CN109708508A - A kind of steam storage method - Google Patents
A kind of steam storage method Download PDFInfo
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- CN109708508A CN109708508A CN201811442272.1A CN201811442272A CN109708508A CN 109708508 A CN109708508 A CN 109708508A CN 201811442272 A CN201811442272 A CN 201811442272A CN 109708508 A CN109708508 A CN 109708508A
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- steam
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- accumulation
- water
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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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
Abstract
The invention discloses a kind of steam storage methods, including steam generator, compressor, phase change heat accumulator and heat-accumulation combustor, it is characterized in that, steps are as follows for specific method: tap water purifying → tap water sterilization → steam generation → both vapor compression → steam fills → steam release → steam heating；This kind of steam storage method advantageously ensures that the cleaning of the steam of generation by carrying out purification and sterilization processing with water to steam generation before steam generation；Compression processing is carried out to steam before steam enters in phase change heat accumulator, so as to obtain high temperature and high pressure steam, so that can more rapid and better carry out phase-transition heat-storage between phase change heat accumulator and the steam of high temperature and pressure；It by the setting of heat-accumulation combustor, is released in steam in use, first heat to the steam released, to obtain high-temperature steam, is then passed through in heat exchanger and is carried out using to be conducive to improve the heat treatment efficiency of heat exchanger again.
Description
Technical field
The present invention relates to technical field of heat treatment, in particular to a kind of steam storage method.
Background technique
With gradually decreasing for non-renewable resources, the coal price that steam uses occurs and goes up all the way, steam cost is big
Width improves, and therefore, enterprise carries out accumulation of heat storage to steam, not only remarkable in economical benefits, while the social benefits such as emission reduction environmental protection are more
Add significant.It is stored currently, usually the steam of generation is directly inputted in steam accumulator, but such storing mode
It is unfavorable for exporting high-temperature steam, to influence heat treatment efficiency when later period use.
Summary of the invention
The main purpose of the present invention is to provide a kind of steam storage methods, can effectively solve asking in background technique
Topic.
To achieve the above object, the invention provides the following technical scheme: a kind of steam storage method, including steam generation
Device, compressor, phase change heat accumulator and heat-accumulation combustor, steps are as follows for specific method:
One, tap water purifying: purification will be filtered to tap water using clarifier；
Two, tap water is sterilized: purified tap water is irradiated using ultraviolet light in sterilization sink, to kill tap water
In bacterium；
Three, steam generation: the tap water after purification and sterilization is passed through in steam generator, and the flow of water is 3L/min, benefit
Heating evaporation is carried out to the tap water after purification and sterilization with steam generator, to form clean water vapour；
Four, both vapor compression: first atmospheric steam is collapsed into using compressor the steam of high temperature and pressure；
Five, steam fills: the steam for connecting steam generator and phase change heat accumulator fills jet chimney between mouth, leads to
Entering high-temperature high-pressure overheat steam, high temperature and high pressure steam fills mouth by steam and is entered inside phase change heat accumulator by steam jet pipe, these
So that container inner pressure rises, the saturated water inside phase change heat accumulator was become by saturation state for the entrance of high temperature and high pressure steam
Cold state, steam condensation become liquid water, meanwhile, stream-liquid two-phase flow flows between metal heat accumulation pipe, constantly washes away each metal
Heat accumulation pipe, the interior sizing phase change heat storage material of metal heat accumulation pipe absorb heat, undergo phase transition when reaching certain temperature, steam exists
The condensation of metal accumulation of heat tube outer surface, the sensible heat and the latent heat of condensation that such high temperature and high pressure steam releases are simultaneously by the liquid of surrounding
Water and metal heat accumulation pipe absorb, and pressure rise in phase change heat accumulator, liquid coolant-temperature gage rises, phase transformation of being formed in metal heat accumulation pipe
Heat-storing material is undergone phase transition due to heat absorption；
Six, steam discharges: the steam (vapor) outlet of phase change heat accumulator is connected to the input channel of heat-accumulation combustor, phase-transition heat-storage
Steam is discharged in device, internal pressure decline, and saturated water becomes superheated water in phase change heat accumulator, and inside flashes, and generates steaming
Vapour, when phase transition temperature of the liquid coolant-temperature gage lower than sizing phase change heat storage material, sizing phase change heat storage material is undergone phase transition, and is released
The latent heat of phase change put passes to liquid water by metal heat accumulation pipe outward, and surface boiling occurs in metal accumulation of heat pipe surface, produces
Raw a large amount of steam；
Seven, steam heats: water vapour enters in heat-accumulation combustor, and the high-temperature thermal storage body in heat-accumulation combustor steams water
Vapour is heated to 750-850 DEG C of high temperature, and the water vapour being heated enters in heat exchanger for material-heat-exchanging use.
