermal power plant process for flue gas desulfurization by limestone/lime-gypsum wet equipment, specifically, is a kind of device that is used for the absorption tower.
Background technology
In Coal,steam plant with FGD technology, the process for flue gas desulfurization by limestone/lime-gypsum wet device is used for removing the sulfur dioxide of boiler smoke, through after the washing of lime stone slurry, sulfur dioxide in flue gas is removed, simultaneously, flue gas has also carried a large amount of little water droplets, if directly be discharged to this flue gas in the air, a large amount of moisture in the flue gas can be lost, and serious corrosion can be caused the equipment in downstream.So, need carry out demist to the wet flue gas of free of water droplets (mist) and handle, device commonly used is a demister, the elementary cell of demister is a blade.
Summary of the invention
The purpose of this utility model provides absorption tower demisting apparatus in a kind of flue gas desulfurization course, makes the thermal power plant improve demist efficient greatly, makes whole desulphurization system more perfect.
Design according to the utility model provides is provided with at least 1 boss on the working surface of blade.
Blade is elongated, and boss is positioned at the both sides of the edge of width of blade direction, and is distributed on two surfaces up and down of blade.Boss is with sphere shape or truncated cone-shaped or cylindrical or terrace with edge shape or the prismatic surface that protrudes in blade.Blade is the curved surface shape on width.
The upper edge of width of blade direction has two boss, and lower edge has 4 boss, and the spacing of boss is 10～20mm, and the height of boss is 0.2～2mm, and the thickness of blade is 2.5～3mm.Fin is set on blade.Fin is positioned at the middle part on the width of blade.
Some blades equidistantly are installed in the demister unit with skewed in the longitudinal direction, and, the two ends of every length of blade direction lay respectively in the geometrical clamp in the demister unit, geometrical clamp is connected on the fixed head in the demister unit, and fixed head is installed on the crossbeam in the demister unit; The working face of every blade in vertical state, the spacing of adjacent two blades is 25～32mm.
The utility model has the advantages that: owing on the working face of blade, be provided with boss, the demist efficient of demister is greatly improved, reduces effectively or avoided the problem that secondary carries water droplet in the flue gas.
Description of drawings
Fig. 1 is an one-level demister blade schematic diagram.
Fig. 2 is the A-A view of Fig. 1.
Fig. 3 is the enlarged drawing of I among Fig. 2.
Fig. 4 is the enlarged drawing of II among Fig. 2.
Fig. 5 is a secondary demister blade schematic diagram.
Fig. 6 is the B-B view of Fig. 5.
Fig. 7 is the enlarged drawing of I among Fig. 6.
Fig. 8 is the enlarged drawing of II among Fig. 6.
Fig. 9 is the enlarged drawing of III among Fig. 6.
Figure 10 is the demister modules schematic diagram of being made up of blade.
Figure 11 is the vertical view of Figure 10.
Figure 12 is the D-D view of Figure 10.
The specific embodiment
As shown in the figure: blade 2 is elongated, and boss 3 is positioned at the both sides of the edge of blade 2 widths, and is distributed on two surfaces up and down of blade 2.Wherein the upper edge at blade 2 widths has two boss 3, and lower edge has 4 boss 3, and the spacing of boss 3 is 10～20mm, and the height of boss 3 is 0.2～2mm, and the thickness of blade 2 is 2.5～3mm.Blade 2 is the curved surface shape on width.Described boss 3 can be the surface that sphere shape or truncated cone-shaped or cylindrical or terrace with edge shape or shape such as prismatic protrude in blade 2.
Fin 4 can also be set on blade 2.Fin 4 is positioned at the middle part on the width of blade 2.
During installation, some blades 2 equidistantly are installed in the demister unit with skewed in the longitudinal direction, and, the two ends of every blade 2 length directions lay respectively in the geometrical clamp in the demister unit, geometrical clamp is connected on the fixed head in the demister unit, and fixed head is installed on the crossbeam in the demister unit; The working face of every blade 2 in vertical state, the spacing of adjacent two blades 2 is 25～32mm.
Demister and accessory system are made up of parts such as Multifolding Corrugated Plate, jig, brace summer, pressing plate and flooding nozzle, flushing pipe, pipeline support, pipe clamps usually.Take all factors into consideration demist efficient and pressure drop considerations, demister often adopts two-layer configuration.The arrangement form of demister is modal to have flat layout and ridge type to arrange.
Demister is arranged in the top on absorption tower usually, sulfur-containing smoke gas when the reaction zone and lime stone slurry carry out forming droplet after the neutralization reaction, droplet rises to the demister zone with flue gas, the effect of demister is exactly that droplet is captured.When the flue gas that contains droplet is flowed through the demister passage, the effect of impact of droplet, effect of inertia, turn to centrifugal force and make droplet be captured with rubbing action, the suction-operated of corrugated sheet, the structure that is folded to of demister corrugated sheet has increased the chance that droplet is captured more, thereby has improved demist efficient greatly.Usually require by the mean value of droplet content in time and spatial dimension behind the demister less than 75mg/Nm3 (mist droplet particle size is greater than 20 μ m).
Blade of the present utility model can be applicable to the ridge type demister.Be processed into a module by some blades 2, these modules are basic composition unit of demister.Demister is made up of one-level demister and secondary demister.The blade 2 of second level demister modules also has a fin 4 on its blade 2 except boss 3 is arranged, form hook-shaped groove on blade 2, and effect is in order to make the flue gas baffling, fully to contact, clash into blade 2, thus raising demist rate.
But the demister continuous operation temperature that the utility model is made into is 60 ℃, but continuous operation 2 minutes in the time of 100 ℃.The flue gas flow rate on absorption tower is generally 3-4m/s.The overall presure drop of whole demister is less than 150Pa.
The wet desulphurization absorption tower of certain engineering is by the droplet content average out to 3750mg/Nm before the demister
3, the droplet content mean value behind the process demister is less than 75mg/Nm
3The demist efficient of the utility model demister has reached more than 98%, satisfies the requirement in big-and-middle-sized thermal power plant.
The demist principle is: when flue gas during by the tortuous exhaust gases passes between two blades 2, utilize in the flue gas gravity, the inertia of water droplet and flue gas different, water droplet is captured in complications are advanced process is adsorbed on the blade, thereby separate the vapour-liquid two-phase, reach the purpose that reduces water droplet content in the flue gas.When water droplet is collected into when to a certain degree being gathered into big water droplet, just rely on gravity to flow down in the slurries pond.If when the water droplet particle that descends was big inadequately, so, the flue gas that the little water droplet of decline may be risen was taken away once more, produce secondary and carry, offset the effect of demist.Reach the optimum efficiency of demist, the form of blade is a key.Each blade of the present utility model all is a chevron-shaped, at the upper and lower edge of blade some little round boss is arranged all.
When flue gas is flowed through the demister passage, the effect of impact of droplet, effect of inertia, turn to centrifugal force and with the rubbing action of corrugated sheet, suction-operated makes droplet be captured by the demister blade, droplet can form large-area droplet at blade surface, because deadweight and blade surface are quite bright and clean, the automatic landing of droplet meeting, at first be to arrive the one-level boss 3 that is positioned at upside, it can be deposited on the boss 3 and can not taken away by flue gas, boss 3 is stacked into saturation state, unnecessary landing downwards again, arrival is positioned at the secondary boss 3 of downside, go down three grades successively, behind the level Four boss 3, droplet just is collected into big particle diameter water droplet basically, big flood drips and falls in the slurries pond, absorption tower, has reached the purpose that water droplet is separated from flue gas.Boss 3 can also make the flue gas commutation, has increased the effect of impact of droplet, helps it and is collected.Boss 3 has prevented that also the secondary of flue gas from carrying.
The main component of demister blade 2 is a polypropylene, and filler is a talcum powder.The width of blade 2 and height calculate according to concrete engineering demand to be decided.General wet process of FGD engineering adopts the secondary demister, and the blade 2 of this secondary demister is different, and the vane tip of higher level (second level) demister has a fin 4 that can form ditch type groove, and 2 in subordinate's (first order) blade does not have.
Claims (9)
1, absorption tower demisting apparatus in the flue gas desulfurization course is characterized in that: at least 1 boss (3) is set on the working surface of blade (2).
2, the device that absorption tower demisting is used in the flue gas desulfurization course according to claim 1, it is characterized in that: blade (2) is elongated, and boss (3) is positioned at the both sides of the edge of blade (2) width, and is distributed on two surfaces up and down of blade (2).
3, absorption tower demisting apparatus in the flue gas desulfurization course according to claim 1, it is characterized in that: boss (3) is with sphere shape or truncated cone-shaped or cylindrical or terrace with edge shape or the prismatic surface that protrudes in blade (2).
4, absorption tower demisting apparatus in the flue gas desulfurization course according to claim 1, it is characterized in that: the upper edge of blade (2) width has two boss (3), lower edge has 4 boss (3), the spacing of boss (3) is 10～20mm, the height of boss (3) is 0.2～2mm, and the thickness of blade (2) is 2.5～3mm.
5, absorption tower demisting apparatus in the flue gas desulfurization course according to claim 1, it is characterized in that: blade (2) is the curved surface shape on width.
6, absorption tower demisting apparatus in the flue gas desulfurization course according to claim 1 is characterized in that: fin (4) is set on blade (2).
7, as absorption tower demisting apparatus in the flue gas desulfurization course as described in the claim 6, it is characterized in that: fin (4) is positioned at the middle part on the width of blade (2).
8, as absorption tower demisting apparatus in the flue gas desulfurization course as described in one of claim 1 to 7, it is characterized in that: some blades (2) equidistantly are installed in the demister unit with skewed in the longitudinal direction, and, the two ends of every blade (2) length direction lay respectively in the geometrical clamp in the demister unit, geometrical clamp is connected on the fixed head in the demister unit, and fixed head is installed on the crossbeam in the demister unit; The working face of every blade (2) in vertical state, the spacing of adjacent two blades (2) is 25～32mm.
9, absorption tower demisting apparatus in the flue gas desulfurization course according to claim 1, it is characterized in that: the main component of blade (2) is a polypropylene, used filler is a talcum powder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620077437 CN2936407Y (en) | 2006-08-11 | 2006-08-11 | Spray tube in smoke desulfurizing process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620077437 CN2936407Y (en) | 2006-08-11 | 2006-08-11 | Spray tube in smoke desulfurizing process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2936407Y true CN2936407Y (en) | 2007-08-22 |
Family
ID=38360427
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620077437 Expired - Fee Related CN2936407Y (en) | 2006-08-11 | 2006-08-11 | Spray tube in smoke desulfurizing process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2936407Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1919421B (en) * | 2006-08-11 | 2010-05-12 | 江苏德克环保设备有限公司 | Absorption tower demisting apparatus in flue gas desulfurization process |
-
2006
- 2006-08-11 CN CN 200620077437 patent/CN2936407Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1919421B (en) * | 2006-08-11 | 2010-05-12 | 江苏德克环保设备有限公司 | Absorption tower demisting apparatus in flue gas desulfurization process |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070822 Termination date: 20120811 |