CN207877299U - A kind of flue gas desulfurization waste-water evaporation and concentration processing unit - Google Patents
A kind of flue gas desulfurization waste-water evaporation and concentration processing unit Download PDFInfo
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- CN207877299U CN207877299U CN201820156984.6U CN201820156984U CN207877299U CN 207877299 U CN207877299 U CN 207877299U CN 201820156984 U CN201820156984 U CN 201820156984U CN 207877299 U CN207877299 U CN 207877299U
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- box body
- flue gas
- uniformly distributed
- tower body
- welded
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Abstract
The utility model is related to environmental technology fields, especially a kind of flue gas desulfurization waste-water is concentrated by evaporation processing unit, including tower body, gas outlet is welded at the top of tower body, the bottom of tower body is welded with leakage fluid dram, top inside tower body is welded with the first uniformly distributed box body, bottom end inside tower body is welded with the second uniformly distributed box body, it is equipped with packing layer successively from top to bottom in tower body and between the first uniformly distributed box body and the second uniformly distributed box body, fluid reservoir, box body and enriched chamber is isolated, if being isolated on box body through equipped with dry flue gas siphunculus, one end of flue gas siphunculus is connected with packing layer, the one end of flue gas siphunculus far from packing layer is connected with the second uniformly distributed box body, fluid reservoir is equipped with infusion device with being isolated between box body, the top side of enriched chamber is equipped with leakage port, the bottom of enriched chamber is equipped with heating plant.The utility model effectively increases evaporation efficiency, reduces tower body volume, improves economy.
Description
Technical field
The utility model is related to environmental technology fields, in particular to a kind of processing of flue gas desulfurization waste-water evaporation and concentration
Device.
Background technology
With being constantly progressive for society, industrialized aggravation brings serious pollution to environment, environmental pollution in order to prevent, often
It often needs to handle industrial smoke, in the desulfurization wastewater for flue gas obtain after desulfurization process, it usually needs steamed
Hair concentration is evaporated desulfurization wastewater using the waste heat of boiler smoke the heat smoke evaporation technique of concentration so as to subsequent processes,
It is a kind of current common technical solution, which is that evaporation efficiency is low, and void tower volume is big, less economical.
Utility model content
Purpose of the utility model is to solve the disadvantage that evaporation efficiency is low, less economical exists in the prior art, and
A kind of flue gas desulfurization waste-water proposed is concentrated by evaporation processing unit.
To achieve the goals above, the utility model uses following technical solution：
A kind of flue gas desulfurization waste-water evaporation and concentration processing unit, including tower body, the top center welding of the tower body
There are gas outlet, the bottom centre position of the tower body to be welded with leakage fluid dram, valve is connected on the leakage fluid dram, the tower body
Bottom is welded with supporting rack, and the top inside the tower body is welded with the first uniformly distributed box body, the side of the described first uniformly distributed box body
It is connected with inlet tube, the inlet tube extends to the outside of the tower body, leads to through equipped with multiple on the described first uniformly distributed box body
Tracheae, is welded with multiple spray heads on the bottom surface of the described first uniformly distributed box body, the spray head and the described first uniformly distributed box body phase
Connection, the bottom end inside the tower body are welded with the second uniformly distributed box body, the side of the described second uniformly distributed box body be welded with flue gas into
Mouthful, the gas inlet extends to the outside of the tower body, runs through on the described second uniformly distributed box body and is equipped with multiple fluid-through tubes, described
It is equipped with packing layer, liquid storage successively from top to bottom in tower body and between the described first uniformly distributed box body and the second uniformly distributed box body
Room, isolation box body and enriched chamber, if through dry flue gas siphunculus is equipped on the isolation box body, several flue gas siphunculus are described in
The internal circumferential of tower body is uniformly arranged, and the flue gas siphunculus is welded to each other with the top surface that box body is isolated, the flue gas siphunculus
It is isolated between the bottom surface of box body equipped with liquid-leadage hole with described, one end of the flue gas siphunculus is connected with described filler layer, described
The one end of flue gas siphunculus far from described filler layer is connected with the described second uniformly distributed box body, and box body is isolated with described in the fluid reservoir
Between be equipped with infusion device, the infusion device is located at the outside of the tower body, and the top side of the enriched chamber is equipped with discouraged
Mouthful, the bottom of the enriched chamber is equipped with heating plant.
It is further preferred that the utility model proposes a kind of flue gas desulfurization waste-water be concentrated by evaporation processing unit, wherein institute
It includes liquid outlet to state infusion device, and the liquid outlet is opened in the side of the fluid reservoir, and infusion is equipped on the liquid outlet
The output end of pump, the infusion pump is connected with woven hose, the one end of the woven hose far from the infusion pump and the barrier box
Body is connected.
It is further preferred that the utility model proposes a kind of flue gas desulfurization waste-water be concentrated by evaporation processing unit, wherein institute
It includes several heat supply endless tubes and heat supply supervisor to state heating plant, and several heat supply endless tubes are evenly spaced in the interior of the tower body
Portion, the heat supply endless tube are welded on the flue gas siphunculus, and the bottom of the heat supply endless tube is circumferentially uniformly provided with heat supply mouth, if
It does the heat supply endless tube to be connected with heat supply supervisor, the heat supply supervisor extends to outside the tower body and is connected with confession
Hot equipment.
It is further preferred that the utility model proposes a kind of flue gas desulfurization waste-water be concentrated by evaporation processing unit, wherein institute
It states flue gas siphunculus and is located on the pipeline section of the enriched chamber that uniform welding has heat-conducting block, the bottom of the heat-conducting block along its length
For pyramidal structure, the heat-conducting block is circumferentially uniformly provided with multiple liquid-leaking nozzles.
It is further preferred that the utility model proposes a kind of flue gas desulfurization waste-water be concentrated by evaporation processing unit, wherein institute
It is structured packing structure to state packing layer.
Compared with prior art, the utility model is used for the evaporation and concentration processing unit of flue gas desulfurization waste-water, beneficial to effect
Fruit is：The utility model is evaporated concentration by flue to desulfurization wastewater, and flue is equipped with thermally conductive sheet, effectively
Disengagement area is increased, additional evaporation calorific requirement is provided for desulfurization wastewater concentration by heating plant, effectively increases evaporation
Efficiency reduces tower body volume, improves economy.
Description of the drawings
Fig. 1 be the utility model proposes a kind of flue gas desulfurization waste-water be concentrated by evaporation processing unit structural schematic diagram；
Fig. 2 is schematic cross-sectional view at the B-B of the utility model Fig. 1；
Fig. 3 is enlarged structure schematic diagram at the A1 of the utility model Fig. 1；
Fig. 4 is enlarged structure schematic diagram at the A2 of the utility model Fig. 1.
In figure：Tower body 1, gas outlet 11, leakage fluid dram 12, valve 121, supporting rack 13, first be evenly distributed with box body 2, spray head 21,
Snorkel 22, inlet tube 23, packing layer 3, fluid reservoir 4, liquid outlet 41, infusion pump 42, woven hose 43, isolation box body 5, liquid-leadage hole
51, it second is evenly distributed with box body 6, gas inlet 61, fluid-through tube 62, flue gas siphunculus 7, heat-conducting block 71, liquid-leaking nozzle 701, enriched chamber 8, lets out
Gas port 81, heat supply endless tube 82, heat supply supervisor 83, heat supply mouth 801.
Specific implementation mode
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.
Referring to Fig.1, Fig. 2, Fig. 3, Fig. 4, a kind of flue gas desulfurization waste-water evaporation and concentration processing unit, which includes tower body 1,
The top center of tower body 1 is welded with gas outlet 11, and the bottom centre position of tower body 1 is welded with leakage fluid dram 12, leakage fluid dram 12
On be connected with valve 121, the bottom of tower body 1 is welded with supporting rack 13, and gas outlet 11 is used for the discharge of purification gas, leakage fluid dram 12
Discharge for desulfurization waste liquor concentrate.
Top inside tower body 1 is welded with the first uniformly distributed box body 2, and the side of the first uniformly distributed box body 2 is connected with inlet tube 23,
Inlet tube 23 extends to the outside of tower body 1, runs through on the first uniformly distributed box body 2 and is equipped with multiple snorkels 22, snorkel 22 is for arranging
Go out purification gas, multiple spray heads 21, spray head 21 and the first 2 phase of uniformly distributed box body are welded on the bottom surface of the first uniformly distributed box body 2
Connection, the first uniformly distributed box body 2 uniformly spray out absorbing liquid by spray head 21, and absorbing liquid is used to carry out desulfurization to flue gas.
Bottom end inside tower body 1 is welded with the second uniformly distributed box body 6, and the side of the second uniformly distributed box body 6 is welded with gas inlet
61, gas inlet 61 extends to the outside of tower body 1, runs through on the second uniformly distributed box body 6 and is equipped with multiple fluid-through tubes 62, fluid-through tube 62 is used
Desulfurization waste liquor after discharge concentrates, the second uniformly distributed box body 6 is for flue gas to be evenly distributed with.
In tower body 1 and positioned at the first uniformly distributed box body 2 and second be evenly distributed between box body 6 from top to bottom successively equipped with packing layer 3,
Fluid reservoir 4, isolation box body 5 and enriched chamber 8, if through dry flue gas siphunculus 7 is equipped on isolation box body 5, if dry flue gas siphunculus 7 is along tower
The internal circumferential of body 1 is uniformly arranged, and flue gas siphunculus 7 is welded to each other with the top surface that box body 5 is isolated, flue gas siphunculus 7 with box body 5 is isolated
Bottom surface between be equipped with liquid-leadage hole 51, one end of flue gas siphunculus 7 is connected with packing layer 3, and flue gas siphunculus 7 is far from packing layer 3
One end is connected with the second uniformly distributed box body 6, and flue gas siphunculus 7 is located on the pipeline section of enriched chamber 8 that uniform welding has along its length
The bottom of heat-conducting block 71, heat-conducting block 71 is pyramidal structure, and heat-conducting block 71 is circumferentially uniformly provided with multiple liquid-leaking nozzles 701, packing layer 3
For structured packing structure, packing layer 3 is handled for flue gas desulfurization, and fluid reservoir 4 is used for for storing desulfurization waste liquor, isolation box body 5
Desulfurization waste liquor is evenly distributed on flue gas siphunculus 7, desulfurization waste liquor passes through flue gas siphunculus 7 and the sepage be isolated between the bottom surface of box body 5
Hole 51 flows downward along flue gas siphunculus 7, and the smoke pre-heating pair flowed through in flue gas siphunculus 7 is utilized in desulfurization waste liquor flow process
Desulfurization waste liquor is evaporated, and is increased effectively disengagement area by heat-conducting block 71, is improved the evaporation efficiency of desulfurization waste liquor.
Fluid reservoir 4 is equipped with infusion device with being isolated between box body 5, and infusion device is located at the outside of tower body 1, infusion device packet
Include liquid outlet 41, liquid outlet 41 is opened in the side of fluid reservoir 4, is equipped with infusion pump 42 on liquid outlet 41, infusion pump 42 it is defeated
Outlet is connected with woven hose 43, and the one end of woven hose 43 far from infusion pump 42 is connected with box body 5 is isolated, and infusion device is used for will
Desulfurization waste liquor in fluid reservoir 4 is sent in isolation box body 5.
The top side of enriched chamber 8 is equipped with leakage port 81, and the bottom of enriched chamber 8 is equipped with heating plant, and heating plant includes
Several heat supply endless tubes 82 and heat supply supervisor 83, several heat supply endless tubes 82 are evenly spaced in the inside of tower body 1, and heat supply endless tube 82 welds
On flue gas siphunculus 7, the bottom of heat supply endless tube 82 is circumferentially uniformly provided with heat supply mouth 801, and several heat supply endless tubes 82 are and heat supply
Supervisor 83 is connected, and heat supply supervisor 83 extends to 1 outside of tower body and is connected with heating equipment, and heating plant passes through heat supply endless tube 82
Evaporating temperature is improved for enriched chamber 8, provides additional evaporation calorific requirement for desulfurization wastewater concentration, the evaporation of this flue gas desulfurization waste-water is dense
Contracting processing unit effectively increases evaporation efficiency, reduces tower body volume, improves economy.
The preferable specific implementation mode of the above, only the utility model, but the scope of protection of the utility model is not
Be confined to this, any one skilled in the art within the technical scope disclosed by the utility model, according to this practicality
Novel technical solution and its utility model design are subject to equivalent substitution or change, should all cover the protection model in the utility model
Within enclosing.
Claims (5)
1. a kind of flue gas desulfurization waste-water is concentrated by evaporation processing unit, including tower body (1), the top center of the tower body (1)
It is welded with gas outlet (11), the bottom centre position of the tower body (1) is welded with leakage fluid dram (12), connects on the leakage fluid dram (12)
It is connected to valve (121), the bottom of the tower body (1) is welded with supporting rack (13), which is characterized in that tower body (1) inside
Top is welded with the first uniformly distributed box body (2), and the side of the described first uniformly distributed box body (2) is connected with inlet tube (23), the feed liquor
Pipe (23) extends to the outside of the tower body (1), runs through on the described first uniformly distributed box body (2) and is equipped with multiple snorkels (22), institute
It states and is welded with multiple spray heads (21) on the bottom surface of the first uniformly distributed box body (2), the spray head (21) and the described first uniformly distributed box
Body (2) is connected, and the internal bottom end of the tower body (1) is welded with the second uniformly distributed box body (6), the described second uniformly distributed box body (6)
Side is welded with gas inlet (61), and the gas inlet (61) extends to the outside of the tower body (1), the described second uniformly distributed box
Through being equipped with multiple fluid-through tubes (62) on body (6), in the tower body (1) and positioned at the described first uniformly distributed box body (2) and described the
It is equipped with packing layer (3), fluid reservoir (4), isolation box body (5) and enriched chamber (8) successively from top to bottom between two uniformly distributed box bodys (6),
The isolation box body (5) if on through be equipped with dry flue gas siphunculus (7), several flue gas siphunculus (7) are along the interior of the tower body (1)
Portion circumferential uniformly arrangement, the flue gas siphunculus (7) are welded to each other with the top surface that box body (5) is isolated, the flue gas siphunculus (7)
It is isolated between the bottom surface of box body (5) equipped with liquid-leadage hole (51), one end of the flue gas siphunculus (7) and described filler layer with described
(3) it is connected, the one end of the flue gas siphunculus (7) far from described filler layer (3) is connected with the described second uniformly distributed box body (6),
The fluid reservoir (4) with it is described be isolated between box body (5) be equipped with infusion device, the infusion device is located at the tower body (1)
The top side of outside, the enriched chamber (8) is equipped with leakage port (81), and the bottom of the enriched chamber (8) is equipped with heating plant.
2. a kind of flue gas desulfurization waste-water according to claim 1 is concentrated by evaporation processing unit, which is characterized in that the infusion
Device includes liquid outlet (41), and the liquid outlet (41) is opened in the side of the fluid reservoir (4), pacifies on the liquid outlet (41)
Equipped with infusion pump (42), the output end of the infusion pump (42) is connected with woven hose (43), and the woven hose (43) is far from described
One end of infusion pump (42) is connected with the box body (5) of being isolated.
3. a kind of flue gas desulfurization waste-water according to claim 1 is concentrated by evaporation processing unit, which is characterized in that the heat supply
Device includes several heat supply endless tubes (82) and heat supply supervisor (83), and several heat supply endless tubes (82) are evenly spaced in the tower body
(1) inside, the heat supply endless tube (82) are welded on the flue gas siphunculus (7), and the bottom of the heat supply endless tube (82) is along week
To heat supply mouth (801) is uniformly provided with, several heat supply endless tubes (82) are connected with heat supply supervisor (83), the heat supply
Supervisor (83) extends to the tower body (1) outside and is connected with heating equipment.
4. a kind of flue gas desulfurization waste-water according to claim 1 is concentrated by evaporation processing unit, which is characterized in that the flue gas
Siphunculus (7) is located on the pipeline section of the enriched chamber (8) that uniform welding has heat-conducting block (71), the heat-conducting block along its length
(71) bottom is pyramidal structure, and the heat-conducting block (71) is circumferentially uniformly provided with multiple liquid-leaking nozzles (701).
5. a kind of flue gas desulfurization waste-water according to claim 1 is concentrated by evaporation processing unit, which is characterized in that the filler
Layer (3) is structured packing structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820156984.6U CN207877299U (en) | 2018-01-30 | 2018-01-30 | A kind of flue gas desulfurization waste-water evaporation and concentration processing unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820156984.6U CN207877299U (en) | 2018-01-30 | 2018-01-30 | A kind of flue gas desulfurization waste-water evaporation and concentration processing unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207877299U true CN207877299U (en) | 2018-09-18 |
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ID=63509736
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820156984.6U Expired - Fee Related CN207877299U (en) | 2018-01-30 | 2018-01-30 | A kind of flue gas desulfurization waste-water evaporation and concentration processing unit |
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| Country | Link |
|---|---|
| CN (1) | CN207877299U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112551627A (en) * | 2020-11-26 | 2021-03-26 | 武汉天空蓝环保科技有限公司 | Desulfurization waste water enrichment facility and zero discharge system |
-
2018
- 2018-01-30 CN CN201820156984.6U patent/CN207877299U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112551627A (en) * | 2020-11-26 | 2021-03-26 | 武汉天空蓝环保科技有限公司 | Desulfurization waste water enrichment facility and zero discharge system |
| CN112551627B (en) * | 2020-11-26 | 2022-01-18 | 武汉天空蓝环保科技有限公司 | Desulfurization waste water enrichment facility and zero discharge system |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180918 Termination date: 20200130 |