CN110028121A - Desulfurization wastewater treatment system - Google Patents
Desulfurization wastewater treatment system Download PDFInfo
- Publication number
- CN110028121A CN110028121A CN201910390843.XA CN201910390843A CN110028121A CN 110028121 A CN110028121 A CN 110028121A CN 201910390843 A CN201910390843 A CN 201910390843A CN 110028121 A CN110028121 A CN 110028121A
- Authority
- CN
- China
- Prior art keywords
- vaporization chamber
- desulfurization wastewater
- salt
- room
- wastewater treatment
- 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.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/042—Prevention of deposits
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/043—Details
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/048—Purification of waste water by evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/06—Flash evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/18—Nature of the water, waste water, sewage or sludge to be treated from the purification of gaseous effluents
Abstract
The invention discloses a kind of desulfurization wastewater treatment systems, and including waste water source, hyperbaric heating room and the vaporization chamber being connected to by waste water delivery pipe, the vaporization chamber top is equipped with gas outlet, bottom end is provided with salt leg, and salt leg bottom is connected with salt slurry delivery pipe and inlet tube.Hyperbaric heating room in the application and it is provided with biggish pressure difference between vaporization chamber, so that desulfurization wastewater rapid pressure drop, evaporation rate after entering vaporization chamber significantly improve, realizes flash distillation；The effects of salt leg is arranged in crystalliser feet, and salt leg plays collection salt, classification, washing, back dissolving soluble impurity, conveying can be improved the quality of salt, reduce system energy consumption；Using circulating pump, make desulfurization wastewater and the crystal salt high-speed circulating between heater and crystallizer, wash away heater tube wall, reduces fouling.
Description
Technical field
The present invention relates to desulfurization wastewater processing technology fields, and in particular to desulfurization wastewater treatment system.
Background technique
Containing sour gas such as a large amount of sulfur dioxide in flue gas, to the seriously polluted of environment, so being put in flue gas
Unprecedentedly, it is necessary to pass through desulfurization process, however desulfurization can generate a large amount of waste water, therefore how desulfurization wastewater handles and can reduce
Pollution to environment is also a very important project.
Summary of the invention
The purpose of the present invention is to provide a kind of desulfurization wastewater treatment system, solve existing desulfurization wastewater amount it is big, to environment
Seriously polluted problem.
In order to solve the above technical problems, the invention adopts the following technical scheme:
A kind of desulfurization wastewater treatment system, it is described including waste water source, hyperbaric heating room and the vaporization chamber being connected to by waste water delivery pipe
Vaporization chamber top is equipped with gas outlet, bottom end is provided with salt leg, and salt leg bottom is connected with salt slurry delivery pipe and inlet tube.
Preferably, desulfurization wastewater is successively softened, is concentrated, concentrated water is obtained, the concentrated water passes through waste water delivery pipe
It is connected to hyperbaric heating room；The salt leg has been sequentially communicated thickener and solid-liquid separating equipment by salt slurry delivery pipe.
Preferably, demister and the support frame for supporting demister are provided in the vaporization chamber, the demisting
Device includes granular filler and for containing the carrying packet of granular filler, and the carrying is surrounded by more than two uniform folds in support frame
On.
Preferably, support frame as described above tilts gradually downward along close to the direction of evaporation chamber interior walls.
Preferably, more than two carrying Bao Jun in a ring and are arranged concentrically, two neighboring carrying wrap between consolidate
Fixed connection and: the outer diameter of inside carrying packet and the internal diameter of outside carrying packet are adapted.
Preferably, being circumferentially provided with supporting table along vaporization chamber in the vaporization chamber, support frame as described above is located at supporting table
On, the width of the supporting table is greater than the carrying packet of largest outside diameter at a distance from evaporation chamber interior walls.
High pressure is transferred to preferably, being additionally provided in the vaporization chamber and hyperbaric heating room and will evaporate indoor liquid
The circulating water pipe of room is heated, is provided with check-valves and/or force (forcing) pump on the circulating water pipe.
Preferably, being provided with heat exchanger in the hyperbaric heating room, the heat exchanger, which includes that bending is serpentine-like, to be changed
Heat exchanger is divided into the first Heat Room and the second Heat Room by hot plate, the heat exchanger plates, and one end of first Heat Room is provided with
Water inlet, the other end are provided with the communication port being connected to the second Heat Room, and second Heat Room is set far from one end of communication port
It is equipped with discharge outlet；The water tank top surface is provided with exhaust outlet.
Preferably, baffle plate is provided in first Heat Room and the second Heat Room, described baffle plate one end
It is fixed on water tank side wall, the other end is located on the inside of the bending section of heat exchanger plates and is provided with baffling gap, institute between bending section
It states baffle plate and heat exchanger plates bending section corresponds.
Preferably, the direction that the interior lateral edge liquid flow of the heat exchanger plates bending section is moved is disposed with the first deflector
With the second deflector, liquid feeding side, the second deflector that first deflector is located at corresponding baffling gap are respectively positioned on corresponding baffling
The tapping side in gap, and second deflector close to one end of the first deflector between the first deflector and bending section.
Compared with prior art, the beneficial effects of the present invention are:
Hyperbaric heating room in the application and biggish pressure difference is provided between vaporization chamber, so that desulfurization wastewater is evaporated entering
Rapid pressure drop behind room, evaporation rate significantly improve, and realize flash distillation.
The effects of salt leg is arranged in crystalliser feet, and salt leg plays collection salt, classification, washing, back dissolving soluble impurity, conveying,
It can be improved the quality of salt, reduce system energy consumption
Using circulating pump, makes desulfurization wastewater and the crystal salt high-speed circulating between heater and crystallizer, wash away heater tube
Wall reduces fouling.
Demister is cooperated using granular filler and carrying packet in the application, so that demister is not easy to plug, even if stifled
Plug also convenience and high-efficiency, quickly demister is dredged.
Using plate heat exchanger, the problem of tubular heat exchanger is easy blocking is avoided, and plate heat exchanger facilitates use
Low-temperature-rise design, avoids waste water from generating bubble in heat exchanger；In addition, heating room uses high temperature design, drop to a greater extent
The possibility that low blistering generates avoids the excessively high caused heat exchanger localized hyperthermia of temperature rise, to avoid after generating bubbles burst
Fouling.
Detailed description of the invention
Fig. 1 is the partial structural diagram of vaporization chamber when this is not laid with demister.
Fig. 2 is a kind of top view of structure of this demister.
Fig. 3 is the A of this Fig. 2 to cross-sectional view.
Fig. 4 is the structural schematic diagram of this supporting table.
Fig. 5 is a kind of top view of structure in this hyperbaric heating room.
Fig. 6 is the partial top view of this heat exchanger plates and baffle plate another kind structure.
Fig. 7 is this hyperbaric heating cell structure schematic diagram.
Specific embodiment
In order to make the objectives, technical solutions, and advantages of the present invention clearer, below in conjunction with attached drawing 1-7 and implementation
Example, the present invention will be described in further detail.It should be appreciated that specific embodiment described herein is only used to explain this hair
It is bright, it is not intended to limit the present invention.
Present embodiments provide a kind of desulfurization wastewater treatment system, including be connected to by waste water delivery pipe waste water source, high pressure
Room 5 and vaporization chamber 1 are heated, 1 top of vaporization chamber is equipped with gas outlet, bottom end is provided with salt leg, and salt leg bottom is connected with
Salt slurry delivery pipe and inlet tube.
After desulfurization wastewater preliminary treatment, pump is transported to the evaporation and crystallization system including hyperbaric heating room 5 and vaporization chamber 1, leads to
It crosses after hyperbaric heating room 5 is heated and enters in vaporization chamber 1, wherein the pressure of hyperbaric heating room 5 is preferably 0.6-0.9MPa, and desulfurization is useless
Pressure reduces rapidly when water enters evaporation and crystallization system, so that gas accelerates evaporation.Explosive evaporation, the salt slurry generated after evaporation from
Salt foot drains into salt slurry tank.
