CN202850090U - Deoxidization and water supply device - Google Patents
Deoxidization and water supply device Download PDFInfo
- Publication number
- CN202850090U CN202850090U CN 201220467564 CN201220467564U CN202850090U CN 202850090 U CN202850090 U CN 202850090U CN 201220467564 CN201220467564 CN 201220467564 CN 201220467564 U CN201220467564 U CN 201220467564U CN 202850090 U CN202850090 U CN 202850090U
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- Prior art keywords
- deoxidization
- water tank
- pipeline
- deoxygenation
- water
- 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.)
- Expired - Fee Related
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- Physical Water Treatments (AREA)
Abstract
The utility model belongs to the technical field of chemical equipment, in particular to a deoxidization and water supply device. The deoxidization and water supply device comprises a deaerator which comprises a deoxidization tower head placed on the upper portion of the deaerator and a deoxidization water tank placed on the lower portion of the deaerator. The deoxidization and water supply device further comprises a spare water tank. The inlet of the spare water tank is communicated to the bottom of the deoxidization tower head through a pipeline. A pipeline connected to the outlet of the spare water tank is joined with a pipeline connected to an outlet of the deoxidization water tank; a valve is placed on a pipeline connected to the outlet of a spare water tank. The deoxidization and water supply device is simple in structure. By adopting the spare water tank and pipelines of the spare water tank, a system can continue to operate when the deaerator is maintained because of a breakdown, and production progress is guaranteed.
Description
Technical field
The utility model belongs to technical field of chemical, relates in particular to a kind of deoxygenation water supply installation.
Background technology
At chemical field, water has a wide range of applications as a kind of raw materials for production and heat-conducting medium.Generally, all dissolve to some extent aerobic in the water, these oxygen exist as impurity.Especially, when the water that contains aerobic flows through various pipelines and equipment, can produce the oxide etch effect to it, affect the application life of equipment and pipeline.Therefore, water needs to carry out first deoxygenation before in entering above-mentioned pipeline and equipment and processes.In the prior art, generally adopt oxygen-eliminating device to process.Water enters in the deoxygenation tower head of oxygen-eliminating device after series of steps is processed deoxidation, and the water of low oxygen content enters in the deoxygenation water tank of below, is pumped in the e-quipment and pipe by water pump again.And generally, oxygen-eliminating device is processed water later and is all being played the part of important role, as condensed water etc.; if breaking down, oxygen-eliminating device cuts off the water supply; then whole system just must be shut down within a few minutes, and the workman that needs repairing fixes a breakdown and just can reproduce afterwards, and is larger on the production process impact.
The utility model content
The utility model provides the deoxygenation water supply installation of a kind of solution simple in structure, effective in oxygen-eliminating device maintenance period damp production problem for solving the technical problem that exists in the known technology.
The technical scheme that the utility model is taked for the technical problem that exists in the solution known technology is: the deoxygenation water supply installation comprises oxygen-eliminating device, described oxygen-eliminating device comprises superposed deoxygenation tower head and is positioned at the deoxygenation water tank of bottom, also comprise buffer tank, its entrance by pipeline connection to the bottom of described deoxygenation tower head, the pipeline that is connected to its outlet converges with the pipeline that is connected to described deoxygenation water tank outlet; On the pipeline that is connected to described buffer tank outlet, also be provided with valve.
Its advantage and good effect are: owing to adopted above-mentioned design, the utility model is simple in structure.On original oxygen-eliminating device and pipeline thereof and connect a buffer tank pipeline, internal reservoir is through the water of deoxygenation tower head deoxidation, when oxygen-eliminating device breaks down when needing repairing, can solve the problem that production process be forced to interrupt by opening the buffer tank pipeline.Buffer tank is that service worker has won the regular hour, fix in during this period oxygen-eliminating device then production process almost do not receive impact.
Description of drawings
Fig. 1 is structural representation of the present utility model.
Among the figure: 1, flow pipe; 2, deoxygenation tower head; 3, deoxygenation water tank; 4, buffer tank; 5, valve.
The specific embodiment
For further understanding summary of the invention of the present utility model, Characteristic, hereby exemplify following examples, and cooperate accompanying drawing to be described in detail as follows:
See also Fig. 1, the utility model comprises oxygen-eliminating device, and it is made of superposed deoxygenation tower head 2 and the deoxygenation water tank 3 that is positioned at the bottom, and the sidewall of deoxygenation tower head 2 upper ends is provided with the water inlet that is connected to flow pipe 1, and the top of deoxygenation tower head 2 is provided with exhaust opening.Water after 2 deoxidations of deoxygenation tower head enters in the deoxygenation water tank 3 of below, enters postorder equipment or pipeline again.
In this example, on the basis of original system and connect buffer tank 4 and pipeline thereof.The water inlet of buffer tank 4 is by the bottom of pipeline connection to deoxygenation tower head 2, and the water after deoxidation can enter the buffer tank 4 from this pipeline.The pipeline that is connected to buffer tank 4 delivery ports converges with the pipeline that is connected to deoxygenation water tank 3 delivery ports, and the end is provided with for the flange that connects water pump.On the pipeline that is connected to buffer tank 4 delivery ports, also be provided with valve 5.
During startup, source water is entered by flow pipe 1 and carries out deoxidation treatment in the deoxygenation tower head 2, enters in the buffer tank 4 along pipeline afterwards until fill, and after this water after the deoxidation enters in the deoxygenation water tank 3.In the situation that valve 5 turn-offs, water pump is pumped the water in the deoxygenation water tank 3 to the equipment or pipeline of postorder.Need repairing when oxygen-eliminating device breaks down, only need cut off source water and open valve 5, the water that wherein stores is emitted.
Claims (1)
1. deoxygenation water supply installation, comprise oxygen-eliminating device, described oxygen-eliminating device comprises superposed deoxygenation tower head (2) and is positioned at the deoxygenation water tank (3) of bottom, it is characterized in that: also comprise buffer tank (4), its entrance by pipeline connection to the bottom of described deoxygenation tower head (2), the pipeline that is connected to its outlet converges with the pipeline that is connected to described deoxygenation water tank (3) outlet; On the pipeline that is connected to described buffer tank (4) outlet, also be provided with valve (5).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220467564 CN202850090U (en) | 2012-09-13 | 2012-09-13 | Deoxidization and water supply device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220467564 CN202850090U (en) | 2012-09-13 | 2012-09-13 | Deoxidization and water supply device |
Publications (1)
Publication Number | Publication Date |
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CN202850090U true CN202850090U (en) | 2013-04-03 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 201220467564 Expired - Fee Related CN202850090U (en) | 2012-09-13 | 2012-09-13 | Deoxidization and water supply device |
Country Status (1)
Country | Link |
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CN (1) | CN202850090U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108709953A (en) * | 2018-04-13 | 2018-10-26 | 北京师范大学 | A kind of simulator of belt of phreatic fluctuation |
CN111985652A (en) * | 2019-05-23 | 2020-11-24 | 中国石油天然气股份有限公司 | Method and device for determining emergency duration and storage medium |
-
2012
- 2012-09-13 CN CN 201220467564 patent/CN202850090U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108709953A (en) * | 2018-04-13 | 2018-10-26 | 北京师范大学 | A kind of simulator of belt of phreatic fluctuation |
CN111985652A (en) * | 2019-05-23 | 2020-11-24 | 中国石油天然气股份有限公司 | Method and device for determining emergency duration and storage medium |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130403 Termination date: 20180913 |
|
CF01 | Termination of patent right due to non-payment of annual fee |