CN201832523U - Circulating water dedusting recoverer - Google Patents
Circulating water dedusting recoverer Download PDFInfo
- Publication number
- CN201832523U CN201832523U CN2010205807014U CN201020580701U CN201832523U CN 201832523 U CN201832523 U CN 201832523U CN 2010205807014 U CN2010205807014 U CN 2010205807014U CN 201020580701 U CN201020580701 U CN 201020580701U CN 201832523 U CN201832523 U CN 201832523U
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- China
- Prior art keywords
- baffling
- dedusting
- solid
- main frame
- equipment
- Prior art date
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- Expired - Fee Related
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Abstract
The utility model relates to a circulating water dedusting recoverer, which comprises a host machine tower and a baffling solid-liquid separation device, wherein the host machine tower is arranged above the baffling solid-liquid separation device, the bottom end part of the host machine tower is provided with a connecting pipe, and an outlet end of the connecting pipe is connected in the baffling solid-liquid separation device; the top end part of the host machine tower is provided with an air discharge port, the middle section of the side wall of the host machine tower is provided with an air inlet, the side wall of the host machine tower at the air inlet is provided with a shower pipe, a dust collecting leakage current plate is bridged on the inner wall of the host machine tower above the air inlet, and a baffling dehumidifying plate is bridged on the inner wall of the host machine tower above the dust collecting leakage current plate; and the outlet end of the baffling solid-liquid separation device is connected with a dedusting water recycling pipe which is provided with a water pump, and the outlet end of the dedusting water recycling pipe is connected with the inlet end of the shower pipe. The circulating water dedusting recoverer has low manufacturing price and less power cycle, dust can be highly recovered without environment pollution, and the water resource is highly utilized.
Description
Technical field
The utility model relates to a kind of environmental protection equipment, especially a kind of recirculated water dedusting recover.
Background technology
Need through surface treatment at metal processing industry, metal material industry, mechanical processing industry etc. more.Tradition adopts (traditional title add sprayer) such as metallic particles, bead, quartz sand, normal sands that material surface is adopted high-pressure injection, the oxide of removing material surface, machining residue, greasy dirt, dust etc., remove after the above solid matter, the necessary acidified processing in the surface that has, obtain cleaner material surface, for being coated with of back, plating, phosphatization, paint etc. ready.
In whole operation, owing to adopt high-pressure injection, sprayer hits pulverizing easily, produce a large amount of dust, contaminated environment is if further carry out acidification, produce a large amount of acid-bearing wastewaters and oily waste water again, must waste a large amount of water treatment expenses and medicament expense usefulness through sewage disposal, waste great amount of water resources simultaneously.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, provides that a kind of manufacturing price is low, circulation power is few, and dust can highly reclaim, free from environmental pollution and water resource reaches the recirculated water dedusting recover that highly utilizes.
The technical scheme that provides according to the utility model, described recirculated water dedusting recover, comprise main frame tower and baffling equipment for separating liquid from solid, the main frame tower is installed in baffling equipment for separating liquid from solid top position, the bottom of main frame tower is equipped with tube connector, and the port of export of tube connector is connected in the baffling equipment for separating liquid from solid; Exhaust outlet outside the top ends of main frame tower is provided with, sidewall middle section position at the main frame tower is provided with air inlet, on the main frame tower side wall of air inlet position, shower is installed, main frame inner wall of tower above air inlet has set up the grey leakage current plate of collection, and the main frame inner wall of tower above the grey leakage current plate of collection has set up baffling dehumidification plate; The port of export of described baffling equipment for separating liquid from solid is connected with dedusting water reuse pipe, on the dedusting water reuse pipe water pump is installed, and the port of export of dedusting water reuse pipe and the entrance point of described shower join.
The bottom of described main frame tower is taper.
Be fixed with the baffling lower plate on the bottom panel of described baffling equipment for separating liquid from solid, on the top panel of baffling equipment for separating liquid from solid, be fixed with the baffling upper plate, and baffling lower plate and baffling upper plate are and shift to install; Have one section flowing water space between the top ends of baffling lower plate and the top panel, have one section flowing water space between the bottom of baffling upper plate and the bottom panel; During work, dust-laden sewage baffling equipment for separating liquid from solid is walked snakelike and is slowed down and finish gravitational settling rapidly.
Described baffling lower plate and baffling upper plate are set in parallel.On the bottom panel of baffling equipment for separating liquid from solid, offer slag-drip opening.On the baffling equipment for separating liquid from solid sidewall of described baffling lower plate top ends top position, offer overfall.
Offer the baffling moisture removal holes on the described baffling dehumidification plate, the axis of the axis of baffling moisture removal holes and main frame tower is antarafacial and intersects setting.
On dedusting water reuse pipe, the pH value optical viewer is installed.
Device fabrication price of the present utility model is low, and circulation power is few, and dust can highly reclaim, and is free from environmental pollution, and water resource reaches highly to be utilized.If in water, add acid simultaneously, can reach the function on acidification surface, spent acid does not need adjustment to handle simultaneously.
Description of drawings
Fig. 1 is an overall structure schematic diagram of the present utility model.
Fig. 2 is the structural representation of the baffling dehumidification plate in the utility model.
The specific embodiment
The utility model is described in further detail below in conjunction with concrete drawings and Examples.
As shown in the figure: this recirculated water dedusting recover, comprise main frame tower 1 and baffling equipment for separating liquid from solid 2, main frame tower 1 is installed in baffling equipment for separating liquid from solid 2 top positions, and the bottom of main frame tower 1 is equipped with tube connector 3, and the port of export of tube connector 3 is connected in the baffling equipment for separating liquid from solid 2; Exhaust outlet 4 outside the top ends of main frame tower 1 is provided with, sidewall middle section position at main frame tower 1 is provided with air inlet 5, on main frame tower 1 sidewall of air inlet 5 positions, shower 6 is installed, main frame tower 1 inwall above air inlet 5 has set up the grey leakage current plate 7 of collection, and main frame tower 1 inwall above the grey leakage current plate 7 of collection has set up baffling dehumidification plate 8; The port of export of described baffling equipment for separating liquid from solid 2 is connected with dedusting water reuse pipe 9, on the dedusting water reuse pipe 9 water pump 10 is installed, and the port of export of dedusting water reuse pipe 9 and the entrance point of described shower 6 join.
The bottom of described main frame tower 1 is taper.
Described baffling lower plate 12 is set in parallel with baffling upper plate 14.On the bottom panel 11 of baffling equipment for separating liquid from solid 2, offer slag-drip opening 15.On baffling equipment for separating liquid from solid 2 sidewalls of described baffling lower plate 12 top ends top positions, offer overfall 16.
Offer the baffling moisture removal holes 17 of One's name is legion on the described baffling dehumidification plate 8, the axis of the axis of baffling moisture removal holes 17 and main frame tower 1 is antarafacial and intersects setting.The gas that contains water smoke is when baffling dehumidification plate 8 belows enter baffling moisture removal holes 17, the gas that contains water smoke will at first strike the wall body of baffling moisture removal holes 17 and baffling, at the air impingement that contains water smoke during to the wall body of baffling moisture removal holes 17, water smoke is assembled on the wall body of baffling moisture removal holes 17 and is formed the globule, falls at last.
On dedusting water reuse pipe 9, pH value optical viewer 18 is installed.
Main frame tower 1 in the utility model is circular up-right tank for the cross section, whole up-right tank is divided into three chambeies, lumen is for carrying the air that contains dust, the air that has dust is created in the surface sand-blasting room, import by air-introduced machine by air inlet 5, arrange some showers 6 on main frame tower 1 wall body of air inlet 5 right opposites, water produces a large amount of water droplets through jet pipe, airborne dust is produced the bottom that is deposited to main frame tower 1 through humidification, the Separation of Solid and Liquid in baffling equipment for separating liquid from solid 2 is carried out in preparation, pass through dedusting water reuse pipe 9 then, water pump 10 uses continuously, carries out the aqueous solution of surperficial acidification if desired, can add needed acid in shower water, adjust pH value, on dedusting water reuse pipe 9, pH value optical viewer 18 is installed, only needs the content of continuous supplemental acid, do not need to carry out the adjustment of pH value.
Outer exhaust outlet 4 through the process of the gas behind humidification main frame tower 1 top enters atmosphere, and main frame tower 1 inwall above air inlet 5 is provided with circular collection ash leakage current plate 7, makes shower water not enter atmosphere.At the Position Design ring-type zigzag overflow launder that collects about 10 centimeters on grey leakage current plate 7 tops, the oil, ash, the foam that make the running water surface may produce accumulation efflux simultaneously, at the mouth of pipe that effluxes baffling dehumidification plate are installed, and make to efflux airborne moisture reduction.The bottom of main frame tower 1 is a tapered structure, make the solid in the water that contains solid produce cohesion rapidly, outside the bottom of main frame tower 1, be discharged in the baffling equipment for separating liquid from solid 2 then, baffling equipment for separating liquid from solid 2 designs for gravitational settling, therefore do not need promptly can obtain the recycle-water of relative clean through filtering.
Be fixed with baffling lower plate 12 on the bottom panel 11 of this baffling equipment for separating liquid from solid 2, on the top panel 13 of baffling equipment for separating liquid from solid 2, be fixed with baffling upper plate 14, and baffling lower plate 12 is with baffling upper plate 14 and shifts to install; Have one section flowing water space between the top ends of baffling lower plate 12 and the top panel 13, have one section flowing water space between the bottom of baffling upper plate 14 and the bottom panel 11; During work, dust-laden sewage baffling equipment for separating liquid from solid 2 is walked snakelike and is slowed down and finish gravitational settling rapidly.During processing, sewage from top, bottom, top, bottom are snakelike like this flows, flow velocity reduces rapidly, the fine particle rapid subsidence in the sewage, the water after the sedimentation continues to recycle through water pump 10.
Claims (8)
1. recirculated water dedusting recover, it is characterized in that: comprise main frame tower (1) and baffling equipment for separating liquid from solid (2), main frame tower (1) is installed in baffling equipment for separating liquid from solid (2) top position, the bottom of main frame tower (1) is equipped with tube connector (3), and the port of export of tube connector (3) is connected in the baffling equipment for separating liquid from solid (2); Exhaust outlet (4) outside the top ends of main frame tower (1) is provided with, sidewall middle section position at main frame tower (1) is provided with air inlet (5), on main frame tower (1) sidewall of air inlet (5) position, shower (6) is installed, main frame tower (1) inwall in air inlet (5) top has set up collection grey leakage current plate (7), and main frame tower (1) inwall in the grey leakage current plate of collection (7) top has set up baffling dehumidification plate (8); The port of export of described baffling equipment for separating liquid from solid (2) is connected with dedusting water reuse pipe (9), and water pump (10) is installed on the dedusting water reuse pipe (9), and the entrance point of the port of export of dedusting water reuse pipe (9) and described shower (6) joins.
2. recirculated water dedusting recover as claimed in claim 1 is characterized in that: the bottom of described main frame tower (1) is taper.
3. recirculated water dedusting recover as claimed in claim 1, it is characterized in that: be fixed with baffling lower plate (12) on the bottom panel (11) of described baffling equipment for separating liquid from solid (2), on the top panel (13) of baffling equipment for separating liquid from solid (2), be fixed with baffling upper plate (14), and baffling lower plate (12) and baffling upper plate (14) are and shift to install; Have one section flowing water space between the top ends of baffling lower plate (12) and the top panel (13), have one section flowing water space between the bottom of baffling upper plate (14) and the bottom panel (11); During work, dust-laden sewage baffling equipment for separating liquid from solid (2) is walked snakelike and is slowed down and finish gravitational settling rapidly.
4. recirculated water dedusting recover as claimed in claim 3 is characterized in that: described baffling lower plate (12) is set in parallel with baffling upper plate (14).
5. recirculated water dedusting recover as claimed in claim 3 is characterized in that: offer slag-drip opening (15) on the bottom panel (11) of baffling equipment for separating liquid from solid (2).
6. recirculated water dedusting recover as claimed in claim 3 is characterized in that: offer overfall (16) on baffling equipment for separating liquid from solid (2) sidewall of described baffling lower plate (12) top ends top position.
7. recirculated water dedusting recover as claimed in claim 1 is characterized in that: offer baffling moisture removal holes (17) on the described baffling dehumidification plate (8), the axis of the axis of baffling moisture removal holes (17) and main frame tower (1) is antarafacial and intersects setting.
8. recirculated water dedusting recover as claimed in claim 1 is characterized in that: pH value optical viewer (18) is installed on dedusting water reuse pipe (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205807014U CN201832523U (en) | 2010-10-28 | 2010-10-28 | Circulating water dedusting recoverer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205807014U CN201832523U (en) | 2010-10-28 | 2010-10-28 | Circulating water dedusting recoverer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201832523U true CN201832523U (en) | 2011-05-18 |
Family
ID=44002619
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205807014U Expired - Fee Related CN201832523U (en) | 2010-10-28 | 2010-10-28 | Circulating water dedusting recoverer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201832523U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101954232A (en) * | 2010-10-28 | 2011-01-26 | 无锡市前洲西塘锻压有限公司 | Circulating water dedusting recovery unit |
| CN102489091A (en) * | 2011-10-27 | 2012-06-13 | 上海多尔流体设备有限公司 | Dry type dust recovery device for amino acid such as lysine |
| CN105435566A (en) * | 2015-11-28 | 2016-03-30 | 洛阳绿仁环保设备有限公司 | Dust removing device for white carbon black production |
-
2010
- 2010-10-28 CN CN2010205807014U patent/CN201832523U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101954232A (en) * | 2010-10-28 | 2011-01-26 | 无锡市前洲西塘锻压有限公司 | Circulating water dedusting recovery unit |
| CN101954232B (en) * | 2010-10-28 | 2012-12-26 | 无锡市前洲西塘锻压有限公司 | Circulating water dedusting recovery unit |
| CN102489091A (en) * | 2011-10-27 | 2012-06-13 | 上海多尔流体设备有限公司 | Dry type dust recovery device for amino acid such as lysine |
| CN105435566A (en) * | 2015-11-28 | 2016-03-30 | 洛阳绿仁环保设备有限公司 | Dust removing device for white carbon black production |
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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: 20110518 Termination date: 20111028 |