CN209567905U - Saline water treatment device is used in soda ash processing - Google Patents
Saline water treatment device is used in soda ash processing Download PDFInfo
- Publication number
- CN209567905U CN209567905U CN201920128721.9U CN201920128721U CN209567905U CN 209567905 U CN209567905 U CN 209567905U CN 201920128721 U CN201920128721 U CN 201920128721U CN 209567905 U CN209567905 U CN 209567905U
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- water
- tank
- venturi tube
- oxidation
- soda ash
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- Treatment Of Water By Oxidation Or Reduction (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The utility model relates to a kind of soda ash processing saline water treatment devices, including air compressor, ozone generator, water supply pump, Venturi tube, oxidation tank and decompose tank, the connection of the air inlet of the gas outlet and ozone generator of the air compressor, the gas outlet of the ozone generator and the air inlet of Venturi tube connect, the water outlet of the water supply pump and the water inlet of Venturi tube connect, the water outlet of the Venturi tube and the water inlet of oxidation tank connect, the water outlet of the oxidation tank is connect with the water inlet for decomposing tank, and active carbon is filled in the decomposition tank.The present apparatus is sufficiently mixed ozone with salt water using Venturi tube, the larger molecular organics oxygenolysis in water can be small organic molecule by ozone in oxidation tank, it is then to utilize remaining ozone under conditions of using active carbon as catalyst in decomposing tank, to the further oxygenolysis of organic matter difficult to degrade in water, to guarantee the mesohalobic exhaustive oxidation of soda ash process, the processing quality of water process is improved.
Description
Technical field
The utility model uses saline water treatment device more particularly to a kind of processing of soda ash.
Background technique
China's soda ash total output in 2016 is 2588.3 ten thousand tons, and soda manufacture technique is formd is with ammonia-soda process, union soda
Main, supplemented by natural alkaline process production pattern, wherein ammonia-soda process yield is slightly larger than union soda, accounts for about the half of total output, i.e., 2016
The soda ash of year ammonia-soda process close to 13,000,000 tons, ammonia-soda process soda ash is with a long history, technology maturation, can be large-scale continuous
Production, the features such as automatic and mechanical degree is high, product purity is high, high-quality, have huge in China coast and Salt Lake Area
Advantage, but waste liquid, waste residue, the CO 2 waste gas of enormous amount that ammonia-soda process soda ash can generate, not only cause huge
Resource and energy waste, while also bringing serious hidden danger and pressure to environment, this is the development of ammonia-soda process soda ash
The major reason seriously restricted.
Utility model content
The purpose of this utility model is to provide a kind of good soda ash processing saline water treatment devices of oxidation effectiveness.
The technical solution adopted in the utility model are as follows: soda ash processing saline water treatment device, including air compressor, ozone
Generator, water supply pump, Venturi tube, oxidation tank and decomposition tank, the gas outlet of the air compressor and the air inlet of ozone generator
The connection of mouth, the gas outlet of the ozone generator and the air inlet of Venturi tube connect, the water outlet of the water supply pump and Wen
The water inlet of pipe connects, and the water outlet of the Venturi tube and the water inlet of oxidation tank connect, the water outlet of the oxidation tank with point
The water inlet connection of tank is solved, is filled with active carbon in the decomposition tank.
Soda ash processing saline water treatment device as described above further illustrates to be the water inlet setting of the oxidation tank
In the bottom of oxidation tank, the top of oxidation tank is arranged in the water outlet of the oxidation tank.
Soda ash processing saline water treatment device as described above, further illustrates to be to be equipped at intervals in the oxidation tank more
A disturbance plate.
Soda ash processing saline water treatment device as described above further illustrates to be the water inlet setting for decomposing tank
In the bottom for decomposing tank, the top for decomposing tank is arranged in the water outlet for decomposing tank.
The beneficial effects of the utility model are: the present apparatus is sufficiently mixed ozone with salt water using Venturi tube, in oxidation tank
Larger molecular organics oxygenolysis in water can be small organic molecule by interior ozone, be then using remaining smelly in decomposing tank
Oxygen is under conditions of using active carbon as catalyst, to the further oxygenolysis of organic matter difficult to degrade in water, to guarantee soda ash
The mesohalobic exhaustive oxidation of process improves the processing quality of water process, has good market prospects and promotional value.
Detailed description of the invention
FIG. 1 is a schematic structural view of the utility model.
In figure: 1, air compressor；2, ozone generator；3, water supply pump；4, Venturi tube；5, oxidation tank；6, tank is decomposed；7,
Active carbon；8, disturbance plate.
Specific embodiment
The utility model embodiment is further elaborated with reference to the accompanying drawing.
As shown in Figure 1, a kind of soda ash processing saline water treatment device provided in this embodiment, including it is air compressor 1, smelly
Oxygen Generator 2, water supply pump 3, Venturi tube 4, oxidation tank 5 and decomposition tank 6, the gas outlet of the air compressor 1 and ozone occur
The connection of the air inlet of device 2, the air compressor 1 is for generating compressed air, and specific structure and working principle are here not
It elaborates, the compressed air that air compressor 1 generates is transported in ozone generator 2, and the ozone generator 2 is for producing
Raw ozone.
The gas outlet of the ozone generator 2 is connect with the air inlet of Venturi tube 4, the water outlet and text of the water supply pump 3
The water inlet of family name's pipe 4 connects, and the water outlet of the Venturi tube 4 is connect with the water inlet of oxidation tank 5, the Venturi tube 4, the text
Family name's pipe 4 is the abbreviation of Venturi tube, and the principle of Venturi effect is then when air blows over obstacle, in the leeward of obstacle
Top near ports air pressure is relatively low, to generate suction-operated and lead to the flowing of air, be exactly air-flow from the coarse to fine,
To accelerate gas flow rate, gas is made to form a low-pressure area in the outer ring that Venturi tube 4 exports, to keep ozone and salt water sufficiently mixed
It closes.
The water outlet of the oxidation tank 5 is connect with the water inlet for decomposing tank 6, and active carbon 7 is filled in the decomposition tank 6.
The larger molecular organics oxygenolysis in water can be small organic molecule by ozone in oxidation tank 5, be then benefit in decomposing tank 6
With remaining ozone under conditions of using active carbon as catalyst, to the further oxygenolysis of organic matter difficult to degrade in water, from
And guarantee the mesohalobic exhaustive oxidation of soda ash process, improve the processing quality of water process, have good market prospects and
Promotional value.
Preferably, guarantee the oxidation quality of salt water to improve the oxidability of oxidation tank 5, it can be by the oxidation
The bottom of oxidation tank 5 is arranged in the water inlet of tank 5, and the top of oxidation tank 5 is arranged in the water outlet of the oxidation tank 5, further
, in order to increase the oxidative decomposition capacity of ozone and salt water in oxidation tank 5, can be equipped at intervals in the oxidation tank 5 more
A disturbance plate 8, this is a kind of preferred embodiment certainly.
Similarly, in order to improve the oxidability for decomposing tank 6, guarantee the oxidation quality of salt water, tank 6 can be decomposed by described
The bottom for decomposing tank 6 is arranged in water inlet, and the top for decomposing tank 6 is arranged in the water outlet for decomposing tank 6.
The utility model is not limited to examples detailed above, in claims limited range of the utility model, this
The various deformations or amendments that field technical staff can make without creative work are protected by this patent.
Claims (4)
1. soda ash processing saline water treatment device, it is characterised in that: including air compressor, ozone generator, water supply pump, Wen
Pipe, oxidation tank and decomposition tank, the connection of the air inlet of the gas outlet and ozone generator of the air compressor, the ozone hair
The gas outlet of raw device and the air inlet of Venturi tube connect, and the water outlet of the water supply pump and the water inlet of Venturi tube connect, described
The water outlet of Venturi tube and the water inlet of oxidation tank connect, and the water outlet of the oxidation tank is connect with the water inlet for decomposing tank, institute
It states and decomposes in tank filled with active carbon.
2. soda ash processing saline water treatment device according to claim 1, it is characterised in that: the water inlet of the oxidation tank
The bottom of oxidation tank is set, and the top of oxidation tank is arranged in the water outlet of the oxidation tank.
3. soda ash processing saline water treatment device according to claim 2, it is characterised in that: interval is set in the oxidation tank
There are multiple disturbance plates.
4. soda ash processing saline water treatment device according to claim 1, it is characterised in that: the water inlet for decomposing tank
The bottom for decomposing tank is set, and the top for decomposing tank is arranged in the water outlet for decomposing tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920128721.9U CN209567905U (en) | 2019-01-25 | 2019-01-25 | Saline water treatment device is used in soda ash processing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920128721.9U CN209567905U (en) | 2019-01-25 | 2019-01-25 | Saline water treatment device is used in soda ash processing |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209567905U true CN209567905U (en) | 2019-11-01 |
Family
ID=68332723
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920128721.9U Expired - Fee Related CN209567905U (en) | 2019-01-25 | 2019-01-25 | Saline water treatment device is used in soda ash processing |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209567905U (en) |
-
2019
- 2019-01-25 CN CN201920128721.9U patent/CN209567905U/en not_active Expired - Fee Related
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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 |
Granted publication date: 20191101 Termination date: 20220125 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |