CN201940141U - Water mill dust collector - Google Patents
Water mill dust collector Download PDFInfo
- Publication number
- CN201940141U CN201940141U CN2011200212416U CN201120021241U CN201940141U CN 201940141 U CN201940141 U CN 201940141U CN 2011200212416 U CN2011200212416 U CN 2011200212416U CN 201120021241 U CN201120021241 U CN 201120021241U CN 201940141 U CN201940141 U CN 201940141U
- Authority
- CN
- China
- Prior art keywords
- water mill
- water
- mill chamber
- chamber
- nozzle
- 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
Images
Landscapes
- Disintegrating Or Milling (AREA)
Abstract
The utility model relates to a water mill dust collector, which is characterized by comprising a water mill chamber A, a water mill chamber B, a high-pressure water pipe, a first deflection plate, a lower nozzle, a water mill tank, a gas inlet, a gas outlet, an upper nozzle, a division stone column, a water discharging port, a second deflection plate and a third deflection plate. The upper ends of the water mill chamber A and the water mill chamber B are connected, the lower end of the water mill chamber A is provided with the gas inlet, the upper end of the gas inlet is provided with the lower nozzle, the lower end of the lower nozzle is provided with the first deflection plate, the diversion stone column is arranged in the middle in the water mill chamber A, the middle part of the water mill chamber A is provided with the second deflection plate, the upper end of the second deflection plate is provided with the high-pressure water pipe, the high-pressure water pipe is connected with the upper nozzle, the upper end of the high-pressure water pipe is provided with the water mill tank, the high-pressure water pipe is arranged in the water mill tank, the side of the lower end of the water mill chamber A deviating from the gas inlet is provided with the water discharging port, and the lower end of the water mill chamber B is provided with the gas outlet. The water mill dust collector has a long service life, needs low investment, and is convenient to maintain and repair. Moreover, the water mill dust collector has high absorption efficiency and no pollution.
Description
Technical field
The utility model relates to a kind of water mill deduster, belongs to the chemical industry equipment field.
Background technology
During present calcium carbonate is produced, to purify carbon dioxide gas, most of producer uses condenser and purifying column to handle, yet when using these two kinds of equipment to handle, the water content of gas is too big, can cause the lost of life of follow-up equipment, strengthened production cost virtually, also strengthen the care and maintenance of equipment, be not suitable for large-scale continuous production, influenced production efficiency.
The utility model content
According to the deficiencies in the prior art, the technical problems to be solved in the utility model is: a kind of water mill deduster is provided, and long service life, the absorption efficiency height, and pollution-free.
The technical scheme that its technical problem that solves the utility model adopts is: a kind of water mill deduster is provided, it is characterized in that comprising: water mill chamber A, water mill chamber B, high-pressure water pipe, the first split flow plate, following nozzle, the water mill groove, air inlet, the gas outlet, top nozzle, the shunting stone column, discharge outlet, the second split flow plate and the 3rd split flow plate, water mill chamber A links to each other with the upper end of water mill chamber B, water mill chamber A lower end is provided with air inlet, the air inlet upper end is equipped with down nozzle, following nozzle lower end is provided with the first split flow plate, the shunting stone column is installed in the middle of in the water mill chamber A, water mill chamber A middle part is equipped with the second split flow plate, second split flow plate upper end is provided with high-pressure water pipe, high-pressure water pipe connects top nozzle, the water mill groove is installed in the high-pressure water pipe upper end, in the water mill groove high-pressure water pipe is installed, the side that water mill chamber A lower end deviates from air inlet is provided with discharge outlet, and water mill chamber B lower end is provided with the gas outlet.
Being shaped as of described water mill chamber A and water mill chamber B is cylindrical structure.
Described top nozzle is one or more.Wherein preferred 2 nozzles, and 2 the relative water mill chamber of nozzle A cylinder center of circle symmetries.
The junction of described water mill chamber A and water mill chamber B is provided with the 3rd split flow plate.
