CN105749361B - A kind of self-operated type heat-exchanger rig condensate flow diverter - Google Patents
A kind of self-operated type heat-exchanger rig condensate flow diverter Download PDFInfo
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- CN105749361B CN105749361B CN201610080922.7A CN201610080922A CN105749361B CN 105749361 B CN105749361 B CN 105749361B CN 201610080922 A CN201610080922 A CN 201610080922A CN 105749361 B CN105749361 B CN 105749361B
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- negative pressure
- heat exchanger
- pressure generator
- pipeline
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Abstract
The invention discloses a kind of self-operated type heat-exchanger rig condensate flow diverter, including negative pressure generator, moisture separator and heat exchanger, the moisture separator is arranged in tank body, tank body is provided with liquid level display and discharge outlet, discharge outlet, in communication with cistern, is wherein provided with the first time-delay valve by pipeline at discharge outlet；Also connected on the negative pressure generator by pipeline with heat exchanger, wherein the connector on the pipeline connected close to negative pressure generator is provided with the second time-delay valve, the connector close to heat exchanger is equipped with control valve.The self-operated type heat-exchanger rig condensate flow diverter, negative pressure generator can realize promotion condensation water sport；Overall structure is simple, and operation is reasonable, greatlys save domestic water and the energy.
Description
Technical field
The present invention relates to flow diverter technical field, specially a kind of self-operated type heat-exchanger rig condensate flow diverter.
Background technology
Existing medical drainage device species is a lot, and what is had does not close with external environment, can cause environmental pollution.Typically draw
Stream device needs negative pressure source.Using very inconvenient；The flow diverter of existing heat-exchanger rig is required to waste substantial amounts of life use simultaneously
Water, it is impossible to which condensate causes unprovoked waste in automatic cycle heat-exchanger rig, therefore, this practicality can be certainly there is provided one kind
Power is by the condensate flow diverter in heat-exchanger rig.
The content of the invention
It is an object of the invention to provide a kind of self-operated type heat-exchanger rig condensate flow diverter, to solve above-mentioned background technology
The problem of middle proposition.
To achieve the above object, the present invention provides following technical scheme：A kind of self-operated type heat-exchanger rig condensate flow diverter,
Including negative pressure generator, moisture separator and heat exchanger, the moisture separator negative pressure generator is arranged in tank body, on tank body
Provided with liquid level display and discharge outlet, discharge outlet, in communication with cistern, is wherein provided with first and prolonged by pipeline at discharge outlet
When valve；Also connected on the negative pressure generator by pipeline with heat exchanger, wherein close to negative pressure generator on the pipeline connected
Connector is provided with the second time-delay valve, and the connector close to heat exchanger is equipped with control valve；The negative pressure generator passes through with vapour source
Pipeline communication, wherein the connector on the pipeline connected close to negative pressure generator is provided with the 3rd time-delay valve；The moisture separator
Gateway be both connected on the pipeline that negative pressure generator is connected with vapour source；The vapour source is also connected with heat exchanger.
It is preferred that, the heat exchanger sets three, and the outlet of heat exchanger is respectively mounted control valve.
It is preferred that, the outlet of the heat exchanger is also by tuber drainage to cistern.
Compared with prior art, the beneficial effects of the invention are as follows：This self-operated type heat-exchanger rig condensate flow diverter, works as liquid level
During the liquid level highest of display, by the 3rd time-delay valve delays time to control, by negative pressure generator by water vapour negative pressure to vapour source,
Second time-delay valve is closed and the first time-delay valve is opened, and the condensate separated in tank body by moisture separator is arranged by discharge outlet
Into cistern；When the liquid level of liquid level display is minimum, the 3rd delay valve breakdown and the second time-delay valve are closed, while by the
One delay valve breakdown, the hot gas in heat exchanger is pipelined in negative pressure generator, negative pressure generator can realize promotion
Condense water sport；Overall structure is simple, and operation is reasonable, greatlys save domestic water and the energy.
Brief description of the drawings
Fig. 1 is overall structure diagram of the invention.
In figure：1 negative pressure generator, 101 first time-delay valves, 102 second time-delay valves, 103 the 3rd time-delay valves, 11 discharge outlet, 2
Moisture separator, 3 liquid level displays, 4 heat exchangers, 41 control valves, 5 vapour sources；6 cisterns, 7 tank bodies.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation is described, it is clear that described embodiment is only a part of embodiment of the invention, rather than whole embodiments.It is based on
Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under the premise of creative work is not made
Embodiment, belongs to the scope of protection of the invention.
Referring to Fig. 1, the present invention provides a kind of technical scheme：A kind of self-operated type heat-exchanger rig condensate flow diverter, including
Negative pressure generator 1, moisture separator 2 and heat exchanger 4, the moisture separator 2 are arranged in tank body 7, and liquid level is provided with tank body 7
Display 3 and discharge outlet 11, discharge outlet 11, in communication with cistern 6, are wherein provided with first at discharge outlet 11 and prolonged by pipeline
When valve 101；Also connected on the negative pressure generator 1 by pipeline with heat exchanger 4, wherein occurring on the pipeline connected close to negative pressure
The connector of device 1 is provided with the second time-delay valve 102, and the connector close to heat exchanger 4 is equipped with control valve 41；The negative pressure generator
1 with vapour source 5 by pipeline communication, wherein on the pipeline connected close to negative pressure generator 1 connector be provided with the 3rd time-delay valve
103；The gateway of the moisture separator 2 is both connected on the pipeline that negative pressure generator 1 is connected with vapour source 5；The vapour source 5 is also
Connected with heat exchanger 4；The heat exchanger 4 sets three, and the outlet of heat exchanger 4 is respectively mounted control valve 41；The heat exchanger 4
Outlet also by tuber drainage to cistern 6.
When liquid level display 3 reaches highest order, the second time-delay valve 102 is closed, and rear 3rd time-delay valve 103 is opened, delay 5
After second, 101 first time-delay valves are opened, and realize that steam is separated, water is discharged into cistern 6.
When liquid level display 3 reaches lowest order, 101 first time-delay valves are closed, rear 3rd time-delay valve 103 is closed, the
Two time-delay valves 102 are opened.
Although an embodiment of the present invention has been shown and described, for the ordinary skill in the art, can be with
A variety of changes, modification can be carried out to these embodiments, replace without departing from the principles and spirit of the present invention by understanding
And modification, the scope of the present invention is defined by the appended.
Claims (3)
1. a kind of self-operated type heat-exchanger rig condensate flow diverter, including negative pressure generator (1), moisture separator (2) and heat exchanger
(4), it is characterised in that：The moisture separator (2) is arranged in tank body (7), tank body (7) provided with liquid level display (3) and
Discharge outlet (11), discharge outlet (11) is by pipeline in communication with cistern (6), and wherein discharge outlet (11) place is provided with the first delay
Valve (101)；Also connected on the negative pressure generator (1) by pipeline with heat exchanger (4), wherein close to negative pressure on the pipeline connected
The connector of generator (1) is provided with the second time-delay valve (102), and the connector close to heat exchanger (4) is equipped with control valve (41)；Institute
Negative pressure generator (1) and vapour source (5) are stated by pipeline communication, wherein on the pipeline connected close to negative pressure generator (1) connection
Mouth is provided with the 3rd time-delay valve (103)；The gateway of the moisture separator (2) is both connected to negative pressure generator (1) and vapour source (5)
On the pipeline of connection；The vapour source (5) also connects with heat exchanger (4).
2. a kind of self-operated type heat-exchanger rig condensate flow diverter according to claim 1, it is characterised in that：The heat exchanger
(4) three are set, and the outlet of heat exchanger (4) is respectively mounted control valve (41).
3. a kind of self-operated type heat-exchanger rig condensate flow diverter according to claim 1, it is characterised in that：The heat exchanger
(4) outlet is also by tuber drainage to cistern (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610080922.7A CN105749361B (en) | 2016-02-01 | 2016-02-01 | A kind of self-operated type heat-exchanger rig condensate flow diverter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610080922.7A CN105749361B (en) | 2016-02-01 | 2016-02-01 | A kind of self-operated type heat-exchanger rig condensate flow diverter |
Publications (2)
| Publication Number | Publication Date |
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| CN105749361A CN105749361A (en) | 2016-07-13 |
| CN105749361B true CN105749361B (en) | 2017-10-27 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201610080922.7A Active CN105749361B (en) | 2016-02-01 | 2016-02-01 | A kind of self-operated type heat-exchanger rig condensate flow diverter |
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Citations (6)
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| CN1098959A (en) * | 1994-05-21 | 1995-02-22 | 陈启松 | Energy saving evaporating apparatus |
| CN102829549A (en) * | 2012-08-24 | 2012-12-19 | 王凯一 | Heat resistance-free heat pipe heating furnace and heating method thereof |
| CN203615468U (en) * | 2013-11-14 | 2014-05-28 | 扬州斯大锅炉有限公司 | Steam negative pressure circulating heating system |
| CN203798185U (en) * | 2013-12-11 | 2014-08-27 | 张红生 | Novel shell and tube evaporative condenser |
| CN104848284A (en) * | 2015-04-09 | 2015-08-19 | 宜诺珐玛（天津）科技有限公司 | Steam condensation water heat recovery method and device |
| CN205322876U (en) * | 2016-02-01 | 2016-06-22 | 王保朋 | Formula of relying on oneself heat transfer device condensate water drainage ware |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08170807A (en) * | 1994-12-15 | 1996-07-02 | Tlv Co Ltd | Steam heating equipment |
| JP3507866B2 (en) * | 1995-01-13 | 2004-03-15 | 株式会社テイエルブイ | Steam heating device |
| JP4449204B2 (en) * | 2000-10-31 | 2010-04-14 | 栗田工業株式会社 | Boiler feed water treatment apparatus and boiler feed water treatment method |
| CN201353311Y (en) * | 2009-02-22 | 2009-12-02 | 陶旭东 | Multifunctional hyperthermic perfusion machine |
| US8403902B2 (en) * | 2010-05-18 | 2013-03-26 | Kci Licensing, Inc. | Reduced-pressure medical systems and methods employing a moisture processing device |
| CN101907294B (en) * | 2010-08-19 | 2012-07-04 | 西安交通大学 | Low-NOx combustion method of cyclone furnace and liquid slag waste heat recycling system of cyclone furnace |
-
2016
- 2016-02-01 CN CN201610080922.7A patent/CN105749361B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1098959A (en) * | 1994-05-21 | 1995-02-22 | 陈启松 | Energy saving evaporating apparatus |
| CN102829549A (en) * | 2012-08-24 | 2012-12-19 | 王凯一 | Heat resistance-free heat pipe heating furnace and heating method thereof |
| CN203615468U (en) * | 2013-11-14 | 2014-05-28 | 扬州斯大锅炉有限公司 | Steam negative pressure circulating heating system |
| CN203798185U (en) * | 2013-12-11 | 2014-08-27 | 张红生 | Novel shell and tube evaporative condenser |
| CN104848284A (en) * | 2015-04-09 | 2015-08-19 | 宜诺珐玛（天津）科技有限公司 | Steam condensation water heat recovery method and device |
| CN205322876U (en) * | 2016-02-01 | 2016-06-22 | 王保朋 | Formula of relying on oneself heat transfer device condensate water drainage ware |
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| Publication number | Publication date |
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| CN105749361A (en) | 2016-07-13 |
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| GR01 | Patent grant | ||
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| TR01 | Transfer of patent right |
Effective date of registration: 20210406 Address after: 252500 in the courtyard of Guanxian Ruixin Casting Co., Ltd., Xingye Road, Guanxian Economic Development Zone, Liaocheng City, Shandong Province Patentee after: Shandong Xinlin paper products Co.,Ltd. Address before: 252517 NO.686, Hanlu village, Lanwo Township, Guan County, Liaocheng City, Shandong Province Patentee before: Wang Baopeng |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: A condensate drainer for self operated heat exchanger Effective date of registration: 20220627 Granted publication date: 20171027 Pledgee: Bank of China Limited Guanxian sub branch Pledgor: Shandong Xinlin paper products Co.,Ltd. Registration number: Y2022980009098 |