CN208194028U - A kind of current equalizer and its smoke processing system for taking into account condensation - Google Patents
A kind of current equalizer and its smoke processing system for taking into account condensation Download PDFInfo
- Publication number
- CN208194028U CN208194028U CN201820402172.5U CN201820402172U CN208194028U CN 208194028 U CN208194028 U CN 208194028U CN 201820402172 U CN201820402172 U CN 201820402172U CN 208194028 U CN208194028 U CN 208194028U
- Authority
- CN
- China
- Prior art keywords
- water chamber
- taking
- current equalizer
- baffle
- condensation
- 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
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a kind of current equalizers and its smoke processing system for taking into account condensation, device includes multiple water chambers laid side by side, there is clearance space between adjacent water chamber, multiple baffles with outer wall with angle, the baffle interlaced arrangement positioned at same interval space are provided on each water chamber at least side outer wall.The utility model increases gas-liquid mass transfer effect by arranging that water chamber and baffle are evenly distributed with air-flow in tower；The utility model can condense flue gas using the condensate liquid filled in water chamber, and flue gas water content is greatly decreased, and eliminate the visual pollution of plume hangover.
Description
Technical field
The utility model relates to a kind of current equalizers and its smoke processing system for taking into account condensation.
Background technique
In the ultra-clean emission treatment technology of current industrial smoke, wet desulphurization humidification-type electrostatic precipitator is that a kind of science is high
The arrangement of effect.Wet-method desulfurized fume water content is high, and water utilization rate is low, and plume hangover is serious, causes vision
Pollution, and carry soluble-salt and flue dust etc..
Multi-pass crosses the diffusivity that flue gas heating improves flue gas at present, mitigates visual pollution, but system does not have water-saving energy
Power, furthermore system is unable to reach the effect for reducing soluble-salt, sulfuric acid mist, organic matter etc. and conventional flue dust.Meanwhile flue gas heats up
After be also easy to cause heat-exchanging tube bundle fouling, reduce heat exchange efficiency, influence the stability of heat-exchange system operation.
In addition, the fields such as current industrial arcola, Ferrous Metallurgy flue gas load amplitude of variation is big, cause desulfurizing tower operation steady
Qualitative difference, outlet dust concentration is high, and flue dust viscosity is big, and the wet cottrell monomer as flue dust accurate process equipment is more difficult to answer
To the flue dust of big concentration, big viscosity, leads to large area scale formation occur inside many wet cottrells, influence wet type
The operation stability of electrostatic precipitator.
Summary of the invention
The utility model to solve the above-mentioned problems, proposes a kind of current equalizer for taking into account condensation and its fume treatment system
System, the utility model can reduce humidity of flue gas, collect the moisture in flue gas, reduce soluble-salt in flue gas, sulfuric acid mist, have
The content of machine object etc. and conventional flue dust.
To achieve the goals above, the utility model adopts the following technical solution:
A kind of current equalizer for taking into account condensation has interval between adjacent water chamber including multiple water chambers laid side by side
Space is provided with multiple baffles with outer wall with angle on each water chamber at least side outer wall, positioned at same interval space
Baffle interlaced arrangement.
The utility model carries out flue gas by the coolant liquid stored in water chamber cold by utilizing water chamber and smoke contacts
But, meanwhile, flue gas is stopped using the baffle that water chamber outer wall is arranged, makes flue gas along the space curve formed between baffle
Shape movement extends the time of contact of flue gas and water chamber, and is flowed to flue gas.
Further, the shape, size, length of each water chamber, width etc. can be unanimously or inconsistent, concrete condition
Those skilled in the art can be according to the concrete condition of flue gas in using area, such as its temperature, the type containing object, content are not
It is same to be adjusted.
Further, the size of the clearance space of adjacent water chamber can unanimously can be inconsistent.
Certainly, when the clearance space of adjacent water chamber it is in the same size when, stream better effect.
It, can be by adjusting the size at interval, the density of baffle, the size of baffle or face when clearance space is inconsistent
The parameters such as long-pending and baffle angle, to realize current balance function.
Preferably, clearance space is 0.3~1m between water chamber.
Further, the water chamber includes inlet and outlet, is respectively used to flowing into and out for coolant liquid.
Further, the relative distance of the inlet and outlet is remote as far as possible.To fully ensure that the utilization rate of coolant liquid,
Go out coolant liquid under preferably enterprising coolant liquid, heat exchange can be made to obtain maximum logarithmic mean temperature difference (LMTD) in this way.
Preferably, the baffle length is the 0.5~0.8 of clearance space.
Preferably, the spacing between the baffle is 1.5~3 times of baffle length.
Preferably, the angle of the baffle and water chamber wall surface is 30 ° -90 °.
Preferably, the baffle positioned at the same side water chamber wall surface is parallel to each other.