When air inlet is provided with, the center of circle of departing from water mill chamber A, do not point to the center of circle, after entering, gas at first sprays by following nozzle, control the direction that gas enters by the split flow plate then, make gas in water mill chamber A, do cyclonic motion around the shunting stone column, the water mill deduster is to use corrosion resistant basalt to be built into, when gas is done cyclonic motion inside, top nozzle and water mill groove that water mill chamber A middle part is provided with, also be provided with high-pressure water pipe in the water mill groove, when water overflows, form a circular water curtain from top to bottom like this, gas and dust be the network of rivers that forms by water curtain and top nozzle of face here just, split flow plate by water mill chamber A top enters water mill chamber B then, is discharged by the gas outlet of water mill chamber B lower end.
The beneficial effects of the utility model are: long service life, and equipment investment is few, makes things convenient for plant maintenance and maintenance, the absorption efficiency height, and pollution-free.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
1 is water mill chamber A among the figure; 2 is water mill chamber B; 3 is high-pressure water pipe; 4 is the first split flow plate; 5 are following nozzle; 6 is the water mill groove; 7 is air inlet; 8 is the gas outlet; 9 is top nozzle; 10 are the shunting stone column; 11 is discharge outlet; 12 is the second split flow plate; 13 is the 3rd split flow plate.
The specific embodiment
Below in conjunction with accompanying drawing embodiment of the present utility model is described further:
As described in Figure 1, the utility model comprises: water mill chamber A1, water mill chamber B2, high-pressure water pipe 3, the first split flow plate 4, following nozzle 5, water mill groove 6, air inlet 7, gas outlet 8, top nozzle 9, shunting stone column 10, discharge outlet 11, the second split flow plate 12 and the 3rd split flow plate 13, water mill chamber A1 links to each other with the upper end of water mill chamber B2, water mill chamber A1 lower end is provided with air inlet 7, the air inlet upper end is equipped with down nozzle 5, following nozzle 5 lower ends are provided with the first split flow plate 4, shunting stone column 10 is installed in the middle of in the water mill chamber A1, water mill chamber A1 middle part is equipped with the second split flow plate 12, the second split flow plate, 12 upper ends are provided with high-pressure water pipe 3, high-pressure water pipe 3 connects top nozzle 5, water mill groove 6 is installed in high-pressure water pipe 3 upper ends, high-pressure water pipe 3 is installed in the water mill groove 6, the side that water mill chamber A1 lower end deviates from air inlet is provided with discharge outlet 11, and water mill chamber B2 lower end is provided with gas outlet 8.
Being shaped as of water mill chamber A1 and water mill chamber B2 is cylindrical structure.
The junction of water mill chamber A1 and water mill chamber B2 is provided with the 3rd split flow plate 13.
When air inlet 7 is provided with, the center of circle of departing from water mill chamber A1, do not point to the center of circle, after entering, gas at first sprays by following nozzle 5, control the direction that gases enter by split flow plate 4 then, make gas in water mill chamber A1, do cyclonic motion around shunting stone column 10, the water mill deduster is to use stone to be built into, when gas is done cyclonic motion inside, top nozzle 9 and water mill groove 6 that water mill chamber A1 middle part is provided with, also be provided with high-pressure water pipe 3 in the water mill groove 6, when water overflows, form a circular water curtain from top to bottom like this, gas and dust be the network of rivers that forms by water curtain and top nozzle 9 of face here just, the 3rd split flow plate 13 by water mill chamber A1 top enters water mill chamber B2 then, is discharged by the gas outlet 8 of water mill chamber B2 lower end.
Claims (4)
1. water mill deduster, it is characterized in that comprising: water mill chamber A (1), water mill chamber B (2), high-pressure water pipe (3), the first split flow plate (4), following nozzle (5), water mill groove (6), air inlet (7), gas outlet (8), top nozzle (9), shunting stone column (10), discharge outlet (11), the second split flow plate (12) and the 3rd split flow plate (13), water mill chamber A (1) links to each other with the upper end of water mill chamber B (2), water mill chamber A (1) lower end is provided with air inlet (7), the air inlet upper end is equipped with down nozzle (5), following nozzle (5) lower end is provided with the first split flow plate (4), shunting stone column (10) is installed in the middle of in the water mill chamber A (1), water mill chamber A (1) middle part is equipped with the second split flow plate (12), the second split flow plate (12) upper end is provided with high-pressure water pipe (3), high-pressure water pipe (3) connects top nozzle (5), water mill groove (6) is installed in high-pressure water pipe (3) upper end, high-pressure water pipe (3) is installed in the water mill groove (6), the side that water mill chamber A (1) lower end deviates from air inlet is provided with discharge outlet (11), and water mill chamber B (2) lower end is provided with gas outlet (8).
2. water mill deduster according to claim 1 is characterized in that being shaped as of described water mill chamber A (1) and water mill chamber B (2) is cylindrical structure.
3. water mill deduster according to claim 1 is characterized in that described top nozzle (9) is for one or more.
4. water mill deduster according to claim 1 is characterized in that the junction of described water mill chamber A (1) and water mill chamber B (2) is provided with the 3rd split flow plate (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200212416U CN201940141U (en) | 2011-01-21 | 2011-01-21 | Water mill dust collector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200212416U CN201940141U (en) | 2011-01-21 | 2011-01-21 | Water mill dust collector |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201940141U true CN201940141U (en) | 2011-08-24 |
Family
ID=44467494
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011200212416U Expired - Fee Related CN201940141U (en) | 2011-01-21 | 2011-01-21 | Water mill dust collector |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201940141U (en) |
-
2011
- 2011-01-21 CN CN2011200212416U patent/CN201940141U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201988343U (en) | Ammonia gas and air Venturi mixer | |
| CN101530720A (en) | Acid fog absorption tower | |
| CN202654927U (en) | Rotational flow rectification gas-liquid absorbing tower | |
| CN215463249U (en) | Partitioned multistage circulating CO2Trapping concentration system | |
| CN204522719U (en) | Flue gas processing equipment of boiler | |
| CN202427338U (en) | Glass fiber reinforced plastic acid gas purifying tower | |
| CN206881311U (en) | Demisting separator | |
| CN103357246A (en) | Seawater desulfurization absorption tower for purifying smoke, desulfurization system and desulfurization method | |
| CN102728185A (en) | Tail gas absorbing device in acetone cyanohydrin production | |
| CN201940141U (en) | Water mill dust collector | |
| CN204447732U (en) | A kind of wet desulphurization CPR dust device and wet desulphurization absorption tower | |
| CN206809915U (en) | A kind of pneumatic combined demisting separator of flat board | |
| CN201959689U (en) | High-efficiency energy-saving washing tower | |
| CN211537149U (en) | Industrial waste gas handles environment-friendly device | |
| CN201643975U (en) | Spraying device of circulating slurry for desulfurizing flue gas | |
| CN201990481U (en) | Concentration device for dilute hydrochloric acid | |
| CN205145931U (en) | High -efficient whirlwind formula exhaust gas purification device | |
| CN204865511U (en) | A desulfurization dust remover for brickfield | |
| CN204684919U (en) | Smoke carbon dioxide capture absorption tower | |
| CN206881310U (en) | A kind of pneumatic combined demisting separator of flat board | |
| CN201389418Y (en) | Rotary spraying acid fog absorption tower | |
| CN201292348Y (en) | Novel biodiesel production reaction column | |
| CN207102121U (en) | Demisting separator | |
| CN207102122U (en) | A kind of pneumatic combined demisting separator of flat board | |
| CN201701860U (en) | Water distribution device of high-purity acid tail gas absorption tower |
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: 20110824 Termination date: 20140121 |