Preferably, the ultraviolet germicidal ultraviolet source wavelength in the step 2 is 260~265nm, and ultraviolet light is radiated at
UV intensity >=80 μ W/cm on the water surface2。
Preferably, the heat storage is accumulation of heat porous ceramics, and the accumulation of heat porous ceramics is mullite ceramic, duct
For six sides, 3 hole of 8mm, the volume of accumulation of heat porous ceramics is 2m in heat-accumulation combustor3。
Preferably, be provided with burner in the heat-accumulation combustor, the burner directly utilize flame to heat storage into
Row heating is to improve its temperature.
Preferably, the shell of the phase change heat accumulator is steel pressure vessel.
Preferably, insulation shell is provided on the phase change heat accumulator outer wall, the insulation shell is filled using mineral wool
It forms.
Preferably, heat preservation outer wall is provided on the heat-accumulation combustor outer wall, the heat preservation outer wall is filled using alumina silicate
It forms.
Preferably, the metal heat accumulation pipe is filled in canister using sizing phase change heat storage material and is made.
Compared with prior art, the invention has the following beneficial effects: this kind of steam storage methods, by sending out in steam
Purification and sterilization processing are carried out with water to steam generation before life, advantageously ensure that the cleaning of the steam of generation；Enter in steam
Compression processing is carried out to steam before in phase change heat accumulator, so as to obtain high temperature and high pressure steam so that phase change heat accumulator with
Phase-transition heat-storage can be more rapid and better carried out between the steam of high temperature and pressure；By the setting of heat-accumulation combustor, discharged in steam
Out in use, first heating to the steam released, to obtain high-temperature steam, then it is passed through in heat exchanger again
It carries out using to be conducive to improve the heat treatment efficiency of heat exchanger.
Detailed description of the invention
Fig. 1 is a kind of steam storage method flow chart of the present invention；
In figure: 1, clarifier；2, sink is sterilized；3, steam generator；4, compressor；5, phase change heat accumulator；6, accumulation of heat is fired
Burner；7, heat exchanger；8, insulation shell；9, steam jet pipe；10, metal heat accumulation pipe；11, burner；12, heat storage；13, it keeps the temperature
Outer wall.
Specific embodiment
To be easy to understand the technical means, the creative features, the aims and the efficiencies achieved by the present invention, tie below
Specific embodiment is closed, the present invention is further explained.
As shown in Figure 1, a kind of steam storage method, including steam generator, compressor, phase change heat accumulator and accumulation of heat combustion
Burner, steps are as follows for specific method:
One, tap water purifying: purification will be filtered to tap water using clarifier；
Two, tap water is sterilized: purified tap water is irradiated using ultraviolet light in sterilization sink, to kill tap water
In bacterium；
Three, steam generation: the tap water after purification and sterilization is passed through in steam generator, and the flow of water is 3L/min, benefit
Heating evaporation is carried out to the tap water after purification and sterilization with steam generator, to form clean water vapour；
Four, both vapor compression: first atmospheric steam is collapsed into using compressor the steam of high temperature and pressure；
Five, steam fills: the steam for connecting steam generator and phase change heat accumulator fills jet chimney between mouth, leads to
Entering high-temperature high-pressure overheat steam, high temperature and high pressure steam fills mouth by steam and is entered inside phase change heat accumulator by steam jet pipe, these
So that container inner pressure rises, the saturated water inside phase change heat accumulator was become by saturation state for the entrance of high temperature and high pressure steam
Cold state, steam condensation become liquid water, meanwhile, stream-liquid two-phase flow flows between metal heat accumulation pipe, constantly washes away each metal
Heat accumulation pipe, the interior sizing phase change heat storage material of metal heat accumulation pipe absorb heat, undergo phase transition when reaching certain temperature, steam exists
The condensation of metal accumulation of heat tube outer surface, the sensible heat and the latent heat of condensation that such high temperature and high pressure steam releases are simultaneously by the liquid of surrounding
Water and metal heat accumulation pipe absorb, and pressure rise in phase change heat accumulator, liquid coolant-temperature gage rises, phase transformation of being formed in metal heat accumulation pipe
Heat-storing material is undergone phase transition due to heat absorption；
Six, steam discharges: the steam (vapor) outlet of phase change heat accumulator is connected to the input channel of heat-accumulation combustor, phase-transition heat-storage
Steam is discharged in device, internal pressure decline, and saturated water becomes superheated water in phase change heat accumulator, and inside flashes, and generates steaming
Vapour, when phase transition temperature of the liquid coolant-temperature gage lower than sizing phase change heat storage material, sizing phase change heat storage material is undergone phase transition, and is released
The latent heat of phase change put passes to liquid water by metal heat accumulation pipe outward, and surface boiling occurs in metal accumulation of heat pipe surface, produces
Raw a large amount of steam；
Seven, steam heats: water vapour enters in heat-accumulation combustor, and the high-temperature thermal storage body in heat-accumulation combustor steams water
Vapour is heated to 750-850 DEG C of high temperature, and the water vapour being heated enters in heat exchanger for material-heat-exchanging use.
Ultraviolet germicidal ultraviolet source wavelength in step 2 is 260~265nm, and ultraviolet light is radiated at the purple on the water surface
Outer intensity >=80 μ W/cm2。
Heat storage is accumulation of heat porous ceramics, and accumulation of heat porous ceramics is mullite ceramic, and duct is six sides, 3 hole of 8mm,
The volume of accumulation of heat porous ceramics is 2m in heat-accumulation combustor3。
Burner is provided in heat-accumulation combustor, burner directly heats to improve it heat storage using flame
Temperature.
The shell of phase change heat accumulator is steel pressure vessel.
Insulation shell is provided on phase change heat accumulator outer wall, insulation shell is filled using mineral wool.
Heat preservation outer wall is provided on heat-accumulation combustor outer wall, heat preservation outer wall is filled using alumina silicate.
Metal heat accumulation pipe is filled in canister using sizing phase change heat storage material and is made.
Embodiment 1
As shown in Figure 1, a kind of steam storage method, including steam generator, compressor, phase change heat accumulator and accumulation of heat combustion
Burner, steps are as follows for specific method:
One, tap water purifying: purification will be filtered to tap water using clarifier；
Two, tap water is sterilized: purified tap water is irradiated using ultraviolet light in sterilization sink, to kill tap water
In bacterium；
Three, steam generation: the tap water after purification and sterilization is passed through in steam generator, and the flow of water is 3L/min, benefit
Heating evaporation is carried out to the tap water after purification and sterilization with steam generator, to form clean water vapour；
Four, both vapor compression: first atmospheric steam is collapsed into using compressor the steam of high temperature and pressure；
Five, steam fills: the steam for connecting steam generator and phase change heat accumulator fills jet chimney between mouth, leads to
Entering high-temperature high-pressure overheat steam, high temperature and high pressure steam fills mouth by steam and is entered inside phase change heat accumulator by steam jet pipe, these
So that container inner pressure rises, the saturated water inside phase change heat accumulator was become by saturation state for the entrance of high temperature and high pressure steam
Cold state, steam condensation become liquid water, meanwhile, stream-liquid two-phase flow flows between metal heat accumulation pipe, constantly washes away each metal
Heat accumulation pipe, the interior sizing phase change heat storage material of metal heat accumulation pipe absorb heat, undergo phase transition when reaching certain temperature, steam exists
The condensation of metal accumulation of heat tube outer surface, the sensible heat and the latent heat of condensation that such high temperature and high pressure steam releases are simultaneously by the liquid of surrounding
Water and metal heat accumulation pipe absorb, and pressure rise in phase change heat accumulator, liquid coolant-temperature gage rises, phase transformation of being formed in metal heat accumulation pipe
Heat-storing material is undergone phase transition due to heat absorption；
Six, steam discharges: the steam (vapor) outlet of phase change heat accumulator is connected to the input channel of heat-accumulation combustor, phase-transition heat-storage
Steam is discharged in device, internal pressure decline, and saturated water becomes superheated water in phase change heat accumulator, and inside flashes, and generates steaming
Vapour, when phase transition temperature of the liquid coolant-temperature gage lower than sizing phase change heat storage material, sizing phase change heat storage material is undergone phase transition, and is released
The latent heat of phase change put passes to liquid water by metal heat accumulation pipe outward, and surface boiling occurs in metal accumulation of heat pipe surface, produces
Raw a large amount of steam；
Seven, steam heats: water vapour enters in heat-accumulation combustor, and the high-temperature thermal storage body in heat-accumulation combustor steams water
Vapour is heated to 750 DEG C of high temperature, and the water vapour being heated enters in heat exchanger for material-heat-exchanging use.
Embodiment 2
As shown in Figure 1, a kind of steam storage method, including steam generator, compressor, phase change heat accumulator and accumulation of heat combustion
Burner, steps are as follows for specific method:
One, tap water purifying: purification will be filtered to tap water using clarifier；
Two, tap water is sterilized: purified tap water is irradiated using ultraviolet light in sterilization sink, to kill tap water
In bacterium；
Three, steam generation: the tap water after purification and sterilization is passed through in steam generator, and the flow of water is 3L/min, benefit
Heating evaporation is carried out to the tap water after purification and sterilization with steam generator, to form clean water vapour；
Four, both vapor compression: first atmospheric steam is collapsed into using compressor the steam of high temperature and pressure；
Five, steam fills: the steam for connecting steam generator and phase change heat accumulator fills jet chimney between mouth, leads to
Entering high-temperature high-pressure overheat steam, high temperature and high pressure steam fills mouth by steam and is entered inside phase change heat accumulator by steam jet pipe, these
So that container inner pressure rises, the saturated water inside phase change heat accumulator was become by saturation state for the entrance of high temperature and high pressure steam
Cold state, steam condensation become liquid water, meanwhile, stream-liquid two-phase flow flows between metal heat accumulation pipe, constantly washes away each metal
Heat accumulation pipe, the interior sizing phase change heat storage material of metal heat accumulation pipe absorb heat, undergo phase transition when reaching certain temperature, steam exists
The condensation of metal accumulation of heat tube outer surface, the sensible heat and the latent heat of condensation that such high temperature and high pressure steam releases are simultaneously by the liquid of surrounding
Water and metal heat accumulation pipe absorb, and pressure rise in phase change heat accumulator, liquid coolant-temperature gage rises, phase transformation of being formed in metal heat accumulation pipe
Heat-storing material is undergone phase transition due to heat absorption；
Six, steam discharges: the steam (vapor) outlet of phase change heat accumulator is connected to the input channel of heat-accumulation combustor, phase-transition heat-storage
Steam is discharged in device, internal pressure decline, and saturated water becomes superheated water in phase change heat accumulator, and inside flashes, and generates steaming
Vapour, when phase transition temperature of the liquid coolant-temperature gage lower than sizing phase change heat storage material, sizing phase change heat storage material is undergone phase transition, and is released
The latent heat of phase change put passes to liquid water by metal heat accumulation pipe outward, and surface boiling occurs in metal accumulation of heat pipe surface, produces
Raw a large amount of steam；
Seven, steam heats: water vapour enters in heat-accumulation combustor, and the high-temperature thermal storage body in heat-accumulation combustor steams water
Vapour is heated to 800 DEG C of high temperature, and the water vapour being heated enters in heat exchanger for material-heat-exchanging use.
Embodiment 3
As shown in Figure 1, a kind of steam storage method, including steam generator, compressor, phase change heat accumulator and accumulation of heat combustion
Burner, steps are as follows for specific method:
One, tap water purifying: purification will be filtered to tap water using clarifier；
Two, tap water is sterilized: purified tap water is irradiated using ultraviolet light in sterilization sink, to kill tap water
In bacterium；
Three, steam generation: the tap water after purification and sterilization is passed through in steam generator, and the flow of water is 3L/min, benefit
Heating evaporation is carried out to the tap water after purification and sterilization with steam generator, to form clean water vapour；
Four, both vapor compression: first atmospheric steam is collapsed into using compressor the steam of high temperature and pressure；
Five, steam fills: the steam for connecting steam generator and phase change heat accumulator fills jet chimney between mouth, leads to
Entering high-temperature high-pressure overheat steam, high temperature and high pressure steam fills mouth by steam and is entered inside phase change heat accumulator by steam jet pipe, these
So that container inner pressure rises, the saturated water inside phase change heat accumulator was become by saturation state for the entrance of high temperature and high pressure steam
Cold state, steam condensation become liquid water, meanwhile, stream-liquid two-phase flow flows between metal heat accumulation pipe, constantly washes away each metal
Heat accumulation pipe, the interior sizing phase change heat storage material of metal heat accumulation pipe absorb heat, undergo phase transition when reaching certain temperature, steam exists
The condensation of metal accumulation of heat tube outer surface, the sensible heat and the latent heat of condensation that such high temperature and high pressure steam releases are simultaneously by the liquid of surrounding
Water and metal heat accumulation pipe absorb, and pressure rise in phase change heat accumulator, liquid coolant-temperature gage rises, phase transformation of being formed in metal heat accumulation pipe
Heat-storing material is undergone phase transition due to heat absorption；
Six, steam discharges: the steam (vapor) outlet of phase change heat accumulator is connected to the input channel of heat-accumulation combustor, phase-transition heat-storage
Steam is discharged in device, internal pressure decline, and saturated water becomes superheated water in phase change heat accumulator, and inside flashes, and generates steaming
Vapour, when phase transition temperature of the liquid coolant-temperature gage lower than sizing phase change heat storage material, sizing phase change heat storage material is undergone phase transition, and is released
The latent heat of phase change put passes to liquid water by metal heat accumulation pipe outward, and surface boiling occurs in metal accumulation of heat pipe surface, produces
Raw a large amount of steam；
Seven, steam heats: water vapour enters in heat-accumulation combustor, and the high-temperature thermal storage body in heat-accumulation combustor steams water
Vapour is heated to 850 DEG C of high temperature, and the water vapour being heated enters in heat exchanger for material-heat-exchanging use.
Table 1 is that the heat treatment efficiency that heat-accumulation combustor carries out heat exchanging device after being heated to 750-850 DEG C to water vapour generates
Influence, test result is as follows:
| Temperature DEG C | 750 | 800 | 850 |
| Heat treatment efficiency % | 69.8 | 72.9 | 76.3 |
As shown in Table 1, the heat treatment efficiency of heat exchanger with heat-accumulation combustor to the raising of the heating temperature of water vapour and
It improves, therefore, high-temperature steam can be obtained by carrying out heating again using heat-accumulation combustor to it after steam release, use height
Warm steam carries out the heat treatment efficiency that heat exchange is conducive to improve heat exchanger to material.
The above shows and describes the basic principles and main features of the present invention and the advantages of the present invention.The skill of the industry
Art personnel it should be appreciated that the present invention is not limited to the above embodiments, the above embodiments and description only describe
The principle of the present invention, without departing from the spirit and scope of the present invention, various changes and improvements may be made to the invention, this
A little changes and improvements all fall within the protetion scope of the claimed invention.The claimed scope of the invention is by the attached claims
Book and its equivalent thereof.
Claims (8)
1. a kind of steam storage method, including steam generator, compressor, phase change heat accumulator and heat-accumulation combustor, feature exist
In steps are as follows for specific method:
One, tap water purifying: purification will be filtered to tap water using clarifier；
Two, tap water is sterilized: purified tap water is irradiated using ultraviolet light in sterilization sink, it is thin in tap water to kill
Bacterium；
Three, steam generation: the tap water after purification and sterilization is passed through in steam generator, and the flow of water is 3L/min, utilizes steaming
Vapour generator carries out heating evaporation to the tap water after purification and sterilization, to form clean water vapour；
Four, both vapor compression: first atmospheric steam is collapsed into using compressor the steam of high temperature and pressure；
Five, steam fills: the steam for connecting steam generator and phase change heat accumulator fills jet chimney between mouth, is passed through high temperature
High pressure superheated steam, high temperature and high pressure steam fill mouth by steam and are entered inside phase change heat accumulator by steam jet pipe, these high temperature are high
The entrance of steam is pressed so that container inner pressure rises, the saturated water inside phase change heat accumulator becomes supercooled state by saturation state,
Steam condensation becomes liquid water, meanwhile, stream-liquid two-phase flow flows between metal heat accumulation pipe, each metal heat accumulation pipe is constantly washed away,
Sizing phase change heat storage material absorbs heat in metal heat accumulation pipe, undergoes phase transition when reaching certain temperature, steam is in metal accumulation of heat
Tube outer surface condensation, the sensible heat and the latent heat of condensation that such high temperature and high pressure steam releases are stored by the liquid water of surrounding and metal simultaneously
Heat pipe absorbs, and pressure rise in phase change heat accumulator, liquid coolant-temperature gage rises, in metal heat accumulation pipe sizing phase change heat storage material due to
Heat absorption is undergone phase transition；
Six, steam discharges: the steam (vapor) outlet of phase change heat accumulator is connected to the input channel of heat-accumulation combustor, is steamed in phase change heat accumulator
Vapour discharge, internal pressure decline, and saturated water becomes superheated water in phase change heat accumulator, and inside flashes, and generate steam, work as liquid
When coolant-temperature gage is lower than the phase transition temperature of sizing phase change heat storage material, sizing phase change heat storage material is undergone phase transition, and the phase transformation of release is latent
Heat passes to liquid water by metal heat accumulation pipe outward, and surface boiling occurs in metal accumulation of heat pipe surface, generates a large amount of steam；
Seven, steam heats: water vapour enters in heat-accumulation combustor, and the high-temperature thermal storage body in heat-accumulation combustor is by steam heating
To 750-850 DEG C of high temperature, the water vapour being heated enters in heat exchanger for material-heat-exchanging use.
2. a kind of steam storage method according to claim 1, which is characterized in that the ultraviolet germicidal in the step 2
Ultraviolet source wavelength is 260~265nm, and ultraviolet light is radiated at the UV intensity on the water surface >=80 μ W/cm2。
3. a kind of steam storage method according to claim 1, which is characterized in that the heat storage is the porous pottery of accumulation of heat
Porcelain, the accumulation of heat porous ceramics are mullite ceramic, and duct is six sides, 3 hole of 8mm, accumulation of heat porous ceramics in heat-accumulation combustor
Volume be 2m3。
4. a kind of steam storage method according to claim 1, which is characterized in that be provided with combustion in the heat-accumulation combustor
Burner, the burner directly heat heat storage using flame to improve its temperature.
5. a kind of steam storage method according to claim 1, which is characterized in that the shell of the phase change heat accumulator is steel
Pressure vessel processed.
6. a kind of steam storage method according to claim 1, which is characterized in that be arranged on the phase change heat accumulator outer wall
There is insulation shell, the insulation shell is filled using mineral wool.
7. a kind of steam storage method according to claim 1, which is characterized in that be arranged on the heat-accumulation combustor outer wall
There is heat preservation outer wall, the heat preservation outer wall is filled using alumina silicate.
8. a kind of steam storage method according to claim 1, which is characterized in that the metal heat accumulation pipe is using sizing phase
Change heat storage material is filled in canister and is made.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811442272.1A CN109708508A (en) | 2018-11-29 | 2018-11-29 | A kind of steam storage method |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811442272.1A CN109708508A (en) | 2018-11-29 | 2018-11-29 | A kind of steam storage method |
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| Publication Number | Publication Date |
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| CN109708508A true CN109708508A (en) | 2019-05-03 |
Family
ID=66255278
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112696655A (en) * | 2021-02-03 | 2021-04-23 | 重庆卓旺科技有限公司 | Steam gas storage device for electric steam generating device |
| CN113606565A (en) * | 2021-05-11 | 2021-11-05 | 严灼坚 | Vapor generation recompression equipment |
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| WO1986003577A1 (en) * | 1984-12-07 | 1986-06-19 | Michael Laumen | Refrigerating machine or heat pump with a jet pump as the compressor |
| CN104406143A (en) * | 2014-12-09 | 2015-03-11 | 苟仲武 | Vacuum compression high-temperature boiler and steam warming method |
| CN104964260A (en) * | 2015-07-02 | 2015-10-07 | 大连交通大学 | Device for transferring heat in solid energy storage body by means of high-temperature steam |
| CN106287623A (en) * | 2016-07-28 | 2017-01-04 | 上海交通大学 | Phase-change heat-storage steam accumulator |
| CN106352333A (en) * | 2015-07-17 | 2017-01-25 | 江苏中科睿赛污染控制工程有限公司 | Steam heat treatment device, treatment method and use thereof |
| CN106482087A (en) * | 2016-11-28 | 2017-03-08 | 克雷登热能设备(浙江)有限公司 | Steam generator water capacity measuring method and device |
-
2018
- 2018-11-29 CN CN201811442272.1A patent/CN109708508A/en active Pending
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1986003577A1 (en) * | 1984-12-07 | 1986-06-19 | Michael Laumen | Refrigerating machine or heat pump with a jet pump as the compressor |
| CN104406143A (en) * | 2014-12-09 | 2015-03-11 | 苟仲武 | Vacuum compression high-temperature boiler and steam warming method |
| CN104964260A (en) * | 2015-07-02 | 2015-10-07 | 大连交通大学 | Device for transferring heat in solid energy storage body by means of high-temperature steam |
| CN106352333A (en) * | 2015-07-17 | 2017-01-25 | 江苏中科睿赛污染控制工程有限公司 | Steam heat treatment device, treatment method and use thereof |
| CN106287623A (en) * | 2016-07-28 | 2017-01-04 | 上海交通大学 | Phase-change heat-storage steam accumulator |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112696655A (en) * | 2021-02-03 | 2021-04-23 | 重庆卓旺科技有限公司 | Steam gas storage device for electric steam generating device |
| CN113606565A (en) * | 2021-05-11 | 2021-11-05 | 严灼坚 | Vapor generation recompression equipment |
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Application publication date: 20190503 |