Preferably, side of the water chamber on the outermost side only towards adjacent water chamber has baffle.
A kind of smoke processing system, including tower body are provided with the above-mentioned current equalizer for taking into account condensation in the tower body, described
Tower body lower end is provided with gas inlet, and upper end is provided with exhanst gas outlet, and flue gas is discharged after current equalizer by exhanst gas outlet.
Further, wet cottrell is additionally provided in the tower body, the wet cottrell is set to
Flow the upside of device.
Further, the tower body lower end is provided with liquid collecting portion.The discharge liquid of the collection of liquid collecting portion condensed fluid and water chamber.
Compared with prior art, the utility model has the following beneficial effects:
1, the utility model water chamber and baffle in desulfurizing tower increases gas-liquid mass transfer effect by that can be evenly distributed with air-flow；
2, the utility model can condense flue gas, flue gas water content is greatly decreased, disappear using the condensate liquid filled in water chamber
Except the visual pollution of plume hangover；
3, the utility model can effectively recycle condensate liquid by collecting tank, realize water-saving.
Detailed description of the invention
The accompanying drawings constituting a part of this application is used to provide further understanding of the present application, and the application's shows
Meaning property embodiment and its explanation are not constituted an undue limitation on the present application for explaining the application.
Fig. 1 is the system structure diagram of the utility model；
Fig. 2 is the current equalizer left view of the utility model；
Fig. 3 is the current equalizer right view of the utility model；
Wherein: 1, gas inlet, 2, tower body, wet cottrell, 4, exhanst gas outlet, 5, collecting tank, 6, right side water
Room, 7, baffle, 8, import, 9, discharge outlet, 10, left side water chamber, 11, intermediate water chamber.
Specific embodiment:
The utility model is described in further detail with embodiment with reference to the accompanying drawing.
It is noted that following detailed description is all illustrative, it is intended to provide further instruction to the application.Unless another
It indicates, all technical and scientific terms used herein has usual with the application person of an ordinary skill in the technical field
The identical meanings of understanding.
It should be noted that term used herein above is merely to describe specific embodiment, and be not intended to restricted root
According to the illustrative embodiments of the application.As used herein, unless the context clearly indicates otherwise, otherwise singular
Also it is intended to include plural form, additionally, it should be understood that, when in the present specification using term "comprising" and/or " packet
Include " when, indicate existing characteristics, step, operation, device, component and/or their combination.
In the present invention, term for example "upper", "lower", "left", "right", "front", "rear", "vertical", "horizontal",
The orientation or positional relationship of the instructions such as " side ", "bottom" is to be based on the orientation or positional relationship shown in the drawings, only to facilitate chatting
The relative for stating each component of the utility model or component structure relationship and determination, not refer in particular in the utility model either component or
Element should not be understood as limiting the present invention.
In the utility model, term such as " affixed ", " connected ", " connection " be shall be understood in a broad sense, and expression can be fixation
Connection, is also possible to be integrally connected or be detachably connected；It can be directly connected, the indirect phase of intermediary can also be passed through
Even.Related scientific research or technical staff for this field can determine as the case may be above-mentioned term in the present invention
Concrete meaning, should not be understood as limiting the present invention.
Just as mentioned in the background art, it in the current desulphurization system course of work, mostly uses to heat up by flue gas and improve
The diffusivity of flue gas mitigates visual pollution, but system does not have water-saving ability, furthermore system is unable to reach reduction solubility
The effect of salt, sulfuric acid mist, organic matter etc. and conventional flue dust.Meanwhile being also easy to cause heat-exchanging tube bundle fouling after flue gas heating, it reduces
Heat exchange efficiency influences the stability of heat-exchange system operation.
The utility model to solve the above-mentioned problems, proposes a kind of current equalizer for taking into account condensation, can be effectively to flue gas
It is shunted and is cooled down, reduce humidity of flue gas, collect the moisture in flue gas, reduce soluble-salt in flue gas, sulfuric acid mist, organic
The content of object etc. and conventional flue dust.
As a kind of exemplary embodiments, as described in Figure 2, a kind of current equalizer for taking into account condensation, mainly by left side water chamber 10,
Right side water chamber 6, baffle 7,9 composition of intermediate water chamber 11, import 8 and outlet.
Certainly, in the present embodiment, water chamber is to collect or accommodate condensate liquid chamber.And water chamber is mentioned, it is to include but is not limited to
The Uniform Name of whole water chambers including left side water chamber 10, right side water chamber 6 and intermediate water chamber 11.Meanwhile left side water chamber 10, right side
Water chamber 6 and intermediate water chamber 11 are only to facilitate a kind of expression method of statement in conjunction with attached drawing, are not limited in other embodiments,
Water chamber from left to right can only successively be laid in the horizontal plane.
Meanwhile intermediate water chamber 11 is only expressed as the water chamber at interlude, non-edge, not representing it is one
A water chamber includes that centre has the case where multiple water chambers.
Likewise, baffle 7 is also only the general designation of all baffles, it is not limited to the individual of several baffles of mark.
Left side water chamber 10, intermediate water chamber 11, right side water chamber 6 are successively laid, and left side water chamber 10 and the unilateral side of right side water chamber 6
It is provided with baffle 7 on wall, is both provided with baffle 7 on the two sides side wall of intermediate water chamber 11.
As shown in Fig. 2, and baffle 7 be it is multiple, as the baffle than more preferably mode, positioned at the same side of same water chamber
In array distribution.
As shown in figure 3, as another kind than more preferably mode, the baffle positioned at the same side of same water chamber is mutually flat
Row.
Water chamber import 8 and outlet 9 are arranged on water chamber maximum distance, to fully ensure that the benefit of coolant liquid (such as cooling water)
With rate, preferably above goes out liquid under feed liquor, heat exchange can be made to obtain maximum logarithmic mean temperature difference (LMTD) in this way.
Baffle 7 is welded in water chamber outside wall surface, spacing distance about 0.3~1m between water chamber, and baffle length is about between water chamber
Away from 0.5~0.8, wall surface overhead gage is spaced about 1.5~3 times of baffle length, the baffle at left and right sides of water chamber same interval
Baffle is arranged in interlaced arrangement, left water chamber 10 and right water chamber 6, side, close to one 0.1~0.2m of lateral extent wall surface of tower body wall surface.
As shown in Figure 1, current equalizer is set to tower body 2 using the smoke processing system for the current equalizer for taking into account condensation
3 front end of wet cottrell, from wet desulfurization system come out saturation wet flue gas from gas inlet 1 enter tower body 2, tower body
2 shape can be circle, can not limit to be rectangular.
Flue gas moves upwards, together under the action of baffle 7 along the curve that interval is laid and formed between baffle 7
When flue gas contacted with water chamber, in water chamber cold water from import 8 enter, absorb flue gas heat after be discharged into tower from discharge outlet 9, flue gas heat
Temperature reduces after amount is absorbed by water chamber water, and the saturation water capacity of flue gas reduces, and the water that flue gas carries is lower, temperature-fall period condensation
Under condensed water and water chamber outfall drain enter collecting tank 5, the flue gas after cooling, into wet cottrell, through depth together
After spending dedusting, tower body is discharged by exhanst gas outlet 4.
The feed liquor of water chamber can be gone out using the condensed water collected through the collecting tank 5 of supercooling and purified treatment with cooling water chamber
Liquid.It being capable of the maximum environment-friendly water-saving realized, recycling resource.
It above are only preferred embodiment, be not intended to limit this application, for those skilled in the art, this
Application can have various modifications and variations.Within the spirit and principles of this application, made any modification, equivalent replacement,
Improve etc., it should be included within the scope of protection of this application.
It is above-mentioned although specific embodiments of the present invention are described with reference to the accompanying drawings, but it is not practical new to this
The limitation of type protection scope, those skilled in the art should understand that, based on the technical solution of the present invention, ability
Field technique personnel do not need to make the creative labor the various modifications or changes that can be made still in the protection model of the utility model
Within enclosing.
Claims (10)
1. a kind of current equalizer for taking into account condensation has between adjacent water chamber it is characterized in that: including multiple water chambers laid side by side
There is clearance space, multiple baffles with outer wall with angle are provided on each water chamber at least side outer wall, are located at same interval
The baffle interlaced arrangement in space.
2. a kind of current equalizer for taking into account condensation as described in claim 1, it is characterized in that: clearance space is between water chamber
0.3~1m.
3. a kind of current equalizer for taking into account condensation as described in claim 1, it is characterized in that: the water chamber includes import and goes out
Mouthful；
The relative distance of the inlet and outlet is remote as far as possible.
4. a kind of current equalizer for taking into account condensation as described in claim 1, it is characterized in that: the baffle length is clearance space
0.5~0.8.
5. a kind of current equalizer for taking into account condensation as described in claim 1, it is characterized in that: the spacing between the baffle is gear
1.5~3 times of plate length.
6. a kind of current equalizer for taking into account condensation as described in claim 1, it is characterized in that: the folder of the baffle and water chamber wall surface
Angle is 30 ° -90 °.
7. a kind of current equalizer for taking into account condensation as described in claim 1, it is characterized in that: being located at the gear of the same side water chamber wall surface
Plate is parallel to each other.
8. a kind of smoke processing system, it is characterized in that: including tower body, setting is any just like in claim 1-7 in the tower body
The current equalizer for taking into account condensation described in, the tower body lower end are provided with gas inlet, and upper end is provided with exhanst gas outlet, flue gas
It is discharged after current equalizer by exhanst gas outlet.
9. a kind of smoke processing system as claimed in claim 8, is removed it is characterized in that: being additionally provided with wet electrostatic in the tower body
Dirt device, the wet cottrell are set to the upside of current equalizer.
10. a kind of smoke processing system as claimed in claim 8, it is characterized in that: the tower body lower end is provided with liquid collecting portion.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820402172.5U CN208194028U (en) | 2018-03-23 | 2018-03-23 | A kind of current equalizer and its smoke processing system for taking into account condensation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820402172.5U CN208194028U (en) | 2018-03-23 | 2018-03-23 | A kind of current equalizer and its smoke processing system for taking into account condensation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208194028U true CN208194028U (en) | 2018-12-07 |
Family
ID=64528652
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820402172.5U Active CN208194028U (en) | 2018-03-23 | 2018-03-23 | A kind of current equalizer and its smoke processing system for taking into account condensation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208194028U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110006264A (en) * | 2019-05-06 | 2019-07-12 | 广西玉柴机器股份有限公司 | A kind of smoke treatment method and device |
| CN111482042A (en) * | 2019-03-14 | 2020-08-04 | 深圳市金迈能科技有限公司 | Exhaust gas diffusion member and corresponding exhaust gas treatment system |
-
2018
- 2018-03-23 CN CN201820402172.5U patent/CN208194028U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111482042A (en) * | 2019-03-14 | 2020-08-04 | 深圳市金迈能科技有限公司 | Exhaust gas diffusion member and corresponding exhaust gas treatment system |
| CN111482042B (en) * | 2019-03-14 | 2022-03-25 | 深圳市金迈能科技有限公司 | Exhaust gas diffusion member and corresponding exhaust gas treatment system |
| CN110006264A (en) * | 2019-05-06 | 2019-07-12 | 广西玉柴机器股份有限公司 | A kind of smoke treatment method and device |
| CN110006264B (en) * | 2019-05-06 | 2024-02-09 | 广西玉柴机器股份有限公司 | Smoke dust treatment method and device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107042048B (en) | Gravity heat pipe type demisting method and demisting device | |
| CN108426264B (en) | Device for removing colored smoke plume through synergistic dedusting of recovered smoke waste heat | |
| CN205850576U (en) | A kind of flue gas desulfurization process system | |
| CN208194028U (en) | A kind of current equalizer and its smoke processing system for taking into account condensation | |
| CN109395882B (en) | Dust removal heat transfer white equipment and system that disappears | |
| CN205182478U (en) | Device of flue gas super -heated rate behind improvement wet flue gas desulfurization | |
| CN105890147B (en) | A kind of gas-liquid full-heat-exchange equipment of the built-in Cooling and Heat Source based on metallic fiber filler | |
| CN110652807A (en) | Non-uniform film falling pipe, unit and device applied to falling film dust removal | |
| CN105688582A (en) | Condensation wet type electric compound flue gas purification process | |
| CN110174020A (en) | A kind of heat exchanger of unsymmetrical arrangement | |
| CN109099451A (en) | A kind of flue gas energy-saving and emission-reduction disappear Bai Wuchong heat-exchange system | |
| CN110186307A (en) | A kind of demisting, cooling integration heat exchanger tube and its device and application | |
| CN104501466B (en) | A kind of earth source heat pump heating power actified solution dehumidifying unit | |
| CN211635861U (en) | Gas collecting device with baffle | |
| CN205667761U (en) | A kind of flue gas waste heat recovery apparatus | |
| CN208032200U (en) | Direct-cooled condensate and wet electrical integrated dedusting demister and system | |
| CN205613223U (en) | Congeal wetting and reply gas cleaning system of closing by cable | |
| CN208475360U (en) | The device of coloured plume is eliminated in a kind of Mist heat recovering collaboration dedusting | |
| CN204193536U (en) | A kind of high-efficiency multi-section preheating plate-type evaporator | |
| CN203672200U (en) | Rapid cooler for high temperature flue gas | |
| CN209020165U (en) | A kind of flue gas depth takes off white minimum discharge device | |
| CN211069540U (en) | Flue gas condenser of giant heat exchange module | |
| CN209214422U (en) | A kind of condensing heat exchanger for high water capacity exhaust-gas treatment | |
| CN110332559A (en) | Flue gas heat-exchange unit | |
| CN110986630A (en) | Oblique air cooling tube bundle countercurrent flow moving water film arrangement system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 250014 5th Floor, Swan Building, 157 Lishan Road, Lixia District, Jinan City, Shandong Province Patentee after: Guoneng (Shandong) energy environment Co.,Ltd. Address before: 250014, Ji'nan City, Lixia District, Lixia District, Lishan Road, No. 173, Lishan County, B, South four blocks, Shandong Patentee before: SHANDONG SHENHUA SHANDA ENERGY ENVIRONMENTAL Co.,Ltd. |