CN208586082U - VOCs separator in waste water - Google Patents
VOCs separator in waste water Download PDFInfo
- Publication number
- CN208586082U CN208586082U CN201821107020.9U CN201821107020U CN208586082U CN 208586082 U CN208586082 U CN 208586082U CN 201821107020 U CN201821107020 U CN 201821107020U CN 208586082 U CN208586082 U CN 208586082U
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- waste water
- vocs
- tower
- separator
- distribution apparatus
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Abstract
VOCs separator in a kind of waste water of the utility model, including air blower, finned heat exchanger, degassing tower, circulating pump, degassing tower includes tower reactor, tower section, the connection of the top of tower section and tower reactor, one upper lateral part of tower reactor is equipped with air intlet, air blower, finned heat exchanger, air intlet is sequentially connected with, another side lower part of tower reactor is equipped with wastewater outlet, one upper lateral part of tower section is equipped with waste water inlet, the other side of tower section, which corresponds to, is equipped with refluxing opening at waste water inlet position, wastewater outlet, circulating pump, refluxing opening is sequentially connected with, the top of tower section is equipped with gas outlet, demister is from top to bottom arranged in sequence in Ta Jienei, distribution apparatus, distribution apparatus is at least provided with two groups, waste water inlet, refluxing opening is arranged between demister and distribution apparatus.VOCs separator in the waste water that the technical problem to be solved by the present invention is to provide a kind of structures is simple, separative efficiency is high, easy to operate.
Description
Technical field
The utility model relates to field of waste water treatment, more particularly to VOCs separator in a kind of waste water.
Background technique
With the continuous exacerbation of environmental problem, people increasingly pay attention to environmental problem, reduce by various modes or drop
Low environment pollution.Currently, it is dissolved with volatile organic compounds (abbreviation VOCs) in waste water, when handling waste water, needed
VOCs in waste water is separated, is then individually handled respectively, waste water and VOCs is made to be attained by processing requirement.It is existing
There is VOCs separative efficiency in separator low, there are still a large amount of VOCs in waste water, subsequent wastewater treatment is caused to be not thorough, needs
Repeatedly to handle can be only achieved emission request, cumbersome.
Utility model content
That the technical problem to be solved by the present invention is to provide a kind of structures is simple, separative efficiency is high, easy to operate useless
VOCs separator in water.
VOCs separator in a kind of waste water of the utility model, including air blower, finned heat exchanger, degassing tower, circulating pump,
The degassing tower includes tower reactor, tower section, and the top of the tower section and tower reactor connects, a upper lateral part of the tower reactor be equipped with air into
Mouthful, the air blower, finned heat exchanger, air intlet are sequentially connected with, and another side lower part of the tower reactor is equipped with wastewater outlet, institute
The upper lateral part for stating tower section is equipped with waste water inlet, and the other side of the tower section, which corresponds to, is equipped with reflux at the waste water inlet position
Mouthful, the wastewater outlet, circulating pump, refluxing opening are sequentially connected with, and the top of the tower section is equipped with gas outlet, and the Ta Jienei is by upper
Demister, distribution apparatus are arranged in sequence under, at least provided with two groups, the waste water inlet, refluxing opening are all provided with the distribution apparatus
It sets between the demister and distribution apparatus.
VOCs separator in the utility model waste water, wherein the distribution apparatus includes point being from top to bottom sequentially arranged
Cloth device, filler, the filler are fixed on packing support.
VOCs separator in the utility model waste water, wherein deflector is equipped between the adjacent distribution apparatus, it is described
The lower part of the packing support is arranged in deflector.
VOCs separator in the utility model waste water, the setting wherein deflector slopes inwardly from top to bottom.
VOCs separator in the utility model waste water is equidistantly set on the chassis wherein the distributor includes chassis
There are several liquid separation slots, the inner wall of each liquid separation slot is equipped with several liquid separation columns, and the liquid separation column is to be connected to chassis up and down
The communicating structure of opening.
VOCs separator in the utility model waste water, wherein the filler is Raschig ring polytetrafluoro filler.
VOCs separator in the utility model waste water, wherein the top of the tower reactor is equipped with gas-liquid intersection connection section,
The gas-liquid intersection connection section includes cavity, and the top of the cavity is equipped with the first intersection connecting with tower section, the chamber
Each side of body is equipped with the second intersection.
VOCs separator in the utility model waste water, wherein the demister uses wire mesh demister.
Compared with prior art, advantages and beneficial effects possessed by the utility model are as follows: 1. the utility model uses wing
Piece heat exchanger heats air, and according to the characteristic of VOCs, temperature is higher, and solubility is lower, and heating air is filled with waste water
When tap touching, heat conversion is carried out, solubility of the VOCs in waste water is reduced, is detached from VOCs more preferably from waste water, is improved useless
The separative efficiency of VOCs in water.2. the utility model persistently carries out air delivery using air blower, and in the work of finned heat exchanger
Persistently there is heating air to convey into degassing tower through air intlet with lower, further decreases at air intlet VOCs in waste water
Solubility improves the separative efficiency of VOCs in waste water so as to realize degassing purpose more thoroughly.3. the utility model tower section
The interior distribution apparatus equipped at least two groups, distribution apparatus make waste water be evenly distributed with heating air, increase waste water and heating air
Contact area, make waste water and heating air carry out more fully heat convert, prevent waste water with heat each self aggregation of air make
It is insufficient at gas-liquid contact.4. the top of the utility model tower reactor is equipped with gas-liquid intersection connection section, gas-liquid intersection connection section
Including cavity, the top of cavity is equipped with the first intersection connecting with tower section, and each side of cavity is equipped with the second intersection.
Heating air successively enters Ta Jienei through the second intersection, the first intersection, and waste water is successively through the first intersection, the second intersection
Into in tower reactor, the setting of gas-liquid intersection connection section, which can be realized, carries out shunting function to heating air, waste water, both prevents from giving up
Dropped down onto tower reactor under water causes heating air that cannot normally rise because flow is excessive, and then causes to separate the phenomenon that interrupting,
Also solve the problems, such as to cause liquid in tower section cannot normally fall since air blower wind pressure is excessive.5. the utility model separation process
Processing be simple and convenient to operate, separating effect is stable, it is practical, have a wide range of application.
VOCs separator in the waste water of the utility model is described further with reference to the accompanying drawing.
Detailed description of the invention
Fig. 1 is the structure chart of VOCs separator in the utility model waste water;
Fig. 2 is the structure chart of degassing tower in VOCs separator in the utility model waste water;
Fig. 3 is the structure chart of distributor in VOCs separator in the utility model waste water;
Fig. 4 is the structure chart of connection section in gas-liquid intersection in VOCs separator in the utility model waste water;
Wherein: 1, air blower;2, finned heat exchanger;3, degassing tower;4, circulating pump;5, tower reactor;6, air intlet;7, gas-liquid
Intersection connection section;71, cavity;72, the first intersection;73, the second intersection;8, tower section;9, packing support;10, filler;
11, distributor;111, chassis;112, liquid separation slot;113, liquid separation column;12, deflector;13, waste water inlet;14, gas outlet;15,
Demister;16, refluxing opening;17, wastewater outlet.
Specific embodiment
As shown in Figure 1 and Figure 2, VOCs separator in a kind of waste water of the utility model, including air blower 1, finned heat exchanger
2, degassing tower 3, circulating pump 4, degassing tower 3 include tower reactor 5, tower section 8, and tower section 8 is connect with the top of tower reactor 5, on the side of tower reactor 5
Portion is equipped with air intlet 6, and air blower 1, finned heat exchanger 2, air intlet 6 are sequentially connected with, and another side lower part of tower reactor 5 is equipped with useless
One upper lateral part of water out 17, tower section 8 is equipped with waste water inlet 13, and the other side of tower section 8 corresponds to be equipped at 13 position of waste water inlet
Refluxing opening 16, wastewater outlet 17, circulating pump 4, refluxing opening 16 are sequentially connected with, and the top of tower section 8 is equipped with gas outlet 14, in tower section 8
Demister 15, distribution apparatus is from top to bottom arranged in sequence, for distribution apparatus at least provided with two groups, waste water inlet 13, refluxing opening 16 are equal
It is arranged between demister 15 and distribution apparatus.
Air is blasted by air blower 1, and finned heat exchanger 2 passes through raw saturated vapor and heats to the air blasted, is then passed through
Air intlet 6 is delivered in degassing tower 3, and waste water is delivered in degassing tower 3 through waste water inlet 13, and waste water moves downward, and heating is empty
Gas moves upwards, and after waste water comes into full contact with heating air, waste water conveys again through wastewater outlet 17, circulating pump 4, refluxing opening 16
To degassing tower 3, multiple circular treatment carried out to waste water, processing to after to a certain degree according to a certain percentage by waste water outlet,
Air, through 14 outlet of gas outlet, thus completes the separation of VOCs in waste water after 15 foam removal of demister.
The utility model separation process processing be simple and convenient to operate, separating effect is stable, it is practical, have a wide range of application.
The utility model heats air using finned heat exchanger 2, and according to the characteristic of VOCs, temperature is higher, molten
Xie Du is lower, when heating air and waste water come into full contact with, carries out heat conversion, reduces solubility of the VOCs in waste water, makes
VOCs is more preferably detached from from waste water, improves the separative efficiency of VOCs in waste water.
The utility model persistently carries out air delivery using air blower 1, and persistently has under the action of finned heat exchanger 2 and add
Hot-air is conveyed through air intlet 6 into degassing tower 3, further decreases solubility of the VOCs in waste water at air intlet 6, from
And can be realized degassing purpose more thoroughly, improve the separative efficiency of VOCs in waste water.
The distribution apparatus of at least two groups is equipped in the utility model tower section 8, distribution apparatus makes waste water and heating air distribution
Uniformly, increase waste water and heat the contact area of air, so that waste water and heating air is carried out more fully heat and convert, prevent from giving up
Water causes gas-liquid contact insufficient with heating each self aggregation of air.
Further, distribution apparatus includes the distributor 11 being from top to bottom sequentially arranged, filler 10, and filler 10, which is fixed on, to be filled out
In material support 9.
Further, deflector 12 is equipped between adjacent distributions device, the lower part of packing support 9 is arranged in deflector 12,
Deflector 12 slopes inwardly setting from top to bottom.Deflector 12 guarantees that the liquid flowed out through upper one group of distribution apparatus converges water conservancy diversion
To next group of distribution apparatus.
Further, as shown in figure 3, distributor 11 includes chassis 111, several liquid separation slots are equidistantly equipped on chassis 111
112, the inner wall of each liquid separation slot 112 is equipped with several liquid separation columns 113, and liquid separation column 113 is to be connected to upper and lower opening with chassis 111
Communicating structure.Waste water carries out branch's water conservancy diversion through liquid separation column 113, is evenly distributed, and prevents liquid accumulation confluence from causing gas-liquid contact not
Sufficiently, VOCs separating effect in waste water is influenced.
Further, filler 10 is Raschig ring polytetrafluoro filler.
Further, as shown in figure 4, the top of tower reactor 5 is equipped with gas-liquid intersection connection section 7, gas-liquid intersection connection section 7
Including cavity 71, the top of cavity 71 is equipped with the first intersection 72 connecting with tower section 8, and each side of cavity 71 is equipped with the
Two intersections 73.It heats air successively to enter in tower section 8 through the second intersection 73, the first intersection 72, waste water is successively through first
Intersection 72, the second intersection 73 enter in tower reactor 5, and the setting of gas-liquid intersection connection section 7 can be realized to heating air, give up
Water carries out shunting function, had both prevented waste water from falling in tower reactor 5 and has caused heating air that cannot normally rise because flow is excessive,
And then the phenomenon that causing separation to be interrupted, also solve to cause liquid in tower section 8 cannot normally fall since 1 wind pressure of air blower is excessive
Problem.
Further, demister 15 uses wire mesh demister, can effectively remove the mist carried secretly in gas.
Embodiment described above is only that preferred embodiments of the present invention are described, not practical to this
Novel range is defined, and under the premise of not departing from the spirit of the design of the utility model, those of ordinary skill in the art are to this
The various changes and improvements that the technical solution of utility model is made should all fall into the protection that the utility model claims book determines
In range.
Claims (8)
1. VOCs separator in a kind of waste water, it is characterised in that: including air blower, finned heat exchanger, degassing tower, circulating pump,
The degassing tower includes tower reactor, tower section, and the top of the tower section and tower reactor connects, a upper lateral part of the tower reactor be equipped with air into
Mouthful, the air blower, finned heat exchanger, air intlet are sequentially connected with, and another side lower part of the tower reactor is equipped with wastewater outlet, institute
The upper lateral part for stating tower section is equipped with waste water inlet, and the other side of the tower section, which corresponds to, is equipped with reflux at the waste water inlet position
Mouthful, the wastewater outlet, circulating pump, refluxing opening are sequentially connected with, and the top of the tower section is equipped with gas outlet, and the Ta Jienei is by upper
Demister, distribution apparatus are arranged in sequence under, at least provided with two groups, the waste water inlet, refluxing opening are all provided with the distribution apparatus
It sets between the demister and distribution apparatus.
2. VOCs separator in waste water according to claim 1, it is characterised in that: the distribution apparatus include by up to
Under the distributor, the filler that are sequentially arranged, the filler is fixed on packing support.
3. VOCs separator in waste water according to claim 2, it is characterised in that: set between the adjacent distribution apparatus
There is deflector, the lower part of the packing support is arranged in the deflector.
4. VOCs separator in waste water according to claim 3, it is characterised in that: the deflector is inside from top to bottom
It is obliquely installed.
5. VOCs separator in waste water according to claim 2, it is characterised in that: the distributor includes chassis, institute
It states and is equidistantly equipped with several liquid separation slots on chassis, the inner wall of each liquid separation slot is equipped with several liquid separation columns, and the liquid separation column is
The communicating structure of upper and lower opening is connected to chassis.
6. VOCs separator in waste water according to claim 2, it is characterised in that: the filler is Raschig ring polytetrafluoro
Filler.
7. VOCs separator in waste water according to claim 1, it is characterised in that: the top of the tower reactor is equipped with gas-liquid
Intersection connection section, the gas-liquid intersection connection section include cavity, and the top of the cavity is equipped with connect with tower section first
Each side of intersection, the cavity is equipped with the second intersection.
8. VOCs separator in waste water according to claim 1, it is characterised in that: the demister uses silk screen foam removal
Device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201821107020.9U CN208586082U (en) | 2018-07-13 | 2018-07-13 | VOCs separator in waste water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201821107020.9U CN208586082U (en) | 2018-07-13 | 2018-07-13 | VOCs separator in waste water |
Publications (1)
Publication Number | Publication Date |
---|---|
CN208586082U true CN208586082U (en) | 2019-03-08 |
Family
ID=65540601
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201821107020.9U Active CN208586082U (en) | 2018-07-13 | 2018-07-13 | VOCs separator in waste water |
Country Status (1)
Country | Link |
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CN (1) | CN208586082U (en) |
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2018
- 2018-07-13 CN CN201821107020.9U patent/CN208586082U/en active Active
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