CN206257651U - Oxygen-eliminating device discharged steam recovering device - Google Patents
Oxygen-eliminating device discharged steam recovering device Download PDFInfo
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- CN206257651U CN206257651U CN201621320174.7U CN201621320174U CN206257651U CN 206257651 U CN206257651 U CN 206257651U CN 201621320174 U CN201621320174 U CN 201621320174U CN 206257651 U CN206257651 U CN 206257651U
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- water
- oxygen
- eliminating device
- steam
- heat exchanger
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Abstract
The utility model is related to a kind of vapour-recovery unit, and in particular to a kind of oxygen-eliminating device discharged steam recovering device.Described oxygen-eliminating device discharged steam recovering device includes oxygen-eliminating device, oxygen-eliminating device top is respectively provided with steam inlet pipe and gland steam exhauster, gland steam exhauster is connected with heat exchanger shell pass entrance, heat exchanger shell pass outlet is connected with water tank, water tank top sets evacuated tube, water tank is also connected with condensated water recovering pump, and condensated water recovering pump is connected by pipeline with oxygen-eliminating device water pipe；Heat exchanger tube pass entrance is connected with deionized water pipeline, and heat exchanger tube pass outlet is connected with oxygen-eliminating device water pipe.The utility model simple structure, it is easy to operate, by using heat exchanger, water tank, condensated water recovering pump, outer row's steam having been reclaimed completely.Not only make use of the heat energy of outer row's steam, and be also fully utilized by outer row's steam condensation into water, also process water is heated, saved the energy.
Description
Technical field
The utility model is related to a kind of vapour-recovery unit, and in particular to a kind of oxygen-eliminating device discharged steam recovering device.
Background technology
Oxygen-eliminating device is one of key equipment that boiler and heating system are used.Oxygen-eliminating device typically uses thermal de-aeration,
Pressure of spraining can be usually produced in the heating process of desalted water, it is necessary to row's steam can just solve the above problems outward.And arranged outside oxygen-eliminating device
Vapor (steam) temperature is general at 115-125 DEG C or so, and quantity of steam about 0.25-0.35t/h causes the serious wave of heat energy and desalted water
Take.
Utility model content
According to deficiency of the prior art above, the technical problems to be solved in the utility model is：A kind of structure letter is provided
Oxygen-eliminating device discharged steam recovering device that is single, making full use of heat energy.
The utility model solves the technical scheme that its technical problem used：
Described oxygen-eliminating device discharged steam recovering device, including oxygen-eliminating device, oxygen-eliminating device top are respectively provided with steam inlet pipe and row
Steam pipe, gland steam exhauster is connected with heat exchanger shell pass entrance, and heat exchanger shell pass outlet is connected with water tank, and water tank top sets emptying
Pipe, water tank is also connected with condensated water recovering pump, and condensated water recovering pump is connected by pipeline with oxygen-eliminating device water pipe；Heat exchange
Device tube-side inlet is connected with deionized water pipeline, and heat exchanger tube pass outlet is connected with oxygen-eliminating device water pipe.
Described condensated water recovering pump is pneumatic condensated water recovering pump.The top of condensated water recovering pump sets source of the gas.
Gland steam exhauster is caused heat exchanger shell pass as thermal source, heat exchanger tube pass is connected on oxygen-eliminating device water pipe.Deoxygenation
Steam is arranged outside device by can completely condense into water after heat exchanger, water conservancy is flowed into water tank with potential difference, and water to be condensed reaches
When a certain amount of, condensed water is depressed into oxygen-eliminating device as device water by condensated water recovering pump using technique wind.In deionized water pipeline
Water enters oxygen-eliminating device water pipe after being exchanged heat by heat exchanger tube pass, has saved thermal source.
The utility model is had an advantageous effect in that：
The utility model simple structure, it is easy to operate, by using heat exchanger, water tank, condensated water recovering pump, returning completely
Outer row's steam is received.Not only make use of the heat energy of outer row's steam, and be also fully utilized by outer row's steam condensation into water, it is also right
Process water is heated, and has saved the energy.
Brief description of the drawings
Fig. 1 is the utility model structural representation；
In figure：1st, steam inlet pipe；2nd, gland steam exhauster；3rd, heat exchanger；4th, evacuated tube；5th, source of the gas；6th, condensated water recovering pump；7th, water storage
Tank；8th, deionized water pipeline；9th, oxygen-eliminating device water pipe；10th, oxygen-eliminating device.
Specific embodiment
Embodiment of the present utility model is described further below in conjunction with the accompanying drawings：
As shown in figure 1, described oxygen-eliminating device discharged steam recovering device, including oxygen-eliminating device 10, the top of oxygen-eliminating device 10 is respectively
Steam inlet pipe 1 and gland steam exhauster 2 are set, and gland steam exhauster 2 is connected with the shell side inlet of heat exchanger 3, the shell-side outlet of heat exchanger 3 and the phase of water tank 7
Even, the top of water tank 7 sets evacuated tube 4, and water tank 7 is also connected with condensated water recovering pump 6, and condensated water recovering pump 6 is by pipe
Road is connected with oxygen-eliminating device water pipe 9；The tube-side inlet of heat exchanger 3 is connected with deionized water pipeline 8, the tube side of heat exchanger 3 outlet with
Oxygen-eliminating device water pipe 9 is connected.Condensated water recovering pump 6 is pneumatic condensated water recovering pump, and its top sets source of the gas 5.
Gland steam exhauster 2 is caused the shell side of heat exchanger 3 as thermal source, the tube side of heat exchanger 3 is connected on oxygen-eliminating device water pipe 9.
The outer row's steam of oxygen-eliminating device 10 can completely condense into water after by heat exchanger 3, and water conservancy is flowed into water tank 7 with potential difference, treats cold
When solidifying water reaches a certain amount of, condensed water is depressed into oxygen-eliminating device 10 as device water by condensated water recovering pump 6 using technique wind.Deionization
Water in water lines 8 enters oxygen-eliminating device water pipe 9 after being exchanged heat by the tube side of heat exchanger 3, has saved thermal source.
The utility model simple structure, it is easy to operate, it is complete by using heat exchanger 3, water tank 7, condensated water recovering pump 6
Outer row's steam is reclaimed entirely.Not only make use of the heat energy of outer row's steam, and be also fully utilized by outer row's steam condensation into water,
Also it is that water in deionized water pipeline 8 is heated to process water, has saved the energy.
Claims (3)
1. a kind of oxygen-eliminating device discharged steam recovering device, including oxygen-eliminating device (10), it is characterised in that：Oxygen-eliminating device (10) top is respectively
Steam inlet pipe (1) and gland steam exhauster (2) is set, and gland steam exhauster (2) is connected with heat exchanger (3) shell side inlet, heat exchanger (3) shell-side outlet and
Water tank (7) is connected, and water tank (7) top sets evacuated tube (4), and water tank (7) is also connected with condensated water recovering pump (6),
Condensated water recovering pump (6) is connected by pipeline with oxygen-eliminating device water pipe (9)；Heat exchanger (3) tube-side inlet and deionization water pipe
Road (8) is connected, and the outlet of heat exchanger (3) tube side is connected with oxygen-eliminating device water pipe (9).
2. oxygen-eliminating device discharged steam recovering device according to claim 1, it is characterised in that：Condensated water recovering pump (6) is
Pneumatic condensated water recovering pump.
3. oxygen-eliminating device discharged steam recovering device according to claim 2, it is characterised in that：Condensated water recovering pump (6)
Top sets source of the gas (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621320174.7U CN206257651U (en) | 2016-12-02 | 2016-12-02 | Oxygen-eliminating device discharged steam recovering device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621320174.7U CN206257651U (en) | 2016-12-02 | 2016-12-02 | Oxygen-eliminating device discharged steam recovering device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206257651U true CN206257651U (en) | 2017-06-16 |
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ID=59027955
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621320174.7U Active CN206257651U (en) | 2016-12-02 | 2016-12-02 | Oxygen-eliminating device discharged steam recovering device |
Country Status (1)
| Country | Link |
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| CN (1) | CN206257651U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106439785A (en) * | 2016-12-02 | 2017-02-22 | 合力泰科技股份有限公司 | Deaerator exhaust steam recovery device |
-
2016
- 2016-12-02 CN CN201621320174.7U patent/CN206257651U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106439785A (en) * | 2016-12-02 | 2017-02-22 | 合力泰科技股份有限公司 | Deaerator exhaust steam recovery device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20171018 Address after: Yiyuan County Economic Development Zone 256100 Shandong city of Zibo province (county Yihe Road No. 1329) Patentee after: Shandong Heli Chemical Co., Ltd. Address before: 256100 Yiyuan City, Zibo Province, east wind road, No., No. 36 Patentee before: SHANDONG LIAHERD CHEMICAL INDUSTRY CO., LTD. |