In order to keep the pressure difference of hyperbaric heating room 5 and vaporization chamber, valve is set between, when hyperbaric heating room 5
Pressure valve opening when reaching at or above 0.9；When the pressure of hyperbaric heating room 5 is lower than 0.6, valve is closed.In addition, in height
The entrance of pressure heating room 5 also needs that check-valves is arranged, and avoids the desulfurization wastewater adverse current of high pressure.
Desulfurization wastewater in the present embodiment first can successively be softened, be concentrated, be obtained before entering hyperbaric heating room 5
To concentrated water, the concentrated water is connected to by waste water delivery pipe with hyperbaric heating room 5；The salt leg is sequentially communicated by salt slurry delivery pipe
There are thickener and solid-liquid separating equipment.
Desulfurization wastewater can be introduced into wastewater collection pond before entering hyperbaric heating room 5 and be collected and homogenization,
In view of the fluctuation of desulfurization waste water quality water, wastewater collection pond can be with design air blender, and waste water is through being sufficiently stirred in pond
After homogeneous, lime is added, carries out preliminarily softened processing, forms the sediment of calcium sulfate, magnesium hydroxide, while magnesium hydroxide carries
Silica forms co-precipitation, and mixed liquor enters clarifying basin, and the water outlet to clarifying basin continues supplement addition sodium hydroxide, to pH value
Accurate adjustment is carried out, keeps magnesium hydrate precipitate more complete, adds sodium carbonate liquor, with the anti-shape of calcium ion remaining in clarifying basin water outlet
At precipitation of calcium carbonate, filters out after solid particle takes clear liquid to carry out micro-filtration or ultrafiltration, depth scale removal and enter film concentration systems, wherein two
Order reaction slot is respectively provided with mechanical stirring and pH value monitoring.Film concentration systems: it is main to realize that decrement treatment is concentrated in desulfurization wastewater, so that
Wastewater flow rate into subsequent flue residue heat vaporising device is down to the 40% or less of raw water.
The effects of salt leg is arranged in 1 bottom of vaporization chamber, and salt leg plays collection salt, classification, washing, back dissolving soluble impurity, conveying,
It is one of the quality for improving salt, the critical component for reducing system energy consumption.Salt leg provides speed appropriate and uniform for crystal salt
Fluidization can be eluriated efficiently, cooled down, classified and be thickened.The crystal that the salt such as NaCl are constantly crystallized out in vaporization chamber 1, because of gravity
Relationship moves downward, and gradually drops into salt leg from vaporization chamber 1, and washing lotion is entered by inlet tube from salt leg lower part, along leg wall
It rises and the removal of the impurity such as organic matter, sylvite is improved into the quality of crystal salt with crystal salt countercurrent washing.Washing lotion is inversely transported with salt slurry
Row has carried out heat exchange, reduces salt discharge temperature, reduces heat lost by brine.This technique uses gypsum seed method antiscale production technology,
By the way that calcium sulfate crystal seed is added, heater fouling can be effectively reduced.
The salt slurry generated after evaporation drains into salt slurry tank from salt foot, is delivered to after thickener is thickened to 60% -70% by brine pump
Centrifugal dehydration is carried out, centrifuge mother liquor returns to vaporization chamber 1.
It is entrained with drop when to avoid gas from being discharged or is evaporated salt, demister can be set in the vaporization chamber 1, it is described to remove
Day with fog can make it is in the prior art any one, also may include: demister and the support frame 2 for supporting demister, institute
Stating demister includes granular filler and for containing the carrying packet 3 of granular filler, and there are two the above uniform folds for the carrying packet 3
On support frame 2.
The present embodiment is in order to which while keeping the defogging effect of demister, the demister solved in existing vaporization chamber 1 is easy
Blocking occurs or occurs to block difficult cleaning of problem, is provided with the structure, in which:
The partial size of granular filler can be determining according to the throughput of fog and the component of fog, in contrast, granular filler
Partial size is smaller, defogging effect is better, but accordingly is also easier to block；The partial size of granular filler is bigger, is more not easy to plug, but demisting
Effect can be relatively weaker, so the partial size of granular filler also needs those skilled in the art to select as needed.
Carrying packet 3 in the application should select material with certain flexibility, combine durability, can select fiber
Net, thinner steel wire etc., so that carrying packet 3 is easy to happen deformation under the effect of external force: when the gap of granular filler is blocked
Plug when influencing fog effect out, carrying packet 3 can be lifted, and carrying packet 3 can deformation occurs under gravity at this time, so that
The relative position of granular filler changes, and generates friction in moving process between each other, can will block the substance in gap from
It is separated on filler particles, so that demister be made to be dredged, dredging is convenient.And when placing it on support frame 2, Ke Yitong
It crosses constantly to lift carrying packet 3 and put down, adjust the thickness of granular filler each section, convenient filling.
The support bearing packet 3 of support frame 2 in the application, as long as there is the gap on certain stability and support frame 2
Less than carrying packet 3 carrying packet 3 will not be slid from support frame 2.
For vaporization chamber 1 in the application in addition to demister, other parts can use existing design, as long as can be realized to liquid
The evaporative crystallization of phase and the work for not influencing demister in the application.
The present embodiment support frame 2 may include the support rod being arranged radially along vaporization chamber 1 and be coaxially disposed with vaporization chamber 1
Support ring, the support rod are fixedly connected with support ring, are matched with the carrying packet 3 of annular setting.
In order to minimize influence of the presence of carrying packet 3 to defogging effect and efficiency, the knot of carrying packet 3 is advanced optimized
Structure: the carrying packet 3 is in netted, and mesh is less than the partial size of granular filler.
During due to demister demisting, has droplets form or water droplet largely condenses on demister, can also make
Gap between filler is filled, and influences fog effect out, so support frame 2 uses the structure that middle part is high, surrounding is low, support frame 2
It tilts along the direction close to 1 inner wall of vaporization chamber, so that the drop of condensation is gathered in the edge of demister, then evaporates gradually downward
The inner wall of room 1 can play the role of water conservancy diversion, so that water droplet is flowed down along 1 inner wall of vaporization chamber.
When low structure, when support frame 2 tilts gradually downward along the direction close to 1 inner wall of vaporization chamber, if being only arranged one
Carrying packet 3, then the filler carried in packet 3 is likely difficult to be uniformly distributed, one side thickness meeting of the carrying packet 3 close to 1 inner wall of vaporization chamber
The one side for being relatively distant from 1 inner wall of vaporization chamber is big, so in order to minimize carrying 3 differences in height in the radial direction of packet, so that demisting
Device each section filler particles are evenly distributed, and improve defogging effect, while the number for reducing carrying packet 3 facilitates processing and installation,
The more than two carrying packets 3 of setting, more than two carrying packets 3 in a ring and are arranged concentrically, between two neighboring carrying packet 3
Be fixedly connected and: inside carrying packet 3 outer diameter and outside carrying packet 3 internal diameter be adapted.
In order to avoid gas is directly raised the effect less than demisting from the gap between 1 inner wall of vaporization chamber and atomizer,
The present embodiment can further be optimized: circumferentially be provided with supporting table 4, the branch along vaporization chamber 1 in the vaporization chamber 1
Support 2 is located in supporting table 4, and the width of the supporting table 4 is greater than the carrying packet 3 of largest outside diameter at a distance from 1 inner wall of vaporization chamber.
On the one hand the presence of supporting table 4 supports support frame 2, on the other hand block between 1 inner wall of vaporization chamber and carrying packet 3
Gap.In order to reduce or even avoid aggregation of the liquid of condensation in supporting table 4, the upper surface of supporting table 4 can be made to tilt and set
It sets, the side far from 1 inner wall of vaporization chamber is lower than close to the side of 1 inner wall of vaporization chamber, to facilitate under liquid flow.
To reduce fouling, it is also provided in the vaporization chamber 1 and hyperbaric heating room 5 and turns the liquid in vaporization chamber 1
The circulating water pipe of hyperbaric heating room 5 is moved to, check-valves and/or force (forcing) pump are provided on the circulating water pipe.Using circulating pump, make
Desulfurization wastewater and the crystal salt high-speed circulating between hyperbaric heating room 5 and vaporization chamber 1 wash away 5 tube wall of hyperbaric heating room, reduce
Fouling.
In order to improve heat exchange efficiency, heat exchanger can be set in hyperbaric heating room 5, the heat exchanger includes that bending is in snake
Heat exchanger is divided into the first Heat Room 51 and the second Heat Room 52, first Heat Room by the heat exchanger plates 6 of shape, the heat exchanger plates 6
51 one end is provided with water inlet 54, the other end is provided with the communication port 53 being connected to the second Heat Room 52, second heat exchange
Room 52 is provided with the discharge outlet 55 being connected to vaporization chamber 1 far from one end of communication port 53；5 top surface of hyperbaric heating room is provided with
Exhaust outlet 56.
Waste water to be processed is entered from water inlet 54, successively passes through the first Heat Room 51, communication port 53, the second Heat Room
52 leave from discharge outlet 55.During waste water stops in hyperbaric heating room 5, heat exchanger and wastewater room will do it heat exchange,
Enter vaporization chamber 1 after heating to waste water.Exhaust outlet 56 can prevent the pressure in hyperbaric heating room 5 excessive, generate safety
Hidden danger.
To improve the efficiency that the time of contact of waste water and heat exchanger plates 6 improves heat exchange, first Heat Room 51 and second
Baffle plate 7 is provided in Heat Room 52, described 7 one end of baffle plate is fixed on 5 side wall of hyperbaric heating room, and the other end, which is located at, to be changed
It is provided with baffling gap on the inside of the bending section of hot plate 6 and between bending section, the baffle plate 7 and 6 bending section of heat exchanger plates are one by one
It is corresponding.
Hot plate be designed to it is snakelike after, the inside waste water flow rate of 6 bending section of heat exchanger plates can reduce, influence heat exchange efficiency,
So setting baffle plate 7, so that waste water has to pass through baffling gap and could continue flow forward, by the width for designing baffling gap
Spend the waste water flow velocity on the inside of adjustable 6 bending section of heat exchanger plates.In addition, the design of baffle plate 7 is so that in same waste water flow velocity
In the case of, waste water residence time in hyperbaric heating room 5 is increased, the time of heat exchange is improved, to improve heat exchange efficiency.
The dynamic direction of the interior lateral edge liquid flow of the bending section of heat exchanger plates 6 described in the present embodiment is disposed with the first deflector
8 and second deflector 9, liquid feeding side, the second deflector 9 that first deflector 8 is located at corresponding baffling gap be respectively positioned on correspondence
The tapping side in baffling gap, and second deflector 9 is located at the first deflector 8 and bending close to one end of the first deflector 8
Between portion.
It needs to turn nearly to adapt to the bending of heat exchanger plates 6, since the inertia of waste water is when waste water passes through baffling gap
Flow forward changes its direction so waste water needs heat exchanger plates 6 to provide enough active forces for it when turning, hits for a long time
The meeting of hitting on the inside of deflector bending section so that be easily damaged, so the first deflector 8 of setting and the second deflector 9, the two can edges
The direction setting of waste water flowing, first deflector 8 and the second deflector 9 between baffle plate 7 and bending section and not with
The two contact, so that waste water is divided into two parts when passing through the first deflector 8, so that the impact force of waste water exchange hot plate 6 has
Half is blocked by the first deflector 8；Since the second deflector 9 is located at the first deflector 8 and curved close to one end of the first deflector 8
Between pars convoluta, so that the second deflector 9 further helps the impact force of the receiving waste water of heat exchanger plates 6, so that heat exchanger plates 6
Loss reduces, and the service life extends.
Although reference be made herein to invention has been described for multiple explanatory embodiments of the invention, however, it is to be understood that
Those skilled in the art can be designed that a lot of other modification and implementations, these modifications and implementations will fall in this Shen
It please be within disclosed scope and spirit.More specifically, disclose in the application, drawings and claims in the range of, can
With the building block and/or a variety of variations and modifications of layout progress to theme combination layout.In addition to building block and/or layout
Outside the modification and improvement of progress, to those skilled in the art, other purposes also be will be apparent.
Claims (10)
1. a kind of desulfurization wastewater treatment system, it is characterised in that: including be connected to by waste water delivery pipe waste water source, hyperbaric heating room
(5) and vaporization chamber (1), vaporization chamber (1) top are provided with salt leg equipped with gas outlet, bottom end, and salt leg bottom is connected with
Salt slurry delivery pipe and inlet tube.
2. desulfurization wastewater treatment system according to claim 1, which is characterized in that desulfurization wastewater is successively softened, is dense
Contracting, obtains concentrated water, and the concentrated water is connected to by waste water delivery pipe with hyperbaric heating room (5)；The salt leg passes through salt slurry delivery pipe
It has been sequentially communicated thickener and solid-liquid separating equipment.
3. desulfurization wastewater treatment system according to claim 1, which is characterized in that be provided with and remove in the vaporization chamber (1)
Day with fog and support frame (2) for supporting demister, the demister include granular filler and for containing holding for granular filler
Packet (3) is carried, there are two the above uniform folds on support frame (2) for the carrying packet (3).
4. desulfurization wastewater treatment system according to claim 3, which is characterized in that support frame as described above (2) is along close to evaporation
The direction of room (1) inner wall tilts gradually downward.
5. desulfurization wastewater treatment system according to claim 3, which is characterized in that more than two carrying packets (3) are equal
In a ring and be arranged concentrically, it is two neighboring carrying packet (3) between be fixedly connected and: inside carrying packet (3) outer diameter and outside hold
The internal diameter for carrying packet (3) is adapted.
6. desulfurization wastewater treatment system according to claim 3, which is characterized in that along vaporization chamber in the vaporization chamber (1)
(1) circumferential to be provided with supporting table (4), support frame as described above (2) is located on supporting table (4), and the width of the supporting table (4) is greater than outer
The maximum carrying packet (3) of diameter is at a distance from vaporization chamber (1) inner wall.
7. desulfurization wastewater treatment system according to claim 1, which is characterized in that the vaporization chamber (1) and hyperbaric heating
The circulating water pipe that the liquid in vaporization chamber (1) is transferred to hyperbaric heating room (5), the circulating water pipe are additionally provided in room (5)
On be provided with check-valves and/or force (forcing) pump.
8. desulfurization wastewater treatment system according to claim 1, which is characterized in that setting in the hyperbaric heating room (5)
There is heat exchanger, the heat exchanger includes the serpentine-like heat exchanger plates (6) of bending, and heat exchanger is divided into first and changed by the heat exchanger plates (6)
Hot cell (51) and the second Heat Room (52), one end of first Heat Room (51) are provided with water inlet (54), other end setting
There is the communication port (53) being connected to the second Heat Room (52), second Heat Room (52) is arranged far from the one end of communication port (53)
There is the discharge outlet (55) being connected to vaporization chamber (1)；Hyperbaric heating room (5) top surface is provided with exhaust outlet (56).
9. desulfurization wastewater treatment system according to claim 8, which is characterized in that first Heat Room (51) and second
It is provided with baffle plate (7) in Heat Room (52), described baffle plate (7) one end is fixed on hyperbaric heating room (5) side wall, another
End is located on the inside of the bending section of heat exchanger plates (6) and is provided with baffling gap, the baffle plate (7) and heat exchanger plates between bending section
(6) bending section corresponds.
10. desulfurization wastewater treatment system according to claim 9, which is characterized in that heat exchanger plates (6) bending section it is interior
The direction of lateral edge liquid flowing is disposed with the first deflector (8) and the second deflector (9), the first deflector (8) position
Liquid feeding side, the second deflector (9) in corresponding baffling gap are respectively positioned on the tapping side in corresponding baffling gap, and second water conservancy diversion
One end of plate (9) close first deflector (8) is between the first deflector (8) and bending section.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910390843.XA CN110028121B (en) | 2019-05-10 | 2019-05-10 | Desulfurization wastewater treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910390843.XA CN110028121B (en) | 2019-05-10 | 2019-05-10 | Desulfurization wastewater treatment system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN110028121A true CN110028121A (en) | 2019-07-19 |
| CN110028121B CN110028121B (en) | 2021-10-22 |
Family
ID=67241794
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910390843.XA Active CN110028121B (en) | 2019-05-10 | 2019-05-10 | Desulfurization wastewater treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110028121B (en) |
Citations (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB191025560A (en) * | 1909-11-09 | 1911-05-11 | Franz Scheinemann | Improvements in Evaporating Apparatus. |
| GB794379A (en) * | 1956-02-02 | 1958-04-30 | Westinghouse Electric Int Co | Improvements in or relating to flash evaporating and condensing systems |
| CN1738668A (en) * | 2002-11-13 | 2006-02-22 | 迪卡产品合伙有限公司 | Pressurized vapor cycle liquid distillation |
| CN201735192U (en) * | 2010-07-27 | 2011-02-09 | 上海亿华科技有限公司 | Internal circulating evaporator with settling chamber |
| CN102861448A (en) * | 2012-09-14 | 2013-01-09 | 苏州市中衡压力容器制造有限公司 | Special pipe header of forced-effect circulation evaporator |
| CN103071310A (en) * | 2013-01-31 | 2013-05-01 | 江苏井神盐化股份有限公司 | Evaporating crystallizer |
| CN103537105A (en) * | 2012-07-11 | 2014-01-29 | 蓝星(北京)化工机械有限公司 | Multi-phase flow evaporation system with distributor and application of multi-phase flow evaporation system |
| CN203595433U (en) * | 2013-12-10 | 2014-05-14 | 山东蓝星清洗防腐公司 | Novel fixed tube-sheet exchanger |
| CN104803535A (en) * | 2015-05-06 | 2015-07-29 | 广州新普利节能环保科技有限公司 | Recycling system and recycling process for recycling salt from desulfurization waste water |
| CN105129890A (en) * | 2015-10-07 | 2015-12-09 | 中国轻工业长沙工程有限公司 | Evaporating crystallizer |
| CN205672578U (en) * | 2016-04-21 | 2016-11-09 | 陕西省石油化工研究设计院 | A kind of be applied to zero discharge of industrial waste water go out salt device |
| CN205773469U (en) * | 2016-06-08 | 2016-12-07 | 广州汉泰环境技术有限公司 | A kind of crystallization apparatus for realizing desulfurization wastewater zero-emission |
| CN207095347U (en) * | 2017-03-14 | 2018-03-13 | 广州赛唯热工设备有限公司 | A kind of node tube type oil cooler |
| CN107930175A (en) * | 2017-12-28 | 2018-04-20 | 沈阳东方钛业股份有限公司 | A kind of crystallizer for MVR sewage disposal systems |
| CN207456243U (en) * | 2017-11-02 | 2018-06-05 | 重庆市映天辉氯碱化工有限公司 | Tubular heat exchanger and chlorine cooling system |
| CN207671727U (en) * | 2017-10-31 | 2018-07-31 | 武汉格瑞拓机械有限公司 | A kind of Crystallization Separation tank and evaporation and crystallization system |
-
2019
- 2019-05-10 CN CN201910390843.XA patent/CN110028121B/en active Active
Patent Citations (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB191025560A (en) * | 1909-11-09 | 1911-05-11 | Franz Scheinemann | Improvements in Evaporating Apparatus. |
| GB794379A (en) * | 1956-02-02 | 1958-04-30 | Westinghouse Electric Int Co | Improvements in or relating to flash evaporating and condensing systems |
| CN1738668A (en) * | 2002-11-13 | 2006-02-22 | 迪卡产品合伙有限公司 | Pressurized vapor cycle liquid distillation |
| CN201735192U (en) * | 2010-07-27 | 2011-02-09 | 上海亿华科技有限公司 | Internal circulating evaporator with settling chamber |
| CN103537105A (en) * | 2012-07-11 | 2014-01-29 | 蓝星(北京)化工机械有限公司 | Multi-phase flow evaporation system with distributor and application of multi-phase flow evaporation system |
| CN102861448A (en) * | 2012-09-14 | 2013-01-09 | 苏州市中衡压力容器制造有限公司 | Special pipe header of forced-effect circulation evaporator |
| CN103071310A (en) * | 2013-01-31 | 2013-05-01 | 江苏井神盐化股份有限公司 | Evaporating crystallizer |
| CN203595433U (en) * | 2013-12-10 | 2014-05-14 | 山东蓝星清洗防腐公司 | Novel fixed tube-sheet exchanger |
| CN104803535A (en) * | 2015-05-06 | 2015-07-29 | 广州新普利节能环保科技有限公司 | Recycling system and recycling process for recycling salt from desulfurization waste water |
| CN105129890A (en) * | 2015-10-07 | 2015-12-09 | 中国轻工业长沙工程有限公司 | Evaporating crystallizer |
| CN205672578U (en) * | 2016-04-21 | 2016-11-09 | 陕西省石油化工研究设计院 | A kind of be applied to zero discharge of industrial waste water go out salt device |
| CN205773469U (en) * | 2016-06-08 | 2016-12-07 | 广州汉泰环境技术有限公司 | A kind of crystallization apparatus for realizing desulfurization wastewater zero-emission |
| CN207095347U (en) * | 2017-03-14 | 2018-03-13 | 广州赛唯热工设备有限公司 | A kind of node tube type oil cooler |
| CN207671727U (en) * | 2017-10-31 | 2018-07-31 | 武汉格瑞拓机械有限公司 | A kind of Crystallization Separation tank and evaporation and crystallization system |
| CN207456243U (en) * | 2017-11-02 | 2018-06-05 | 重庆市映天辉氯碱化工有限公司 | Tubular heat exchanger and chlorine cooling system |
| CN107930175A (en) * | 2017-12-28 | 2018-04-20 | 沈阳东方钛业股份有限公司 | A kind of crystallizer for MVR sewage disposal systems |
Also Published As
| Publication number | Publication date |
|---|---|
| CN110028121B (en) | 2021-10-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| WO2016086735A1 (en) | Apparatus and method for producing magnesium sulphate from coal-fired boiler flue gas | |
| CN110183025A (en) | Desulfurization wastewater recycling processing method and system | |
| CN104925986B (en) | Steel industry pickle liquor and flushing waste water near-zero release processing system and technique thereof | |
| CN104445477B (en) | Evaporative-crystallization salt making equipment and wastewater treatment system for treating high-salt organic wastewater | |
| CN208008627U (en) | Brine waste zero emission system | |
| CN104445725B (en) | Waste gas and high-concentration ammonia nitrogenous wastewater process integrated apparatus | |
| CN102923893A (en) | System and method for treating wastewater containing sodium chloride | |
| CN102698463A (en) | Moving bed type thermal method distillation crystallizer | |
| CN203971422U (en) | A kind of device that is applicable to the separation of emulsion internal solvent | |
| CN106145487A (en) | A kind of technique processing rare-earth trade high-concentration ammonia nitrogenous wastewater reuse | |
| CN203820492U (en) | Continuous wastewater evaporation-concentration-crystallization device | |
| CN208525882U (en) | Vacuum flash evaporation mould and multistage flash distillation crystallization apparatus | |
| CN110028121A (en) | Desulfurization wastewater treatment system | |
| CN105129890A (en) | Evaporating crystallizer | |
| CN103537105A (en) | Multi-phase flow evaporation system with distributor and application of multi-phase flow evaporation system | |
| RU161443U1 (en) | FLOATING UNIT FOR CRYSTALLIZING SOLUTIONS | |
| CN104524806B (en) | A kind of hexamethylenamine complete continuous crystallisation production technology and equipments | |
| CN108128971B (en) | Dithioformate-containing wastewater treatment device | |
| CN203833712U (en) | Water softening device | |
| CN108793557B (en) | Desulfurization wastewater bypass flue evaporation treatment process and system | |
| CN110237558A (en) | A kind of integrated crystallization apparatus and method for crystallising with continuous fine crystal elimination circulation | |
| CN202700112U (en) | Multiphase flow evaporation system with distributor | |
| CN205023891U (en) | Crystallizing evaporator | |
| CN103435213A (en) | Three-phase flow separation device for natural gas wastewater | |
| CN104772033B (en) | Flue gas dry wet purification recovery processing system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |