CN102418953A - Household negative pressure steam heating system - Google Patents
Household negative pressure steam heating system Download PDFInfo
- Publication number
- CN102418953A CN102418953A CN2011104087462A CN201110408746A CN102418953A CN 102418953 A CN102418953 A CN 102418953A CN 2011104087462 A CN2011104087462 A CN 2011104087462A CN 201110408746 A CN201110408746 A CN 201110408746A CN 102418953 A CN102418953 A CN 102418953A
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- steam
- heat exchanger
- outlet
- liquid separator
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- 238000010438 heat treatment Methods 0.000 title claims abstract description 23
- 239000007788 liquid Substances 0.000 claims abstract description 61
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 40
- 238000002485 combustion reaction Methods 0.000 claims description 17
- 230000008676 import Effects 0.000 claims description 12
- 230000005484 gravity Effects 0.000 claims description 6
- 229910000831 Steel Inorganic materials 0.000 claims description 3
- 230000000694 effects Effects 0.000 claims description 3
- 238000002347 injection Methods 0.000 claims description 3
- 239000007924 injection Substances 0.000 claims description 3
- 239000007791 liquid phase Substances 0.000 claims description 3
- 239000010959 steel Substances 0.000 claims description 3
- 230000009471 action Effects 0.000 abstract description 6
- 238000009833 condensation Methods 0.000 abstract description 3
- 230000005494 condensation Effects 0.000 abstract description 3
- 239000000446 fuel Substances 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 6
- 238000005265 energy consumption Methods 0.000 description 3
- 239000012071 phase Substances 0.000 description 3
- 238000005485 electric heating Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 238000009835 boiling Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 230000001131 transforming effect Effects 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/12—Hot water central heating systems using heat pumps
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- Steam Or Hot-Water Central Heating Systems (AREA)
Abstract
The invention discloses a household negative pressure steam heating system which comprises a gas heater, a bubble pump lifting pipe, a gas-liquid separator, a heat exchanger, a liquid collector, a U-shaped bent pipe, an electric control valve and a steam ejector. The invention provides working medium circulating power by utilizing the thermosiphon action of the bubble pump riser, saves a circulating pump which is necessary to be arranged in the existing household hot water heating system, and saves electric energy; the water is vaporized under the condition of vacuum and lower temperature to increase the heat exchange temperature difference of the gas heater, improve the efficiency of the gas heater and save fuel; the steam-air heat exchanger has the advantages that the steam phase change condensation heat exchange is utilized to improve the efficiency of the steam-air heat exchanger, reduce the heat exchange area and realize the miniaturization of the steam-air heat exchanger; the steam ejector replaces a vacuum pump to ensure stable and reliable operation of the system. Compared with a household hot water heating system, the system has no moving parts, consumes no electric energy, saves gas and has wide application prospect.
Description
Technical field
The present invention relates to steam heating system, relate in particular to a kind of family formula negative pressure steam heating system.
Background technology
What Xia Redong cryogenic region dwelling house mainly adopted is the electric heating form, its shortcoming be not energy-conservation and comfortableness poor.In order to improve the indoor thermal comfort in winter, the most common way is to replace the electric heating mode with steam heating mode or hot water heating mode.The working media of steam heating mode is a water vapour; The water vapour specific latent heat is saved conveying energy consumption greatly; And water vapour phase-change heat-exchange and reduce radiator area; But traditional steam heating system has characteristics such as vapor (steam) temperature height, saturation pressure height, energy quality height, has problems such as energy consumption height, potential safety hazard, steam leakage, maintenance management difficulty, therefore is not suitable for the average family residence heating; The working media of hot-water heating system is liquid water, and system pressure is less, temperature is lower, increases conveying energy consumption but aqueous water specific heat is little; Also, in addition, receive the home dwelling limitation in height because of sensible heat transfer increases heat exchange area; Gravity circulating hot water heating system also is difficult to use at home dwelling, and therefore, existing family formula heating system adopts pump to drive hot water system more; So not only need consumed power, also possibly bring noise aspect problem.
Summary of the invention
The purpose of this invention is to provide a kind of family formula negative pressure steam heating system that utilizes airlift pump to provide driving force, water at low temperature steam phase transforming to discharge a large amount of condensation heat.
For realizing above-mentioned purpose, the present invention adopts following technical scheme: a kind of family formula negative pressure steam heating system comprises combustion heater, airlift pump riser, vapour liquid separator, heat exchanger, liquid trap, U-bend, motor-operated control valve, steam ejector; Said combustion heater outlet links to each other with the import of airlift pump riser; The outlet of airlift pump riser is inserted in the vapour liquid separator; The steam outlet of vapour liquid separator links to each other with the heat exchanger import; The liquid phase water outlet of vapour liquid separator converges with the liquid trap import with the condensate outlet of heat exchanger and links to each other, and liquid trap outlet, U-bend, electronic supplying valve, combustion heater import connect successively; Said vapour liquid separator also is provided with two other steam (vapor) outlet; The outlet of vapour liquid separator overhead vapor links to each other with the working steam inlet of steam ejector; Vapour liquid separator side steam (vapor) outlet is arranged on the above position of liquid level in the gas-liquid separator; Vapour liquid separator side steam (vapor) outlet links to each other with steam ejector injection gas access through choke valve, and the steam ejector mixed gas outlet links to each other with electric check valve.
Said vapour liquid separator is established pressure sensor, and the electrical signal of pressure sensor links to each other with controller, and controller also links to each other with the electrical signal line of timer, motor-operated control valve and electric check valve.
Said heat exchanger is steel radiator, fan coil or radiant panel, and the condensate outlet that the steam inlet of said heat exchanger is arranged on heat exchanger top, heat exchanger is arranged on the heat exchanger bottom, and condensate relies on the gravity effect to flow from top to bottom.
The working media that said system adopted is water or the water vapour of 10 ℃～100 ℃ of temperature, absolute pressure 1.2kPa～101.4kPa.
Combustion heater of the present invention adds the small steam bubble that hot water produces and combines to form steam water interface with the major diameter steam bubble; Steam water interface gets in the airlift pump riser; The liquid that utilizes air bubble buoyancy power to drive the bubble top upwards flows along riser; Thereby liquid-vapor mixture is admitted in the vapour liquid separator, and the outlet of airlift pump riser must surpass the liquid level position of vapour liquid separator in case the refluence of solution stopping body.
The present invention requires between combustion heater and vapour liquid separator, to be provided with at least one airlift pump riser; Rounded or the plurality of stepped serrations shape of steam bubble pump riser is to reduce fluid flow resistance, keep the bubble spherical form, to avoid bubble to break at flow process.
The present invention establishes U-bend and solves the vent plug problem that the hot water return pipe section possibly occur between liquid trap and motor-operated control valve, increase system reliability.
The invention has the advantages that and utilize airlift pump riser thermosyphon action that the working media circulation power is provided, save the circulating pump that existing family formula hot water system institute must be provided with, the saving electric energy; Utilize water under the vacuum lower temperature conditions, to vaporize to increase the combustion heater heat transfer temperature difference, to improve combustion heater efficient, fuel saving; Utilize water vapour phase transformation condensing heat-exchange to improve steam-air heat exchanger efficient, reduce heat exchange area, realize steam-air heat exchanger miniaturization.Replace vavuum pump to guarantee the system stability reliably working with steam ejector.Compare with family formula hot water system, this system's movement-less part, consumed power is not saved combustion gas, has a extensive future.
Description of drawings
Fig. 1 is a structural principle sketch map of the present invention.
The specific embodiment
Like Fig. 1 is family of the present invention formula negative pressure steam heating system, and the arrow among Fig. 1 representes to connect between system's each several part ducted direction of flow.The working media that system adopted is water or the water vapour of 10 ℃～100 ℃ of temperature, absolute pressure 1.2kPa～101.4kPa.
This system comprises combustion heater 1, airlift pump riser 2, vapour liquid separator 3, heat exchanger 4, liquid trap 5, U-bend 6, motor-operated control valve 11, steam ejector 8; Said combustion heater 1 outlet links to each other with 2 imports of airlift pump riser; The outlet of airlift pump riser 2 is inserted in the vapour liquid separator 3; The steam outlet of vapour liquid separator 3 links to each other with heat exchanger 4 imports; The liquid phase water outlet of vapour liquid separator 3 converges with liquid trap 5 imports with the condensate outlet of heat exchanger 4 and links to each other, and liquid trap 5 outlets, U-bend 6, electronic supplying valve 11, combustion heater 2 imports connect successively; Said vapour liquid separator 3 also is provided with two other steam (vapor) outlet; The outlet of vapour liquid separator 3 overhead vapor links to each other with the working steam inlet of steam ejector 8; Vapour liquid separator 3 side steam (vapor) outlets link to each other with steam ejector 8 injection gas accesses through choke valve 12, and steam ejector 8 mixed gas outlets link to each other with electric check valve 9.
Said vapour liquid separator 3 is established pressure sensor 7, and the electrical signal of pressure sensor 7 links to each other with controller 10, and controller 10 also links to each other with timer 13, motor-operated control valve 11 and the electrical signal line of electric check valve 9.
Said heat exchanger 4 is steel radiator, fan coil or radiant panel; The condensate outlet that the steam inlet of said heat exchanger 4 is arranged on heat exchanger 4 tops, heat exchanger 4 is arranged on heat exchanger 4 bottoms, and condensate relies on the gravity effect to flow from top to bottom.
The present invention is made up of the hot water and steam circulatory system, steam ejection formula vacuum-pumping system and their supplementary controlled system.The hot water and steam circulatory system course of work is that water is become steam water interface by combustion heater 1 heating local boiling in the combustion heater 1; Deliver to vapour liquid separator 3 via steam bubble pump riser 2; The water vapour entering heat exchanger 4 that flows out from vapour liquid separator 3 carries out heat exchange with air; Water vapour undergoes phase transition and condenses into water and discharge condensation heat; After condensate rely on gravity to flow out from top to bottom to flow out from heat exchanger 4 bottoms in the heat exchanger 4, converge with hot water and flows into liquid trap 5, the priorities under gravity and buoyancy lift acting in conjunction of the hot water in the liquid trap 5 flow through U-bend 6, motor-operated control valve 11 from vapour liquid separator 3; Flow back to combustion heater 1 then, so far accomplish a cyclic process; The steam ejection formula vacuum-pumping system course of work is to vacuumize when working under the pattern when controller 10, and motor-operated control valve 11 is closed, the vaporization of combustion heater 1 heat hot water; Gas pressure constantly increases in the vapour liquid separator 3; Prescribe a time limit when vapour liquid separator 3 internal pressures reach on the controller 10 set high-pressures, electric check valve 9 is opened, and the overhead G&W vapor mixing of vapour liquid separator 3 liquid levels gas flows into choke valve 12; Mist after choke valve 12 throttling step-downs is got into steam ejector 8 by the high steam suction from vapour liquid separator 3; The mist of steam ejector 8 outlets is drained in the atmosphere then, thereby air is constantly taken away on the vapour liquid separator 3 interior liquid levels, up to reaching the controller 10 set pumpdown time upper limits; Motor-operated control valve 11 is opened, electric check valve 9 cuts out, and vacuum finishes; Supplementary controlled system comprises electric check valve 9 and motor-operated control valve 11 controls.
The control of electric check valve 9 and motor-operated control valve 11 is set according to the heat supply mode and the pattern that vacuumizes.Under the heat supply mode, controller 10 sends that action electric check valve 9 cuts out, motor-operated control valve 11 is opened; Vacuumize under the pattern; Controller 10 sends action and at first cuts out motor-operated control valve 11, prescribes a time limit when 7 detected pressures of vapour liquid separator 3 set pressure sensors rise on the set high-pressure, and controller 10 sends action electric check valve 9 and opens; Timer 13 picks up counting; When the pumpdown time reached set time upper limit, controller 10 sent 9 unlatchings of action electric check valve, motor-operated control valve 11 is closed, and the work that vacuumizes is accomplished.
Claims (4)
1. a family formula negative pressure steam heating system is characterized in that: comprise combustion heater, airlift pump riser, vapour liquid separator, heat exchanger, liquid trap, U-bend, motor-operated control valve, steam ejector; Said combustion heater outlet links to each other with the import of airlift pump riser; The outlet of airlift pump riser is inserted in the vapour liquid separator; The steam outlet of vapour liquid separator links to each other with the heat exchanger import; The liquid phase water outlet of vapour liquid separator converges with the liquid trap import with the condensate outlet of heat exchanger and links to each other, and liquid trap outlet, U-bend, electronic supplying valve, combustion heater import connect successively; Said vapour liquid separator also is provided with two other steam (vapor) outlet; The outlet of vapour liquid separator overhead vapor links to each other with the working steam inlet of steam ejector; Vapour liquid separator side steam (vapor) outlet is arranged on the above position of liquid level in the gas-liquid separator; Vapour liquid separator side steam (vapor) outlet links to each other with steam ejector injection gas access through choke valve, and the steam ejector mixed gas outlet links to each other with electric check valve.
2. the described family of claim 1 formula negative pressure steam heating system; It is characterized in that: said vapour liquid separator is established pressure sensor; The electrical signal of pressure sensor links to each other with controller, and controller also links to each other with the electrical signal line of timer, motor-operated control valve and electric check valve.
3. family according to claim 1 formula negative pressure steam heating system, it is characterized in that: said heat exchanger is steel radiator, fan coil or radiant panel; The condensate outlet that the steam inlet of said heat exchanger is arranged on heat exchanger top, heat exchanger is arranged on the heat exchanger bottom, and condensate relies on the gravity effect to flow from top to bottom.
4. family according to claim 1 formula negative pressure steam heating system is characterized in that: working media is water or the water vapour of 10 ℃～100 ℃ of temperature, absolute pressure 1.2kPa～101.4kPa.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110408746.2A CN102418953B (en) | 2011-12-10 | 2011-12-10 | Household negative-pressure steam heating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110408746.2A CN102418953B (en) | 2011-12-10 | 2011-12-10 | Household negative-pressure steam heating system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102418953A true CN102418953A (en) | 2012-04-18 |
| CN102418953B CN102418953B (en) | 2014-11-12 |
Family
ID=45943491
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201110408746.2A Active CN102418953B (en) | 2011-12-10 | 2011-12-10 | Household negative-pressure steam heating system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102418953B (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105651057A (en) * | 2016-03-21 | 2016-06-08 | 中国恩菲工程技术有限公司 | Cooling system |
| CN108036396A (en) * | 2017-11-02 | 2018-05-15 | 哈尔滨理工大学 | A kind of portable domestic heating plant |
| CN108550948A (en) * | 2018-04-16 | 2018-09-18 | 河南科技大学 | A kind of cold heat binary cycle system for power battery pack heat management |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6141850A (en) * | 1984-07-31 | 1986-02-28 | Hitachi Zosen Corp | Hot water generating equipment utilizing geothermal water |
| JPS63197906U (en) * | 1987-06-11 | 1988-12-20 | ||
| JPH01155099A (en) * | 1987-12-11 | 1989-06-16 | Kajima Corp | Liquid forcing device by means of low boiling point medium |
| CN2152166Y (en) * | 1993-01-05 | 1994-01-05 | 白亮显 | Household steam central heating device |
-
2011
- 2011-12-10 CN CN201110408746.2A patent/CN102418953B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6141850A (en) * | 1984-07-31 | 1986-02-28 | Hitachi Zosen Corp | Hot water generating equipment utilizing geothermal water |
| JPS63197906U (en) * | 1987-06-11 | 1988-12-20 | ||
| JPH01155099A (en) * | 1987-12-11 | 1989-06-16 | Kajima Corp | Liquid forcing device by means of low boiling point medium |
| CN2152166Y (en) * | 1993-01-05 | 1994-01-05 | 白亮显 | Household steam central heating device |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105651057A (en) * | 2016-03-21 | 2016-06-08 | 中国恩菲工程技术有限公司 | Cooling system |
| CN108036396A (en) * | 2017-11-02 | 2018-05-15 | 哈尔滨理工大学 | A kind of portable domestic heating plant |
| CN108550948A (en) * | 2018-04-16 | 2018-09-18 | 河南科技大学 | A kind of cold heat binary cycle system for power battery pack heat management |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102418953B (en) | 2014-11-12 |
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| Date | Code | Title | Description |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220916 Address after: 644303 Leigong Group (2# workshop), Kaifu Longmen Village, Changning Town, Changning County, Yibin, Sichuan Province, etc. Patentee after: Sichuan Lex fluid control equipment Co.,Ltd. Address before: 621010, No. 59, Qinglong Avenue, Fucheng District, Sichuan, Mianyang Patentee before: Southwest University of Science and Technology |
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| TR01 | Transfer of patent right |