CN209602289U - Organic wastewater oxidation treatment device - Google Patents
Organic wastewater oxidation treatment device Download PDFInfo
- Publication number
- CN209602289U CN209602289U CN201920054454.5U CN201920054454U CN209602289U CN 209602289 U CN209602289 U CN 209602289U CN 201920054454 U CN201920054454 U CN 201920054454U CN 209602289 U CN209602289 U CN 209602289U
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- China
- Prior art keywords
- oxidation chamber
- oxidation
- chamber
- treatment device
- connecting tube
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- 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.)
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- 230000003647 oxidation Effects 0.000 title claims abstract description 125
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 125
- 239000002351 wastewater Substances 0.000 title claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 29
- 238000005192 partition Methods 0.000 claims abstract description 7
- 208000002925 dental caries Diseases 0.000 claims abstract description 3
- 238000003756 stirring Methods 0.000 claims description 30
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 14
- 239000003054 catalyst Substances 0.000 claims description 14
- 238000010438 heat treatment Methods 0.000 claims description 9
- 230000001590 oxidative effect Effects 0.000 claims description 9
- 230000000712 assembly Effects 0.000 claims description 8
- 238000000429 assembly Methods 0.000 claims description 8
- 239000012535 impurity Substances 0.000 claims description 8
- 238000012423 maintenance Methods 0.000 claims description 8
- 238000005485 electric heating Methods 0.000 claims description 6
- 230000002070 germicidal effect Effects 0.000 claims description 6
- 239000007800 oxidant agent Substances 0.000 claims description 6
- 238000007789 sealing Methods 0.000 claims description 6
- 238000001914 filtration Methods 0.000 claims description 3
- 238000009298 carbon filtering Methods 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 10
- 230000000694 effects Effects 0.000 abstract description 6
- 230000003197 catalytic effect Effects 0.000 abstract description 3
- 238000004065 wastewater treatment Methods 0.000 abstract description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- 239000010812 mixed waste Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Physical Water Treatments (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model discloses a kind of organic wastewater oxidation treatment device, including tank body, the tank interior is amount of laterally located and the partition being tightly connected with tank body is divided into the first oxidation chamber, three independent cavitys of second oxidation chamber and third oxidation chamber, first oxidation chamber inside the first connecting tube and the second oxidation chamber by being connected to, second oxidation chamber inside the second connecting tube and third oxidation chamber by being connected to, the first connection pump and the second connection pump are respectively equipped in first connecting tube and the second connecting tube, second oxidation chamber and third oxidation chamber pass through respectively to be connected to inside the first return pipe and the second return pipe and the first oxidation chamber, the first back water pump and the second back water pump are respectively equipped on first return pipe and the second return pipe.The utility model combines photochemical oxidation method and catalytic wet air oxidation, and structure is simple and fully ensures that the effect of wastewater treatment.
Description
Technical field
The utility model belongs to field of waste water treatment, and in particular to a kind of organic wastewater oxidation treatment device.
Background technique
Organic wastewater generally refers to the dirt of the life containing organic substances such as carbohydrate, protein, grease, lignin
The industrial wastewaters such as water, food processing and papermaking.It is right due to organic wastewater complicated component and with peculiar smell and strong acid and strong base
The processing of organic wastewater is increasingly important.Currently, the processing most common mode of organic wastewater is oxidizing process.One of the most common
Oxidizing process is photochemical oxidation method and catalytic wet air oxidation.Currently, there is the oxidation dress for combining two kinds of oxidizing process
It sets, but these devices or structure too complex or treatment of Organic Wastewater are not thorough, and are not able to satisfy actual demand.
Utility model content
Technical problem to be solved in the utility model is in view of the above shortcomings of the prior art, to provide a kind of organic waste
Water oxidation treatment device combines photochemical oxidation method and catalytic wet air oxidation, and structure is simple and fully ensures that useless
The effect of water process.
The technical scheme adopted by the utility model is a kind of organic wastewater oxidation treatment device, including tank body, the tank
Internal portion is amount of laterally located and the partition being tightly connected with tank body is divided into the first oxidation chamber, the second oxidation chamber and third oxidation chamber
Three independent cavitys, first oxidation chamber inside the first connecting tube and the second oxidation chamber by being connected to, second oxidation
Chamber is respectively equipped with first in first connecting tube and the second connecting tube by being connected to inside the second connecting tube and third oxidation chamber
Connection pump and the second connection pump, second oxidation chamber and third oxidation chamber pass through respectively the first return pipe and the second return pipe with
It is connected to inside first oxidation chamber, is respectively equipped with the first back water pump and the second return water on first return pipe and the second return pipe
Pump, the top of the tank are equipped with the water inlet pipe being connected to the first oxidation chamber inside, and the top of the tank is additionally provided with and the first oxidation
The oxidant pipe of intracavitary portion connection, tank body lateral wall position corresponding with third oxidation chamber be equipped with its it is internal be connected to out
Water pipe, the first oxidation chamber inner top surface pass through branch and are provided with ultraviolet germicidal lamp, and two diaphragm internals are provided with heating chamber, institute
Electric heating tube is equipped in heating chamber, the heating chamber bottom is equipped with the heat being connected to inside the second oxidation chamber and third oxidation chamber
Wind channel, the tank body lateral wall are equipped with the catalyst tank that top is provided with opening close to the position at top, and the catalyst tank is logical
It crosses catalyst connecting tube to be connected to inside the second oxidation chamber and third oxidation chamber respectively, second oxidation chamber and third oxidation chamber
Inner sidewall is equipped with the stirring rod being laterally arranged by axle sleeve, its axis is surrounded on the stirring rod and is equipped with array stirring sheet, described
Tank body lateral wall position corresponding with the second oxidation chamber and third oxidation chamber, which is respectively equipped with, to be connect with stirring rod and drives its rotation
Stirring motor.
In one embodiment, first oxidation chamber, the second oxidation chamber are consistent with third oxidation chamber volume.
In one embodiment, filter assemblies are equipped between the water inlet pipe and tank body.
In one embodiment, the filter assemblies include shell, and the enclosure interior is successively arranged along water inlet direction
The large granular impurity filter screen and activated charcoal strainer being tightly connected with its inner sidewall.
In one embodiment, the hull outside wall is corresponding with large granular impurity filter screen and activated charcoal strainer
Position is provided with access hole, and the access hole, which is submitted, is connected to maintenance door.
In one embodiment, sealing ring is equipped between the maintenance door and access hole.
In one embodiment, the stirring sheet includes the main leaf connecting with stirring rod, and the main leaf is far from stirring rod
One end end face be provided with adjusting cavity distributed along its length, bluff bit, the main leaf top are slidably connected in the adjusting cavity
Portion position corresponding with adjusting cavity is equipped with the lock-screw at the top of main leaf and locking main leaf and bluff bit.
The utility model has the beneficial effects that:
1, exhaust gas can be handled respectively inside three oxidation chambers of tank interior, fully ensures that the effect of processing;
2, waste water can be re-fed into the first oxidation chamber by the setting of the first return pipe and the second return pipe, carry out oxygen again
Change, guarantees the effect of oxidation.
Detailed description of the invention
FIG. 1 is a schematic structural view of the utility model;
Fig. 2 is the utility model stirring sheet structural schematic diagram;
Fig. 3 is the utility model filter assemblies structural schematic diagram.
In figure: 1, tank body;2, partition;3, the first oxidation chamber;4, the second oxidation chamber;5, third oxidation chamber;6, the first connection
Pipe;7, the second connecting tube;8, the first connection pump;9, the second connection pump;10, the first return pipe;11, the second return pipe;12, first
Back water pump;13, the second back water pump;14, water inlet pipe;15, oxidant pipe;16, outlet pipe;17, bracket;18, ultraviolet germicidal lamp;
19, heating chamber;20, electric heating tube;21, hot-air channel;22, catalyst tank;23, catalyst connecting tube;24, axle sleeve;25, it stirs
Bar;26, stirring sheet;27, motor is stirred;28, filter assemblies;261, main leaf;262, adjusting cavity;263, bluff bit;264, it locks
Screw;281, shell;282, large granular impurity filter screen;283, activated charcoal strainer;284, maintenance door;285, sealing ring.
Specific embodiment
The utility model is described in further detail below in conjunction with the accompanying drawings and the specific embodiments.
As shown in Figure 1, Figure 2 and Figure 3, a kind of organic wastewater oxidation treatment device, including tank body 1, the 1 inside quilt of tank body
Laterally it is arranged and the partition 2 being tightly connected with tank body 1 is divided into the first oxidation chamber 3, the second oxidation chamber 4 and third oxidation chamber 5 three
A independent cavity, first oxidation chamber 3 inside the first connecting tube 6 and the second oxidation chamber 4 by being connected to, second oxidation
Chamber 4 is set in first connecting tube 6 and the second connecting tube 7 respectively by being connected to inside the second connecting tube 7 and third oxidation chamber 5
There are the first connection pump 8 and the second connection pump 9, second oxidation chamber 4 and third oxidation chamber 5 pass through 10 He of the first return pipe respectively
It is connected to inside second return pipe 11 and the first oxidation chamber 3, is respectively equipped on first return pipe 10 and the second return pipe 11
One back water pump 12 and the second back water pump 13 are equipped at the top of the tank body 1 and the water inlet pipe 14 that is connected to inside the first oxidation chamber 3, institute
The oxidant pipe 15 for being additionally provided at the top of tank body 1 and being connected to inside the first oxidation chamber 3 is stated, 1 lateral wall of tank body and third aoxidize
The corresponding position of chamber 5 is equipped with to be passed through bracket 17 and is equipped with its internal outlet pipe 16 being connected to, 3 inner top surface of the first oxidation chamber
Ultraviolet germicidal lamp 18 is provided with heating chamber 19 inside two partitions 2, is equipped with electric heating tube 20 in institute's heating chamber 19, it is described plus
Hot 19 bottom of chamber is equipped with and the hot-air channel 21 that is connected to inside the second oxidation chamber 4 and third oxidation chamber 5,1 lateral wall of tank body
It is equipped with the catalyst tank 22 that top is provided with opening close to the position at top, the catalyst tank 22 is divided by catalyst connecting tube 23
It is not connected to inside the second oxidation chamber 4 and third oxidation chamber 5, second oxidation chamber 4 and 5 inner sidewall of third oxidation chamber pass through axis
Set 24 is equipped with the stirring rod 25 being laterally arranged, and surrounds its axis on the stirring rod 25 and is equipped with array stirring sheet 26, the tank body 1
Lateral wall position corresponding with the second oxidation chamber 4 and third oxidation chamber 5, which is respectively equipped with, to be connect with stirring rod 25 and drives its rotation
Stirring motor 27.
In the present embodiment, first oxidation chamber 3, the second oxidation chamber 4 are consistent with 5 volume of third oxidation chamber.
In the present embodiment, filter assemblies 28 are equipped between the water inlet pipe 14 and tank body 1.
In the present embodiment, the filter assemblies 28 include shell 281, and 281 inside of shell is successively set along water inlet direction
There are the large granular impurity filter screen 282 being tightly connected with its inner sidewall and activated charcoal strainer 283.
In the present embodiment, 281 lateral wall of shell and large granular impurity filter screen 282 and activated charcoal strainer 283 are right
The position answered is provided with access hole, and the access hole, which is submitted, is connected to maintenance door 284.
In the present embodiment, sealing ring 285 is equipped between the maintenance door 284 and access hole.
In the present embodiment, the stirring sheet 26 includes the main leaf 261 connecting with stirring rod 25, and the main leaf 261 is separate to be stirred
One end end face for mixing bar 25 is provided with adjusting cavity 262 distributed along its length, slidably connects bluff bit in the adjusting cavity 262
263,261 top of main leaf position corresponding with adjusting cavity 262 is equipped with across 261 top of main leaf and locking main leaf 261 and pair
The lock-screw 264 of piece 263.
In the present apparatus, first connection pump the 8, second connection the 9, first back water pump 12 of pump and the second back water pump 13 are centrifugation
Pump, be fixed by devices such as connection frames, installation site determines according to actual conditions, can guarantee water flow it is smooth i.e.
It can.Ultraviolet germicidal lamp 18 and 20 power supply of electric heating tube are external, and connection type and driving method are the prior art, this Shen
Please in no longer individually explanation.In order to guarantee the service life of partition 2, heating chamber 19 and 21 inner sidewall of hot-air channel are equipped with high temperature resistant painting
Layer.Stirring motor 27 is direct current generator, and structure and driving method are the prior art, are no longer individually repeated in the application.
When the present apparatus aoxidizes, waste water enters the first oxidation chamber 3 from water inlet pipe 14, and during this, waste water passed through first
The large granular impurity filter screen 282 and activated charcoal strainer 283 for filtering component 28 carry out filtering one step ahead to waste water.Shell 281
The access hole that lateral wall is provided with is replaceable and cleaning filter screen, maintenance door 284 cooperate sealing ring 285 that can realize sealing.Waste water into
While entering the first oxidation, 03, H202,02 and air etc. is added from oxidant pipe 15 and is used as oxidant, ultraviolet germicidal lamp 18
Work, is aoxidized.Waste water after the completion of once oxidation passes sequentially through the first connecting tube 6 and the second connecting tube 7 enters the second oxygen
Change chamber 4 and the second oxidation chamber 4 carries out secondary oxidation and aoxidizes three times.During this, electric heating tube 20 works, to the second oxidation
Hot-air is injected in chamber 4 and third oxidation chamber 5;Meanwhile by catalyst connecting tube 23 to the second oxidation chamber 4 and third oxidation chamber
The catalyst such as 5 inside injection oxides, noble metal;Stirring motor 27 drives agitating shaft and stirring sheet 26 to work, and is sufficiently mixed
Waste water and catalyst guarantee the effect of oxidation.26 adjustable in length of stirring sheet, can be when dividing cavity, according to the shape of cavity
It is adjusted with size, to meet various sizes of tank body 1, without being individually customized for various sizes of tank body 1,
Cost can be reduced to a certain extent.Secondary oxidation and three times aoxidize after waste water can pass through the first return pipe 10 and the second return pipe
11 come back to the oxidation that the first oxidation chamber 3 is recycled, and fully ensure that the effect of oxidation.
Specific embodiment of the present utility model above described embodiment only expresses, the description thereof is more specific and detailed,
But it should not be understood as limiting the scope of the patent of the utility model.It should be pointed out that for the common of this field
For technical staff, without departing from the concept of the premise utility, various modifications and improvements can be made, these all belong to
In the protection scope of the utility model.
Claims (7)
1. a kind of organic wastewater oxidation treatment device, including tank body, it is characterised in that: the tank interior be amount of laterally located and with
The partition that tank body is tightly connected is divided into three the first oxidation chamber, the second oxidation chamber and third oxidation chamber independent cavitys, described
For first oxidation chamber by be connected to inside the first connecting tube and the second oxidation chamber, second oxidation chamber passes through the second connecting tube and the
It is connected to inside three oxidation chambers, the first connection pump and the second connection pump is respectively equipped in first connecting tube and the second connecting tube,
Second oxidation chamber and third oxidation chamber pass through respectively to be connected to inside the first return pipe and the second return pipe and the first oxidation chamber,
Be respectively equipped with the first back water pump and the second back water pump on first return pipe and the second return pipe, the top of the tank be equipped with
The water inlet pipe being connected to inside first oxidation chamber, the top of the tank are additionally provided with the oxidant pipe being connected to the first oxidation chamber inside,
Tank body lateral wall position corresponding with third oxidation chamber be equipped with its internal outlet pipe being connected to, in first oxidation chamber
Top surface passes through branch and is provided with ultraviolet germicidal lamp, and two diaphragm internals are provided with heating chamber, heats and intracavitary is equipped with electric heating
Pipe, the heating chamber bottom are equipped with the hot-air channel being connected to inside the second oxidation chamber and third oxidation chamber, the tank body outside
Wall is equipped with top close to the position at top and is provided with the catalyst tank of opening, the catalyst tank by catalyst connecting tube respectively with
It is connected to inside second oxidation chamber and third oxidation chamber, second oxidation chamber and third oxidation chamber inner sidewall pass through axle sleeve and be equipped with cross
To the stirring rod of setting, array stirring sheet, the tank body lateral wall and the second oxidation are equipped with around its axis on the stirring rod
Chamber and the corresponding position of third oxidation chamber are respectively equipped with the stirring motor for connecting with stirring rod and it being driven to rotate.
2. organic wastewater oxidation treatment device according to claim 1, it is characterised in that: first oxidation chamber, second
Oxidation chamber is consistent with third oxidation chamber volume.
3. organic wastewater oxidation treatment device according to claim 1, it is characterised in that: between the water inlet pipe and tank body
Equipped with filter assemblies.
4. organic wastewater oxidation treatment device according to claim 1, it is characterised in that: filter assemblies include shell, institute
It states enclosure interior and is successively arranged the large granular impurity filter screen being tightly connected with its inner sidewall and active carbon filtering along water inlet direction
Net.
5. organic wastewater oxidation treatment device according to claim 4, it is characterised in that: the hull outside wall and big
Grain impurity filtering net and the corresponding position of activated charcoal strainer are provided with access hole, and the access hole, which is submitted, is connected to maintenance door.
6. organic wastewater oxidation treatment device according to claim 5, it is characterised in that: the maintenance door and access hole it
Between be equipped with sealing ring.
7. organic wastewater oxidation treatment device according to claim 1, it is characterised in that: the stirring sheet includes and stirring
The main leaf of bar connection, the main leaf are provided with adjusting cavity distributed along its length, the tune far from one end end face of stirring rod
Save it is intracavitary slidably connect bluff bit, position corresponding with adjusting cavity is equipped at the top of main leaf and locks main leaf at the top of the main leaf
With the lock-screw of bluff bit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920054454.5U CN209602289U (en) | 2019-01-14 | 2019-01-14 | Organic wastewater oxidation treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920054454.5U CN209602289U (en) | 2019-01-14 | 2019-01-14 | Organic wastewater oxidation treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209602289U true CN209602289U (en) | 2019-11-08 |
Family
ID=68400561
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920054454.5U Expired - Fee Related CN209602289U (en) | 2019-01-14 | 2019-01-14 | Organic wastewater oxidation treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209602289U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111606368A (en) * | 2020-05-29 | 2020-09-01 | 安庆丰源化工有限公司 | Strong acid chemical wastewater treatment device |
-
2019
- 2019-01-14 CN CN201920054454.5U patent/CN209602289U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111606368A (en) * | 2020-05-29 | 2020-09-01 | 安庆丰源化工有限公司 | Strong acid chemical wastewater treatment device |
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Legal Events
| 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: 20191108 |