CN217989667U - Wet cyclone dust removal equipment - Google Patents
Wet cyclone dust removal equipment Download PDFInfo
- Publication number
- CN217989667U CN217989667U CN202221946720.3U CN202221946720U CN217989667U CN 217989667 U CN217989667 U CN 217989667U CN 202221946720 U CN202221946720 U CN 202221946720U CN 217989667 U CN217989667 U CN 217989667U
- Authority
- CN
- China
- Prior art keywords
- dust removal
- air inlet
- inlet chamber
- cyclone dust
- liquid
- 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.)
- Active
Links
Images
Landscapes
- Separation Of Particles Using Liquids (AREA)
- Cyclones (AREA)
Abstract
The utility model provides a wet process cyclone dust removal equipment, includes dust removal barrel, air inlet chamber way and whirlwind lumen, the air inlet chamber way one end is passed through whirlwind lumen intercommunication dust removal barrel, the fan is connected to the other end that the air inlet chamber said, be provided with a plurality of atomizing spray tubes in the air inlet chamber way, be provided with a plurality of atomizing nozzles on the atomizing spray tube, dust removal barrel top is provided with the air outlet, dust removal barrel below is provided with liquid collecting device. Compared with the prior art, the utility model discloses a wet process cyclone dust collecting equipment has following characteristics: the whole equipment has small volume; the dust removal efficiency is high, and fine dust particles with the particle size of less than 10 mu m can be removed; simple structure, convenient use and low maintenance cost.
Description
Technical Field
The utility model relates to a waste gas dust removal technical field, in particular to wet process cyclone dust collecting equipment.
Background
Conventional dry cyclone is generally used as a primary treatment device for dust removal. The separation efficiency of the method on fine dust particles is low, and the separation efficiency of fine powder can only reach 70-90%; and when the particle size is less than 5 mu, the centrifugal force of the particle is not enough to throw the particle on the inner wall, and the particle is too small to be carried out by the air flow which is re-involved in the central tube, so that the dust removal efficiency of the dust collector is limited. The bag type dust collector can be used as a primary dust collector or a secondary dust collector, has good effect, but has the same obvious defects that a cloth bag is easy to stick, the system resistance is large, the temperature of tail gas is too high, the possibility of combustion is high, and the maintenance cost is high; the packed tower is used for spray washing and serves as secondary dust removal equipment, the effect is achieved, the water consumption is large (800 Kg of water per t of powder under the circulating condition), and defoaming agents are required to be added when foam is generated seriously.
SUMMERY OF THE UTILITY MODEL
To prior art defect above, the utility model provides a wet process cyclone equipment as follows:
the technical scheme of the utility model is realized like this:
the utility model provides a wet process cyclone dust removal equipment, includes dust removal barrel, air inlet chamber way and whirlwind lumen, the air inlet chamber way one end is passed through whirlwind lumen intercommunication dust removal barrel, the fan is connected to the other end that the air inlet chamber said, be provided with a plurality of atomizing spray tubes in the air inlet chamber way, be provided with a plurality of atomizing nozzles on the atomizing spray tube, dust removal barrel top is provided with the air outlet, dust removal barrel below is provided with liquid collecting device.
Preferably, the atomizing spray pipe is vertically arranged in the air inlet cavity channel, and the atomizing nozzles on the atomizing spray pipe are uniformly arranged.
Preferably, the liquid collecting device comprises a conical liquid collecting tank, a liquid seal pipe and a liquid seal tank, the bottom surface of the conical liquid collecting tank is communicated with the lower part of the dust removal barrel, the top end of the conical liquid collecting tank is connected with the liquid seal pipe, and the liquid seal pipe is communicated with the liquid seal tank filled with solution.
Preferably, a manhole is arranged at the upper end of the air inlet cavity channel.
Compared with the prior art, the utility model discloses there is following beneficial effect:
the utility model discloses a wet cyclone dust removal device, in the process that dusty airflow enters a dust removal barrel from an air inlet cavity channel at high speed, the airflow is changed from linear motion to circular motion, when the airflow passes through the inlet of a cyclone cavity, water with certain pressure is atomized by an atomizing nozzle, and a water-sprayed curtain wall is formed at the inlet; after the airflow passes through the cyclone tube cavity, dust particles and liquid drops collide to be intercepted and condensed, water mist is combined to form particles larger than 10 mu, the particles are separated from the airflow under the centrifugal force action of cyclone separation, the dust-containing liquid drops flow out from the bottom of the dust removal cylinder body due to gravity, a water seal is arranged at the bottom of the dust removal cylinder body, and the purified airflow can only be discharged through an air outlet; the equipment can be matched with dry cyclone for secondary dust removal treatment; this beneficial effect includes: 1. the whole equipment volume is small, and the water consumption is greatly reduced; 2. the dust removal efficiency is high, and fine dust particles of less than 10 mu m can be removed; 3. simple structure, convenient use and low maintenance cost.
Drawings
FIG. 1 is a schematic structural view of the wet cyclone dust removal apparatus of the present invention;
fig. 2 is a top view of fig. 1.
In the figure: the dust removal device comprises a dust removal barrel body 1, an air inlet cavity channel 2, a cyclone tube cavity 3, an air outlet 4, an atomizing spray pipe 5, an atomizing nozzle 6, a conical liquid collecting tank 7, a liquid seal pipe 8, a liquid seal tank 9 and a manhole 10.
Detailed Description
The present invention will be described more fully and clearly with reference to the accompanying drawings, which are incorporated in and constitute a part of this specification.
As shown in fig. 1 and 2, a wet process cyclone dust removal equipment, including dust removal barrel 1, air inlet chamber way 2 and cyclone tube chamber 3, cyclone tube chamber 3 intercommunication dust removal barrel 1 is passed through to 2 one ends in air inlet chamber way, the fan is connected to the other end that air inlet chamber said 2, the fan is used for letting in dusty air current to equipment and removes dust, be provided with a plurality of atomizing spray pipes 5 in the air inlet chamber way 2, be provided with a plurality of atomizing spray nozzles 6 on the atomizing spray pipe 5, atomizing spray nozzle 6 is used for spraying the rivers in the atomizing spray pipe 5 and forms the curtain that one water sprays, dust removal barrel 1 top is provided with air outlet 4, purifies back air current and passes through air outlet 4 and discharges, dust removal barrel 1 below is provided with album of liquid device, album of liquid device is used for retrieving dusty liquid drop. The vertical setting of atomizing spray tube 5 is in air inlet chamber way 2, atomizing nozzle 6 on the atomizing spray tube 5 evenly sets up, makes the water that it sprays out drench curtain evenly distributed. The liquid collecting device comprises a conical liquid collecting tank 7, a liquid seal pipe 8 and a liquid seal tank 9, the bottom surface of the conical liquid collecting tank 7 is communicated with the lower part of the dust removing cylinder body 1, the top end of the conical liquid collecting tank 7 is connected with the liquid seal pipe 8, the liquid seal pipe 8 is led into the liquid seal tank 9 filled with solution, and the liquid seal tank 9 is arranged to prevent dust-containing liquid drops at the bottom of the dust removing cylinder body 1 from being sucked to the upper part again by high-speed rotating airflow. The upper end of the air inlet cavity channel 2 is provided with a manhole 10. For checking the operating condition of the atomising nozzle 5.
The working process is as follows:
the wet cyclone dust removal equipment is connected with an outlet pipeline of the fan when in use, and when the fan runs, the spraying water valve is opened simultaneously; the air flow from the outlet of the fan enters the air inlet cavity channel 2 along the straight line direction; after water with certain pressure is atomized by a specially selected atomizing nozzle 6, a curtain wall with water spraying is formed at an inlet; when the airflow passes through the cyclone tube cavity 3, dust particles and liquid drops collide to be intercepted and condensed, water mist is combined to form particles larger than 10 mu, the particles collide to be intercepted and condensed to form large liquid drops, the large liquid drops flow downwards along the tube wall in a spiral shape to the conical liquid collecting tank 7 to be discharged, the outer cyclone airflow which rotates and descends continuously flows into the central part of the dust removal tube body 1 in the descending process to form centripetal radial airflow, and the airflow forms inward cyclone which rotates upwards; the rotation directions of the inner rotational flow and the outer rotational flow are the same, the bottom of the dust removal cylinder 1 is provided with a water seal, and the purified air flow can only be discharged through the air outlet 4; because the water spray direction and the air flow direction are opposite, the air flow and the fog drops collide more intensely and contact more fully; therefore, the dust removal effect is better; when the device is used for secondary dust removal, the emission can reach less than 25mg/m < 3 > (ppm) which is far lower than the national standard, but the water consumption is only 20Kg/t powder to 25Kg/t powder which is far less than the water consumption of a tower spray washer (800 Kg/t powder), the collected water can be recycled, and the heat of the tail gas is fully utilized.
According to the structure of the utility model, the wet cyclone dust removal equipment of the utility model has small volume and greatly reduces water consumption; the dust removal efficiency is high, and fine dust particles with the particle size of less than 10 mu m can be removed; simple structure, convenient use and low maintenance cost.
Claims (4)
1. The utility model provides a wet process cyclone dust removal equipment, its characterized in that, says and whirlwind lumen including dust removal barrel, air inlet chamber says that one end passes through whirlwind lumen intercommunication dust removal barrel, the fan is connected to the other end that the air inlet chamber was said, air inlet chamber says and is provided with a plurality of atomizing spray tubes, be provided with a plurality of atomizing nozzles on the atomizing spray tube, dust removal barrel top is provided with the air outlet, dust removal barrel below is provided with liquid collecting device.
2. The wet cyclone dust removing apparatus as claimed in claim 1, wherein the atomizing nozzles are vertically arranged in the air inlet channel, and the atomizing nozzles on the atomizing nozzles are uniformly arranged.
3. The wet cyclone dust removal device as claimed in claim 1, wherein the liquid collecting device comprises a conical liquid collecting tank, a liquid seal pipe and a liquid seal tank, the bottom surface of the conical liquid collecting tank is communicated with the lower part of the dust removal cylinder, the top end of the conical liquid collecting tank is connected with the liquid seal pipe, and the liquid seal pipe is communicated with the liquid seal tank filled with the solution.
4. The wet cyclone dust collecting apparatus as claimed in claim 1, 2 or 3, wherein a manhole is provided at an upper end of the air inlet duct.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202221946720.3U CN217989667U (en) | 2022-07-27 | 2022-07-27 | Wet cyclone dust removal equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202221946720.3U CN217989667U (en) | 2022-07-27 | 2022-07-27 | Wet cyclone dust removal equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
CN217989667U true CN217989667U (en) | 2022-12-09 |
Family
ID=84316735
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202221946720.3U Active CN217989667U (en) | 2022-07-27 | 2022-07-27 | Wet cyclone dust removal equipment |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN217989667U (en) |
-
2022
- 2022-07-27 CN CN202221946720.3U patent/CN217989667U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN100482320C (en) | Gas absorption purifier | |
CN111298584B (en) | Double-venturi pneumatic wet dust removal system | |
CN106582121A (en) | Tube bundle type dedusting and demisting device with liquid collection function | |
CN108424792B (en) | Integrated cooling separator and working method thereof | |
WO2003084642A1 (en) | Dust collector | |
CN106390652A (en) | Wet type fine particle high-efficiency cyclone removal device | |
CN214319573U (en) | Dust remover miropowder system of recycling | |
CN108607312A (en) | A kind of ash-laden gas processing method and its device | |
CN209997390U (en) | dust removing device | |
CN216677569U (en) | Powder dust remover with dust fall function sprays | |
CN209397166U (en) | Purification device | |
CN205164414U (en) | Wet -type whirlwind water curtain dust collector | |
CN217989667U (en) | Wet cyclone dust removal equipment | |
CN103866067A (en) | Blast furnace coal gas gravitational dust collector with cooling effect | |
CN220878213U (en) | Novel high-efficient wet dedusting tower | |
CN210522148U (en) | Venturi and gas-liquid cyclone dust removal device | |
CN209076340U (en) | A kind of wet type three-stage dust catcher | |
CN108543632B (en) | Wet type cyclone dust collector capable of recycling washing liquid | |
CN205886495U (en) | Gas -liquid separating device | |
CN211462590U (en) | Metallurgical flue gas dust removal device | |
CN109277210B (en) | Novel VOCs waste gas dry-type pretreatment system equipment | |
CN208694571U (en) | A kind of water filtering cyclone dust collectors | |
CN209271703U (en) | A kind of novel VOCs exhaust gas dry type pre-processing system equipment | |
CN208151316U (en) | Integrated cooling separator | |
CN211462591U (en) | Dust removal collecting tower |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |