CN208814685U - Improve the device of organic wastewater surface tension - Google Patents
Improve the device of organic wastewater surface tension Download PDFInfo
- Publication number
- CN208814685U CN208814685U CN201821263499.5U CN201821263499U CN208814685U CN 208814685 U CN208814685 U CN 208814685U CN 201821263499 U CN201821263499 U CN 201821263499U CN 208814685 U CN208814685 U CN 208814685U
- Authority
- CN
- China
- Prior art keywords
- reaction tower
- organic wastewater
- surface tension
- ozone generator
- ozone
- 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.)
- Active
Links
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model proposes a kind of devices for improving organic wastewater surface tension, it include: reaction tower, the reaction tower has inlet and outlet, and the water inlet is located at the lower part of the side wall of the reaction tower, and the water outlet is located at the top of the side wall of the reaction tower;Elevator pump, the output end of the elevator pump are connected with the water inlet;Ozone generator, the ozone generator are located at the outside of the reaction tower, and the output end of the ozone generator protrudes within the reaction tower.The device according to the present utility model for improving organic wastewater surface tension, organic wastewater is pre-processed using ozone, ozone is reacted with the hydrophilic radical of organic waste Organic substance in water compared with the conventional method, destroy the structure of hydrophilic radical, the surface tension of organic wastewater is improved with this, so more targetedly, effect is good and processing cost is lower.
Description
Technical field
The utility model relates to water-treatment technology fields, more particularly to a kind of dress for improving organic wastewater surface tension
It sets.
Background technique
Existing method improves the surface of organic wastewater with this by the organic matter in pretreatment removal organic wastewater
Power.That there are processing costs is excessively high for existing method, improves the problems such as surface tension effect is unobvious.
Utility model content
The utility model is intended to solve at least some of the technical problems in related technologies.
For this purpose, a purpose of the utility model is to propose a kind of device for improving organic wastewater surface tension, use
Ozone pre-processes organic wastewater, and ozone is reacted with the hydrophilic radical of organic waste Organic substance in water compared with the conventional method,
The structure for destroying hydrophilic radical, the surface tension of organic wastewater is improved with this, and so more targetedly, effect is good and is processed into
This is lower.
The device according to the present utility model for improving organic wastewater surface tension, comprising:
Reaction tower, the reaction tower have inlet and outlet, and the water inlet is located at the side wall of the reaction tower
Lower part, the water outlet are located at the top of the side wall of the reaction tower;
Elevator pump, the output end of the elevator pump are connected with the water inlet;
Ozone generator, the ozone generator are located at the outside of the reaction tower, the output end of the ozone generator
It protrudes within the reaction tower.
Advantageously, the device of the raising organic wastewater surface tension further includes ozonation aerated head, described ozonation aerated
Head is located in the reaction tower and is connected with the output end of the ozone generator.
Advantageously, the device of the raising organic wastewater surface tension further includes palladium catalyst, and the palladium catalyst is set
The upper surface of in the reaction tower and be located at the ozonation aerated head.
Advantageously, the reaction tower is cylindrical reaction tower.
Advantageously, the ozonation aerated head includes aeration disk compatible with the reaction tower and arranged for interval in institute
Multiple aeration nozzles on aeration disk are stated, multiple aeration nozzles are connected with the output end of the ozone generator.
Advantageously, when work, the minimum volume ratio of organic wastewater and ozone is 1:10~1:20.
Advantageously, when work, the reaction temperature of organic wastewater and ozone is >=10 DEG C.
Advantageously, when work, the reaction time of organic wastewater and ozone is 20min~40min.
The additional aspect and advantage of the utility model will be set forth in part in the description, partially will be from following description
In become obvious, or recognized by the practice of the utility model.
Detailed description of the invention
Fig. 1 is the schematic diagram according to the device of the raising organic wastewater surface tension of the utility model one embodiment.
Specific embodiment
The embodiments of the present invention are described below in detail, examples of the embodiments are shown in the accompanying drawings, wherein from beginning
Same or similar element or element with the same or similar functions are indicated to same or similar label eventually.Below by ginseng
The embodiment for examining attached drawing description is exemplary, it is intended to for explaining the utility model, and should not be understood as to the utility model
Limitation.
Below with reference to the accompanying drawings come be described in detail it is according to the present utility model improve organic wastewater surface tension device.
As shown in Figure 1, the device according to the present utility model for improving organic wastewater surface tension, comprising: reaction tower 100,
Elevator pump 200, ozone generator 300.
Specifically, reaction tower 100 has water inlet 110 and water outlet 120, water inlet 110 is located at the side of reaction tower 100
The lower part of wall, water outlet 120 are located at the top of the side wall of reaction tower 100.
The output end of elevator pump 200 is connected with water inlet 110, for conveying organic wastewater into reaction tower 100.
Ozone generator 300 is located at the outside of reaction tower 100, the output end of ozone generator 300 protrude into reaction tower 100 it
It is interior, for providing the ozone reacted with organic wastewater into reaction tower 100.
The device according to the present utility model for improving organic wastewater surface tension, locates organic wastewater using ozone in advance
Reason, ozone is reacted with the hydrophilic radical of organic waste Organic substance in water compared with the conventional method, the structure of hydrophilic radical is destroyed, with this
The surface tension of organic wastewater is improved, so more targetedly, effect is good and processing cost is lower.
Advantageously, the also ozonation aerated head 400 of device of the raising organic wastewater surface tension, ozonation aerated head 400
It is located in reaction tower 100 and is connected with the output end of ozone generator 300.Ozonation aerated head 400 can be by ozone gas rheology as a result,
At tiny bubble, can sufficiently be reacted with organic wastewater.
Further, the device of the raising organic wastewater surface tension further includes palladium catalyst 500, palladium catalyst
500 are located in reaction tower 100 and positioned at the upper surface of ozonation aerated head 400.The selectivity for improving reaction as a result, make ozone with
The hydrophilic radical of organic waste Organic substance in water is preferably reacted, and the structure of hydrophilic radical is preferably destroyed.
Advantageously, reaction tower 100 is cylindrical reaction tower.Further, ozonation aerated head 400 includes and reaction tower 100
The multiple aeration nozzle (not shown) of compatible aeration disk (not shown) and arranged for interval on the aeration disk are more
A aeration nozzle is connected with the output end of ozone generator 300.Thus, it is possible to further fill ozone with organic wastewater
Divide reaction.
Advantageously, when work, the minimum volume ratio of organic wastewater and ozone is 1:10~1:20.Organic wastewater and ozone
Reaction temperature is >=10 DEG C.The reaction time of organic wastewater and ozone is 20min~40min.
In other words, from the lower part of reaction tower 100 into such as, ozone is become by ozonation aerated head 400 for organic wastewater and ozone
The bubble and organic wastewater of very little are sufficiently mixed, and the volume ratio minimum of organic wastewater and ozone can reach 1:10~1:20.Then
Sufficiently reacted under the action of palladium catalyst, since palladium catalyst greatly improves reaction rate so that the reaction 10 DEG C with
On can have good effect.Reaction time between 20min to 40min, when reacted between when reaching 40min, organic wastewater
Surface tension after reacted almost can reach 70mN/m close to the surface tension numerical value of pure water.
The device according to the present utility model for improving organic wastewater surface tension carries out organic wastewater by using ozone
Processing, while being catalyzed using palladium catalyst, the selectivity of reaction is improved, the method compared with the conventional method urge in palladium by ozone
It is reacted under the action of agent with the hydrophilic radical of organic waste Organic substance in water, destroys the structure of hydrophilic radical, improved with this
The surface tension of machine waste water, so more targetedly, effect is good and processing cost is lower.
In the description of the present invention, it should be understood that term " center ", " longitudinal direction ", " transverse direction ", " length ", " width
Degree ", " thickness ", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom" "inner", "outside", " suitable
The orientation or positional relationship of the instructions such as hour hands ", " counterclockwise ", " axial direction ", " radial direction ", " circumferential direction " is orientation based on the figure
Or positional relationship, be merely for convenience of describing the present invention and simplifying the description, rather than the device of indication or suggestion meaning or
Element must have a particular orientation, be constructed and operated in a specific orientation, therefore should not be understood as the limit to the utility model
System.
In addition, term " first ", " second " are used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance
Or implicitly indicate the quantity of indicated technical characteristic.Define " first " as a result, the feature of " second " can be expressed or
Implicitly include one or more of the features.The meaning of " plurality " is two or more in the description of the present invention, remove
It is non-separately to have clearly specific restriction.
In the present invention unless specifically defined or limited otherwise, term " installation ", " connected ", " connection ", " Gu
It is fixed " etc. terms shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integral;It can be
Mechanical connection, is also possible to be electrically connected;It can be directly connected, two can also be can be indirectly connected through an intermediary
The interaction relationship of connection or two elements inside element.It for the ordinary skill in the art, can basis
Concrete condition understands the concrete meaning of above-mentioned term in the present invention.
In the present invention unless specifically defined or limited otherwise, fisrt feature is in the second feature " on " or " down "
It can be that the first and second features directly contact or the first and second features are by intermediary mediate contact.Moreover, first is special
Sign can be fisrt feature above the second feature " above ", " above " and " above " and be directly above or diagonally above the second feature, or only
Indicate that first feature horizontal height is higher than second feature.Fisrt feature under the second feature " below ", " below " and " below " can be with
It is that fisrt feature is directly under or diagonally below the second feature, or is merely representative of first feature horizontal height less than second feature.
In the description of this specification, reference term " one embodiment ", " some embodiments ", " example ", " specifically show
The description of example " or " some examples " etc. means specific features, structure, material or spy described in conjunction with this embodiment or example
Point is contained at least one embodiment or example of the utility model.In the present specification, to the schematic table of above-mentioned term
It states and is necessarily directed to identical embodiment or example.Moreover, particular features, structures, materials, or characteristics described can be with
It can be combined in any suitable manner in any one or more of the embodiments or examples.In addition, without conflicting with each other, this field
Technical staff can by the feature of different embodiments or examples described in this specification and different embodiments or examples into
Row combination and combination.
Although the embodiments of the present invention have been shown and described above, it is to be understood that above-described embodiment is
Illustratively, it should not be understood as limiting the present invention, those skilled in the art are in the scope of the utility model
It inside makes changes, modifications, substitutions and variations to the above described embodiments, each falls within the protection scope of the utility model.
Claims (5)
1. a kind of device for improving organic wastewater surface tension characterized by comprising
Reaction tower, the reaction tower have inlet and outlet, and the water inlet is located at the lower part of the side wall of the reaction tower,
The water outlet is located at the top of the side wall of the reaction tower;
Elevator pump, the output end of the elevator pump are connected with the water inlet;
Ozone generator, the ozone generator are located at the outside of the reaction tower, and the output end of the ozone generator protrudes into
Within the reaction tower.
2. the device according to claim 1 for improving organic wastewater surface tension, which is characterized in that further include ozonation aerated
Head, the ozonation aerated head are located in the reaction tower and are connected with the output end of the ozone generator.
3. the device according to claim 2 for improving organic wastewater surface tension, which is characterized in that further include palladium chtalyst
Agent, the palladium catalyst are located in the reaction tower and positioned at the upper surface of described ozonation aerated head.
4. the device according to claim 2 for improving organic wastewater surface tension, which is characterized in that the reaction tower is circle
Cylindricality reaction tower.
5. the device according to claim 4 for improving organic wastewater surface tension, which is characterized in that the ozonation aerated head
Multiple aeration nozzles including aeration disk compatible with the reaction tower and arranged for interval on the aeration disk are more
A aeration nozzle is connected with the output end of the ozone generator.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201821263499.5U CN208814685U (en) | 2018-08-01 | 2018-08-01 | Improve the device of organic wastewater surface tension |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201821263499.5U CN208814685U (en) | 2018-08-01 | 2018-08-01 | Improve the device of organic wastewater surface tension |
Publications (1)
Publication Number | Publication Date |
---|---|
CN208814685U true CN208814685U (en) | 2019-05-03 |
Family
ID=66272519
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201821263499.5U Active CN208814685U (en) | 2018-08-01 | 2018-08-01 | Improve the device of organic wastewater surface tension |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN208814685U (en) |
-
2018
- 2018-08-01 CN CN201821263499.5U patent/CN208814685U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
RU2604371C2 (en) | Methods and apparatus for enhanced gas distribution | |
US5314076A (en) | Installation for the mixing of two fluid phases by mechanical stirring, notably for the treatment of water by transfer of oxidizing gas, and use of such an installation | |
US8808550B2 (en) | Apparatus and method for dissolution of ozone in water and catalytic oxidation | |
KR101697526B1 (en) | high efficient ozone-water treatment system | |
JP4128890B2 (en) | Gas-liquid mixing reaction method and gas-liquid mixing reaction apparatus | |
CN206424892U (en) | gas-liquid stirring device | |
CN208814685U (en) | Improve the device of organic wastewater surface tension | |
CN106430523B (en) | Organic wastewater bio-chemical effluent ozone advanced treatment apparatus and processing method | |
CN109019824A (en) | A kind of efficiently catalyzing and oxidizing organic wastewater treating system | |
CN208482466U (en) | A kind of mixing reaction kettle for water treatment agent production | |
CN101508502B (en) | Gas-liquid photocatalysis oxidation reaction apparatus | |
CN205556261U (en) | Aeration equipment is cuted to whirl | |
CN201530748U (en) | Gas blasting movable injection aerator | |
CN103011377A (en) | Enhanced oxidization device and method used for organic wastewater treatment | |
KR101634667B1 (en) | Apparatus for generating high density ozone gas dissolved water using electromagnetic field | |
CN201362609Y (en) | Gas-liquid photocatalytic oxidation reaction device | |
KR102207979B1 (en) | Bubble Generator Integrated with Multistage Pump | |
KR100445301B1 (en) | Ozone Sterilization Method and Device for Water Supply Drainage | |
CN218810779U (en) | Baffle plate type multistage heterogeneous high-efficiency ozone catalytic device | |
KR100968752B1 (en) | Multi aeration-mixing machine | |
CN203200065U (en) | Intensified oxidization device applied to organic wastewater treatment | |
CN104891706A (en) | Ozone oxidation wastewater treatment device | |
CN212476243U (en) | Ozone circulation oxidation equipment and multistage ozone circulation oxidation equipment thereof | |
CN218688065U (en) | Be used for high-efficient deacidification defogging spray column of exhaust-gas treatment | |
CN207002359U (en) | A kind of efficiently PAC chemicals dosing plants |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |