CN2902416Y - Gas liquid separator used in smoke dust elimination, sulfur removing device - Google Patents
Gas liquid separator used in smoke dust elimination, sulfur removing device Download PDFInfo
- Publication number
- CN2902416Y CN2902416Y CN 200620071193 CN200620071193U CN2902416Y CN 2902416 Y CN2902416 Y CN 2902416Y CN 200620071193 CN200620071193 CN 200620071193 CN 200620071193 U CN200620071193 U CN 200620071193U CN 2902416 Y CN2902416 Y CN 2902416Y
- Authority
- CN
- China
- Prior art keywords
- gas
- flue gas
- liquid separator
- hollow
- separator
- 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 - Fee Related
Links
Landscapes
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The utility model is a gas-liquid separator used in devices that dedust and desulfurize smoke gas. The utility model has a small drag on smoke gas and can thoroughly separate liquid from gas. The utility model comprises a separator body that is provided with through-holes. The utility model is characterized in that the separator body is a hollow sphere or a hollow cylinder and the through-holes are distributed on the wall of the hollow sphere or cylinder. The material of the separator body is ceramics.
Description
(1) technical field
The utility model relates to the parts of environmental protection equipment, is specially the gas-liquid separator that uses in flue gas ash removal, the desulfurizer.
(2) background technology
At present, two kinds of structures of the normal employing of the gas-liquid separator that uses in flue gas ash removal, the desulfurizer, a kind of structure adopts filler to carry out gas-liquid separation exactly, and when flue gas passed through filler, the moisture in the filling adsorption flue gas, dust granule were finally realized gas-liquid separation; Another kind of structure adopts the porous dewatering plate to realize gas-liquid separation exactly, the flue gas that flows is through the hole of dewatering plate fast, flue gas can flow until going out dewatering plate along the hole spiral inner wall, and the centrifugal force that screw produces is thrown the liquid in the flue gas out, thereby realizes gas-liquid separation.The common drawback of above-mentioned two kinds of structures is exactly: resistance was bigger when flue gas passed through separator, and gas-liquid separation is not thorough, and the flue gas mass dryness fraction only can reach 97%.
(3) summary of the invention
At the weak point of existing gas-liquid separator, the utility model provides the gas-liquid separator that uses in a kind of flue gas ash removal, the desulfurizer, and less to the resistance of flue gas, gas-liquid separation is more thorough.
Its technical scheme is such; It comprises the separator body, and described body is provided with through hole, it is characterized in that: described body is hollow ball or hollow cylinder, and described through hole is distributed in the wall of described hollow ball or hollow cylinder.
It is further characterized in that: described hollow ball is an oval ball; Described hollow ball is a spherosome; The material of described separator body is a pottery.
The utility model adopts after the said structure, when flue gas will pass two through holes during by separator at least, and the decentraction nearly all of any two through holes on spheroid or the cylinder, and flue gas enters in the spheroid by a through hole or will rush at spheroid or cylindrical wall in the cylinder, wall rotates flue gas to flue gas huge impact power in spheroid or in the cylinder, thereby produce huge centrifugal force, make drop and flue dust in the wet flue gas be thrown to ball wall or cylindrical wall, dry flue gas is then discharged along spheroid or cylindrical other through hole, because centrifugal force is bigger, gas-liquid separation is more thorough like this, the flue gas mass dryness fraction can reach more than 98%, and through hole is distributed in spheroid or cylindrical curved surface, and the area of curved surface is greater than the area on plane, like this for onesize discharge flue, curved surface has increased through hole, reduced resistance accordingly to flue gas, and pottery has stronger gas permeability and adsorptivity, further guarantee the thorough separation of flue gas and can absorb subacidity drops a large amount of in the flue gas, can effectively avoid the corrosion of upstream device.
(4) description of drawings
Fig. 1, Fig. 2, Fig. 3 are respectively structural representation of the present utility model and partial sectional view.
(5) specific embodiment
The utility model comprises the separator body, and body is provided with through hole 2, and body is hollow ball or hollow cylinder; See Fig. 1, hollow ball is a hollow spheres 1, and this is embodiment 1; See Fig. 2, hollow ball is a hollow ellipse spheroid 3, and this is embodiment 2; See Fig. 3, body is a hollow cylinder 4, and this is embodiment 3; Through hole 2 is distributed in the wall of hollow spheres 1 or hollow ellipse spheroid 3 or hollow cylinder 4 respectively.The material of hollow spheres 1, hollow ellipse spheroid 3, hollow cylinder 4 is a pottery.Through hole 2 has a plurality of, concrete quantity to decide according to the size of body.
Claims (4)
1, the gas-liquid separator that uses in flue gas ash removal, the desulfurizer, it comprises the separator body, described body is provided with through hole, it is characterized in that: described body is hollow ball or hollow cylinder, and described through hole is distributed in the wall of described hollow ball or hollow cylinder.
2, according to the gas-liquid separator that uses in the described flue gas ash removal of claim 1, the desulfurizer, it is characterized in that: described hollow ball is an oval ball.
3, according to the gas-liquid separator that uses in the described flue gas ash removal of claim 1, the desulfurizer, it is characterized in that: described hollow ball is a spherosome.
4, according to the gas-liquid separator that uses in claim 2 or 3 described flue gas ash removals, the desulfurizer, it is characterized in that: the material of described separator body is pottery.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200620071193 CN2902416Y (en) | 2006-04-29 | 2006-04-29 | Gas liquid separator used in smoke dust elimination, sulfur removing device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200620071193 CN2902416Y (en) | 2006-04-29 | 2006-04-29 | Gas liquid separator used in smoke dust elimination, sulfur removing device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2902416Y true CN2902416Y (en) | 2007-05-23 |
Family
ID=38077818
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 200620071193 Expired - Fee Related CN2902416Y (en) | 2006-04-29 | 2006-04-29 | Gas liquid separator used in smoke dust elimination, sulfur removing device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2902416Y (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN117046297A (en) * | 2023-10-12 | 2023-11-14 | 常州宏川石化仓储有限公司 | Dry and wet waste gas conveying mechanism, vocs waste gas recycling system and recycling method |
-
2006
- 2006-04-29 CN CN 200620071193 patent/CN2902416Y/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN117046297A (en) * | 2023-10-12 | 2023-11-14 | 常州宏川石化仓储有限公司 | Dry and wet waste gas conveying mechanism, vocs waste gas recycling system and recycling method |
CN117046297B (en) * | 2023-10-12 | 2024-01-02 | 常州宏川石化仓储有限公司 | Dry and wet waste gas conveying mechanism, vocs waste gas recycling system and recycling method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105797855B (en) | A kind of gas cleaning plant | |
CN201524521U (en) | Large wet desulphurization device with wet-type electrostatic demister | |
CN203123767U (en) | Composite type dust collector | |
CN2902416Y (en) | Gas liquid separator used in smoke dust elimination, sulfur removing device | |
CN206454382U (en) | A kind of bundled tube dedusting demister collected with liquid | |
CN201015722Y (en) | Hybrid type highly effective dust remover | |
CN201279434Y (en) | Inner tower type double-cycle impulse desulfurization duster | |
CN112774320A (en) | Device and method for preventing secondary carrying and dedusting and demisting of rotational flow plate | |
CN201810558U (en) | Exhausting silencer of wet vacuum pup | |
CN206911039U (en) | A kind of high-efficiency swirl-type dedusting demister of fairing and application fairing | |
CN203598679U (en) | Cyclone device of dual-vortex flue gas washing tower | |
CN203971636U (en) | Inclined grille dust-removal and desulfurizing integrated device | |
CN205586773U (en) | Energy -saving desulfurization dust shaker | |
CN204543977U (en) | A kind of absorption tower with vortex-flow and defrosting plate | |
CN204193723U (en) | Eddy flow air intake twin-stage purifying dust-removing device | |
CN203990228U (en) | Wave-shape board water desulfurizing-dusting device | |
CN204073790U (en) | A kind of blue charcoal tail gas cooling, purifying system | |
CN207445965U (en) | A kind of lime stone-gypsum wet flue gas desulfurizing demister | |
CN201277580Y (en) | Boiler dust remover | |
CN202921093U (en) | Efficient wet desulphurization demister | |
CN202237590U (en) | Novel folding-line type two-passage defogger | |
CN101632891A (en) | Molecular screening protector | |
CN206008409U (en) | A kind of flue gas desulfurization and denitrification spray absorber | |
CN201552058U (en) | Electrostatic dust collection equipment | |
CN105879521A (en) | Method for capturing PM2.5 fine particles |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
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 |