CN210237223U - Strong oxidant contact tank - Google Patents
Strong oxidant contact tank Download PDFInfo
- Publication number
- CN210237223U CN210237223U CN201921154616.9U CN201921154616U CN210237223U CN 210237223 U CN210237223 U CN 210237223U CN 201921154616 U CN201921154616 U CN 201921154616U CN 210237223 U CN210237223 U CN 210237223U
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- cell body
- baffler
- board
- cell
- accordance
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- 239000007800 oxidant agent Substances 0.000 title claims abstract description 18
- 230000001590 oxidative effect Effects 0.000 title claims description 11
- 210000005056 cell body Anatomy 0.000 claims abstract description 42
- 230000004888 barrier function Effects 0.000 claims description 32
- 238000003756 stirring Methods 0.000 claims description 23
- 210000004027 cell Anatomy 0.000 claims description 11
- 230000003014 reinforcing effect Effects 0.000 claims description 9
- 230000000149 penetrating effect Effects 0.000 claims description 2
- 238000006243 chemical reaction Methods 0.000 abstract description 18
- 230000000903 blocking effect Effects 0.000 description 14
- 239000007788 liquid Substances 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 238000000034 method Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 230000014759 maintenance of location Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 125000003636 chemical group Chemical group 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model relates to a strong oxidizer contact tank, including cell body and the breather pipe of setting in the cell body bottom, the one end of breather pipe is located the cell body outside, and the breather pipe is located one of the cell body outside and serves and install the air pump, cell body internal fixation install at least two sets of bafflers, contain a baffler in every baffler of group at least, wherein a set of baffler fixed connection is in one side of cell body, another set of baffler fixed connection is at the opposite side of cell body, the bottom surface of baffler is the inclined plane, and the baffler bottom surface is close to the one end of its connected cell body and is the lower extreme on inclined plane, the projection sum of two sets of bafflers on the horizontal plane is greater. The gas can fully react with the moisture in the tank body, and the reaction efficiency is improved.
Description
Technical Field
The utility model relates to a strong oxidizer apparatus for producing's technical field especially relates to a strong oxidizer contact pond.
Background
The strong oxidant is required to react by mixing a plurality of materials in the manufacturing process, wherein one of the materials is required to mix gas and liquid, water is put into a contact pool, and plasma gas is introduced into the contact pool to react with the water to generate active chemical groups capable of generating the strong oxidation reaction. The existing contact pool has the following defects: the floating speed of the gas is slow, the bubbles are large, the contact between the gas and the liquid is less, and the gas which is not completely reacted floats out of the water surface, so that the resource waste is caused.
If the granted public number is CN205965726U discloses a strong oxidizer contact tank, including cell body and the breather pipe that lets in the cell body bottom, the intake pipe of breather pipe extends to the cell body outside, is linked together with the air pump that is located cell body one side, set up the venthole on the breather pipe, the short upwards of giving vent to anger of venthole is provided with the bubble in the cell body and breaks up the device. Which increases the reaction rate. However, in such a structure, the retention time of the gas in the contact cell is mainly determined by the height of water in the contact cell, and the depth of the contact cell is generally not so high that the retention time of the plasma gas in the contact cell is short, and even if the gas is scattered, the incomplete reaction is likely to occur.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a strong oxidizer contact tank, when letting in gas from the cell body bottom, the time that gas was retained in the contact tank is longer relatively, and the reaction is more complete.
The above object of the present invention can be achieved by the following technical solutions: the utility model provides a strong oxidizer contact tank, includes the cell body and sets up the breather pipe in the cell body bottom, and the one end of breather pipe is located the cell body outside, and the breather pipe is located one of the cell body outside and serves and install the air pump, the cell body in fixed mounting have at least two sets of bafflers, contain a baffler in every baffler at least, one of them baffler fixed connection is in one side of cell body, another group of baffler fixed connection is at the opposite side of cell body, the bottom surface of baffler is the inclined plane, and the baffler bottom surface is close to the one end of its connected cell body and is the least significant end on inclined plane, the projection sum of two sets of bafflers on.
Through adopting above-mentioned technical scheme, after letting in gas on the cell body bottom, the bubble floats. When the air bubbles float to the position attached to the bottom surface of the blocking plate, the bottom surface of the blocking plate is inclined, so that the air bubbles move towards the higher end of the bottom surface of the blocking plate. When the bubbles move to the end with the higher bottom surface of the baffle plate, the bubbles separate from the bottom surface of the baffle plate and continuously float upwards. Because the sum of the projections of the two groups of baffle plates on the horizontal plane is larger than the cross section of the tank body, namely, a part of overlapped position exists between the two groups of baffle plates, after the bubbles float upwards, the bubbles are finally attached to the bottom surface of the baffle plate adjacent to the upper side of the baffle plate and continue to move along the bottom surface of the baffle plate. The time that its effectual bubble that has increased is stayed in the cell body makes gas can be more for abundant moisture reaction with the cell body, has improved reaction efficiency.
The utility model discloses further set up to: the higher one side of separation board bottom surface be connected with the mesh board, the other end that the mesh board kept away from its connected separation board is connected with the cell body, the length of mesh board equals the side length that mesh board and separation board are connected.
Through adopting above-mentioned technical scheme, through the mesh board, be connected between the higher one end of baffler bottom surface and the cell body, and through the hole on the mesh board, when great bubble passes through the mesh board, can be broken up and become less bubble, make gaseous and the liquid contact surface in the cell body bigger, improved reaction efficiency, the phenomenon of incomplete reaction is difficult for appearing.
The utility model discloses further set up to: the barrier plate on wear to be equipped with vertical axis of rotation, and the axis of rotation passes a set of barrier plate at least, the axis of rotation is by motor drive, installs stirring paddle in the axis of rotation.
Through adopting above-mentioned technical scheme, at the pivoted in-process of axis of rotation, stirring paddle stirs the liquid in the cell body. Because the gas and the liquid are separated by the baffle plate in the process of reacting, the liquid in each part is easy to have the phenomenon of uneven reaction. The stirring paddle can drive the liquid to rotate together, so that the water in the tank body is stirred uniformly, and the reaction is more uniform.
The utility model discloses further set up to: the stirring paddle installed on one rotating shaft is at least two, and at least one stirring paddle is arranged between the two barrier plates which are adjacent up and down and the barrier plate at the lowest side and the bottom surface of the tank body.
Through adopting above-mentioned technical scheme, increased stirring paddle's quantity, stirring that can be fine makes the moisture in the pond stirred evenly, and the reaction is more even.
The utility model discloses further set up to: at least two rotating shafts penetrate through the group of barrier plates, and the rotating shafts are located at the positions of the projections of the two groups of barrier plates, which are superposed on the horizontal plane.
Through adopting above-mentioned technical scheme, be provided with many (mixing) shafts, stirring that can be better makes the moisture in the pond by the stirring, can fully react.
The utility model discloses further set up to: the rotating directions of the rotating shafts penetrating through the group of barrier plates are the same.
Through adopting above-mentioned technical scheme, each (mixing) shaft is because the rotation direction is the same to make the rivers direction conflict that each (mixing) shaft drove, can play better stirring effect, make the moisture in the pond by the stirring, can fully react.
The utility model discloses further set up to: and reinforcing strips are fixedly arranged on the upper surface of the barrier plate.
Through adopting above-mentioned technical scheme, strengthen the effectual intensity that increases the baffler of strip, make it be difficult for being damaged.
The utility model discloses further set up to: the cross section of the reinforcing strip is in a shape of a minor arc.
Through adopting above-mentioned technical scheme, rivers in the cell body are by the in-process of (mixing) shaft stirring, and the resistance that the enhancement strip received is little, is difficult for being damaged, has improved the life of strengthening the strip.
To sum up, the utility model discloses a beneficial technological effect does:
1. the gas introduced into the tank body can more fully react with the moisture in the tank body, so that the reaction efficiency is improved;
2. the stirring paddle can drive the liquid in the tank body to rotate together, so that the water in the tank body is uniformly stirred, and the reaction is more uniform.
Drawings
Fig. 1 is a schematic structural diagram of the present invention;
FIG. 2 is a schematic structural view after a part of the tank body and a part of the barrier plate are hidden.
Reference numerals: 1. a tank body; 11. a breather pipe; 12. an air pump; 2. a barrier plate; 21. a mesh plate; 3. a rotating shaft; 31. a stirring paddle; 4. a reinforcing strip.
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings.
As shown in figure 1, the strong oxidant contact tank comprises a square tank body 1, a vent pipe 11 penetrates through the bottom end of the side surface of the tank body 1, an air pump 12 is installed at one end, located on the outer side of the tank body 1, of the vent pipe 11, and the other end of the vent pipe 11 is located in the tank body 1.
As shown in fig. 1 and 2, two groups of baffle plates 2 are fixedly arranged in the tank body 1. Each group of baffle plates 2 is provided with two. A group of baffle plates 2 are respectively arranged on the side surfaces of two sides of the wide position in the tank body 1. The blocking plate 2 is a rectangular plate, the top surface of the blocking plate 2 is horizontally arranged, and the bottom surface of the blocking plate is obliquely arranged. The side of the bottom surface of the blocking plate 2 connected with the tank body 1 is the side with the lowest height in the bottom surface of the blocking plate 2, the length of the side is equal to the width of the water tank, and the length of the side, perpendicular to the width of the water tank, of the upper surface of the blocking plate 2 is larger than half of the length of the water tank. A mesh plate 21 is fixedly arranged on one side of the blocking plate 2 far away from the side face of the tank body 1 connected with the blocking plate, the width of the mesh plate 21 is equal to that of the blocking plate 2, and the mesh plate 21 and the upper surface of the blocking plate 2 are positioned in the same plane. The other side of the mesh plate 21 is fixedly connected with the side wall of the tank body 1. The intervals between the baffle plates 2 are equal and are arranged in the tank body 1 in a staggered mode in sequence. When larger bubbles pass through the mesh plate 21, the larger bubbles are scattered into smaller bubbles, so that the contact surface of gas and liquid in the pool body 1 is larger, the reaction efficiency is improved, and the phenomenon of incomplete reaction is not easy to occur.
As shown in fig. 1 and 2, two vertical rotating shafts 3 penetrate through the blocking plate 2, and a plane where the two rotating shafts 3 are located passes through the middle point of the longer side edge of the tank body 1. The rotating shaft 3 penetrates through the four barrier plates 2 simultaneously, four stirring blades 31 are mounted on the rotating shaft 3, and one stirring blade 31 is arranged between the two adjacent barrier plates 2 and between the barrier plate 2 at the lowest side and the bottom surface of the tank body 1. The rotating shaft 3 is driven by a motor to rotate, and the rotating directions are the same. Since the gas and the liquid are separated by the barrier plate 2 during the reaction, the liquid in each part is prone to have uneven reaction. The stirring paddle 31 can drive the liquid to rotate together to stir the water in the tank body 1. Two (mixing) shafts can play better stirring effect because the rotation direction is the same, make the moisture in the cell body 1 stirred evenly, can fully react.
As shown in fig. 2, at least two reinforcing strips 4 are formed on the upper surface of the barrier plate 2 in a protruding manner, the reinforcing strips 4 are parallel to each other, and the distance between two adjacent reinforcing strips 4 is equal. The cross section of the reinforcing bar 4 is in the shape of a minor arc segment. Strengthen the effectual intensity that increases barrier plate 2 of strip 4, and the rivers in cell body 1 are stirred by the (mixing) shaft in-process, and the resistance that strengthens strip 4 and receive is little, is difficult for being damaged, has improved the life who strengthens strip 4.
After gas is introduced into the bottom end of the tank body 1, the bubbles float upwards. When the bubbles float to the position where they are attached to the bottom surface of the barrier plate 2, the bottom surface of the barrier plate 2 is inclined, and therefore, the bubbles move toward the higher end of the bottom surface of the barrier plate 2. When the bubbles move to the end with the higher bottom surface of the baffle plate 2, the bubbles continuously float upwards through the mesh plate 21. Because the sum of the projections of the two groups of barrier plates 2 on the horizontal plane is larger than the cross section of the tank body 1, namely, a position of partial overlap exists between the two groups of barrier plates 2, after the bubbles float upwards, the bubbles are finally attached to the bottom surface of the barrier plate 2 adjacent to the upper side of the barrier plate 2 and continue to move along the bottom surface of the barrier plate 2. The time of bubbles remaining in the pool body 1 is effectively increased, so that the gas can be more fully reacted with the moisture in the pool body 1, and the reaction efficiency is improved.
The embodiment of this specific implementation mode is the preferred embodiment of the present invention, not limit according to this the utility model discloses a protection scope, so: all equivalent changes made according to the structure, shape and principle of the utility model are covered within the protection scope of the utility model.
Claims (8)
1. The utility model provides a strong oxidizer contact tank, includes cell body (1) and sets up breather pipe (11) in cell body (1) bottom, and the one end of breather pipe (11) is located cell body (1) outside, and breather pipe (11) are located one of cell body (1) outside and serve and install air pump (12), its characterized in that: cell body (1) internal fixed mounting have at least two sets of baffler board (2), contain a baffler board (2) in every group baffler board (2) at least, wherein one side of a set of baffler board (2) fixed connection in cell body (1), another side of baffler board (2) fixed connection in cell body (1), the bottom surface of baffler board (2) is the inclined plane, and baffler board (2) bottom surface is close to the one end of its connected cell body (1) and is the least significant end on inclined plane, the projection sum of two sets of baffler board (2) on the horizontal plane is greater than the cross section of cell body (1).
2. A strong oxidant contact cell in accordance with claim 1, wherein: the higher one side of baffler (2) bottom surface be connected with mesh board (21), mesh board (21) keep away from the other end and the cell body (1) of baffler (2) that it connects, the length of mesh board (21) equals the side length that mesh board (21) and baffler (2) are connected.
3. A strong oxidant contact cell in accordance with claim 1, wherein: barrier plate (2) on wear to be equipped with vertical axis of rotation (3), and axis of rotation (3) pass a set of barrier plate (2) at least, axis of rotation (3) are by motor drive, install stirring paddle (31) on axis of rotation (3).
4. A strong oxidant contact cell in accordance with claim 3, wherein: the stirring paddle (31) installed on one rotating shaft (3) is at least two, and at least one stirring paddle (31) is arranged between the two barrier plates (2) which are adjacent up and down and the barrier plate (2) at the lowest side and the bottom surface of the tank body (1).
5. A strong oxidant contact cell in accordance with claim 4, wherein: at least two rotating shafts (3) penetrate through the group of barrier plates (2), and the rotating shafts (3) are located at the positions of the projections of the two groups of barrier plates (2) superposed on the horizontal plane.
6. A strong oxidant contact cell in accordance with claim 5, wherein: the rotating directions of the rotating shafts (3) penetrating through the group of barrier plates (2) are the same.
7. A strong oxidant contact cell in accordance with claim 1, wherein: and a reinforcing strip (4) is fixedly arranged on the upper surface of the barrier plate (2).
8. A strong oxidant contact cell in accordance with claim 7, wherein: the cross section of the reinforcing strip (4) is in a shape of a minor arc.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921154616.9U CN210237223U (en) | 2019-07-22 | 2019-07-22 | Strong oxidant contact tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921154616.9U CN210237223U (en) | 2019-07-22 | 2019-07-22 | Strong oxidant contact tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210237223U true CN210237223U (en) | 2020-04-03 |
Family
ID=69992236
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921154616.9U Active CN210237223U (en) | 2019-07-22 | 2019-07-22 | Strong oxidant contact tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210237223U (en) |
-
2019
- 2019-07-22 CN CN201921154616.9U patent/CN210237223U/en active Active
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 362201 room 402, building 6, Juzhi real estate, No. 565, Meiling Road, Bishan community, Meiling street, Jinjiang City, Quanzhou City, Fujian Province Patentee after: Fujian Jinlan Environmental Protection Co.,Ltd. Country or region after: China Address before: 362201 room 402, building 6, Juzhi real estate, No. 565, Meiling Road, Bishan community, Meiling street, Jinjiang City, Quanzhou City, Fujian Province Patentee before: Fujian Jinlan Environmental Protection Technology Co.,Ltd. Country or region before: China |
|
| CP03 | Change of name, title or address |