CN110500908A - A kind of mobile thermal storage equipment of vehicle-mounted type - Google Patents
A kind of mobile thermal storage equipment of vehicle-mounted type Download PDFInfo
- Publication number
- CN110500908A CN110500908A CN201810465946.3A CN201810465946A CN110500908A CN 110500908 A CN110500908 A CN 110500908A CN 201810465946 A CN201810465946 A CN 201810465946A CN 110500908 A CN110500908 A CN 110500908A
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- Prior art keywords
- heat
- fluid
- storage heater
- storage
- tube
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- 239000012530 fluid Substances 0.000 claims abstract description 114
- 238000005338 heat storage Methods 0.000 claims abstract description 32
- 238000009825 accumulation Methods 0.000 claims abstract description 30
- 239000011232 storage material Substances 0.000 claims abstract description 29
- 238000010438 heat treatment Methods 0.000 claims abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 7
- 238000009434 installation Methods 0.000 claims abstract description 6
- 229910001220 stainless steel Inorganic materials 0.000 claims description 7
- 239000010935 stainless steel Substances 0.000 claims description 7
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- 239000007787 solid Substances 0.000 claims description 4
- 239000000919 ceramic Substances 0.000 claims description 3
- 238000005485 electric heating Methods 0.000 claims description 3
- 238000004146 energy storage Methods 0.000 claims description 3
- 239000005416 organic matter Substances 0.000 claims description 3
- YJTKZCDBKVTVBY-UHFFFAOYSA-N 1,3-Diphenylbenzene Chemical group C1=CC=CC=C1C1=CC=CC(C=2C=CC=CC=2)=C1 YJTKZCDBKVTVBY-UHFFFAOYSA-N 0.000 claims description 2
- GKQBSTJUOVBUDX-UHFFFAOYSA-N 1-(2,3-dimethylphenoxy)-2,3-dimethylbenzene Chemical compound CC1=CC=CC(OC=2C(=C(C)C=CC=2)C)=C1C GKQBSTJUOVBUDX-UHFFFAOYSA-N 0.000 claims description 2
- -1 Benzene-biphenyl ether Chemical compound 0.000 claims description 2
- 230000008859 change Effects 0.000 claims description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 2
- 230000008676 import Effects 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims description 2
- 239000012074 organic phase Substances 0.000 claims description 2
- 150000003839 salts Chemical class 0.000 claims description 2
- 229920002545 silicone oil Polymers 0.000 claims description 2
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 claims 1
- 239000002918 waste heat Substances 0.000 abstract description 12
- 230000005611 electricity Effects 0.000 abstract description 11
- 238000000034 method Methods 0.000 abstract description 6
- 238000005213 imbibition Methods 0.000 abstract 1
- 239000012774 insulation material Substances 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000012071 phase Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- 238000010792 warming Methods 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 239000012782 phase change material Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D20/00—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
- F28D20/02—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat
- F28D20/021—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat the latent heat storage material and the heat-exchanging means being enclosed in one container
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Air-Conditioning For Vehicles (AREA)
Abstract
The invention discloses a kind of mobile thermal storage equipments that can utilize paddy electricity and industrial exhaust heat: paddy electricity by heating element heat form and waste heat input in the form of steam or hot water and moves accumulation of heat vehicle；The storage heater of accumulation of heat box body installation storage thermal energy, the interior heat storage material of placing of storage heater store energy；Expansion tube is placed in two sides at the top of storage heater；The electrical heating elements of top position installation are passed directly to storage heater bottom；The cylindrical groove being isolated with storage heater is installed at top close to storage heater tail position, places circulating pump in slot；Circulating pump is pumped into double-tube heat exchanger from fluid collection pipe imbibition, and fluid enters the fluid distributor of bottom after heat exchange, then with heat storage material heat exchange；Using mobile storage heater using paddy electricity or the method for waste heat supply thermal energy, traditional pipeline heating mode is changed, energy-saving and emission-reduction can be realized using residual heat resources to heating system peak load shifting.
Description
Technical field
The present invention relates to the vehicle-mounted type thermal storage equipments that a kind of packaged type is used for energy storage.
Background technique
Industrial processes generate many waste heats and waste heat fails to utilize and waste, but have a large number of users again simultaneously
Meet production thermal energy needs by combustion gas or oil burning boiler is provided for oneself to produce simultaneously to cause the energy loss that can not be estimated
A large amount of environmental pollution is given birth to.Government has not been met to production under current national energy conservation and emission reduction and environmental protection pay attention to day by day
The requirement of unit.Such as the afterheat steam that some plant produceds generate finds new outlets just as an urgent demand of factory's gain；Or
Person steam power plant carrys out additional income in daytime and night electricity consumption imbalance of supply and demand, warming peak load notch and summer affluence thermal energy
To itself and a difficult problem.If can elsewhere waste heat or paddy electricity come without pipeline transportation, supplement meets the winter
Season peak load notch, the rich thermal energy of production in summer is removed and is used, be solve problem above feasible method.
Summary of the invention
Present invention solves the technical problem that being how waste heat to be removed to use, with the organic company of user for thering is thermal energy to need
It connects, steam or hot water can be supplied and used to user.The bridge for having erected residual heat resources recycling changes traditional energy supply side
Formula realizes the peak load shifting to electric power and gas heating system, has achieved the purpose that using residual heat resources, and then reduce dirt
Dye discharge.
The present invention provides the vehicle-mounted type thermal storage equipment that a kind of packaged type is used for energy storage, the technical solutions of use
For, paddy electricity with heating element heat form and waste heat inputs mobile store via double pipe heat exchanger heat transfer form with steam or hot water
Hot vehicle.The storage heater of storage thermal energy is installed in accumulation of heat compartment main body.Storage heater keeps a spacing with sweep by storage heater support
From.Filling thermal insulation material between accumulation of heat vehicle external box of microvave and storage heater and between sweep and storage heater prevents heat waste.Storage heater
Interior placement heat storage material stores energy, and related heat storage material includes the accumulation of heat of solid ceramic heat-storing sphere, packaging phase change material
Ball and has between circulation of fluid and apparent density contrast and do not react immiscible organic matter in use temperature range
As heat storage material.Expansion tube is placed in two sides at the top of storage heater, for receiving fluid high-temperature expansion part.Top center position is
Electrical heating elements are passed directly to storage heater bottom.Top tail end middle position is cylindrical groove, installs circulating pump in cylindrical groove.For just
Save space simultaneously in installation, cylindrical groove is partially submerged into storage heater, but cylindricality trench bottom is closed and storage heater internal flow every
From.Fluid collection pipe passes through cylindrical groove and connects pump entry, and circulating-pump outlet is connected with another pipeline for passing through cylindrical groove, should
Pipeline is connected with tube chamber in double-tube heat exchanger.Double-tube heat exchanger be it is snakelike, be disposed vertically, straight pipe part and electric heating tube
Intersect installation.The tube chamber other end is communicated with the fluid distributor of storage heater bottom in double-tube heat exchanger.Outside double-tube heat exchanger
Casing inlet pipeline and double-tube heat exchanger outer sleeve outlet conduit pass through storage heater bottom and draw from accumulation of heat vehicle side or tail portion
It is connected out with the inlet and outlet of external fluid.
Detailed description of the invention
Attached drawing 1 is that each component of vehicular accumulation of heat vehicle is shown in right part of flg, is marked in figure: 101- storage heater；102- accumulation of heat object
Matter；103- circulation of fluid；104- expansion tube；105- electrical heating elements；106- cylindrical groove；107- circulating pump；108- fluid collection
Device supervisor；109- fluid collector branch pipe；110- double-tube heat exchanger；111- fluid distributor supervisor；112- fluid distributor branch
Pipe；113- thermal fluid inlet；114- hot fluid outlet ports；The support of 115- storage heater；116- accumulation of heat car body；117- thermal insulation material.
Attached drawing 2 is that each component of vehicular accumulation of heat vehicle is shown in main view, is marked in figure: 201- storage heater；202- accumulation of heat object
Matter；203- circulation of fluid；204- expansion tube；205- electrical heating elements；206- cylindrical groove；207- circulating pump；208- fluid collection
Device supervisor；209- fluid collector branch pipe；210- double-tube heat exchanger；211- fluid distributor supervisor；212- fluid distributor branch
Pipe；213- thermal fluid inlet and outlet；The support of 215- storage heater；216- accumulation of heat car body；217- thermal insulation material.
Attached drawing 3 is that each component of vehicular accumulation of heat vehicle is shown on top view, is marked in figure: 301- storage heater；302- accumulation of heat
Substance；304- expansion tube；305- electrical heating elements；306- cylindrical groove；307- circulating pump；308- fluid collector supervisor/fluid
Distributor supervisor；309- fluid collector branch pipe/fluid distributor branch pipe；310- double-tube heat exchanger；316- accumulation of heat car body；
317- thermal insulation material.
Attached drawing 4 is double-tube heat exchanger schematic diagram, is marked in figure: 401- double-tube heat exchanger outer sleeve；402- sleeve heat exchange
Device inner tube；403- double-tube heat exchanger outer sleeve entrance；The outlet of 404- double-tube heat exchanger outer sleeve；405- circulation of fluid enters
Mouthful；The outlet of 406- circulation of fluid.
Attached drawing 5 is fluid distributor schematic diagram, is marked in figure: 501- fluid distributor supervisor；502- fluid distributor branch
Pipe；503- fluid distributor branch pipe aperture.
Attached drawing 6 is fluid collector schematic diagram, is marked in figure: 601- fluid collector supervisor；602- fluid collector branch
Pipe；603- fluid collector branch pipe aperture.
Specific embodiment
In the case of heat storage material and circulation of fluid direct contact type phase-transition heat-storage, the present invention in accumulation of heat and is put
Thermal process is illustrated.
Paddy electricity accumulation of heat: due to being heat storage material and circulation of fluid direct contact type phase-transition heat-storage situation, heat storage material density
Higher than circulation of fluid density, therefore circulation of fluid and heat storage material have obvious layering, and the heat storage material that heat release is completed is with solid-state shape
Formula is deposited in storage heater bottom, and there are a large amount of micropores between accumulation of heat particle or crystal, and micropore gap is filled by circulation of fluid, and big portion
The circulation of fluid divided swims in the top of heat storage material.Paddy electricity is converted into thermal energy, electrical heating elements hair by electrical heating elements
Heat transfers energy to the circulation of fluid and heat storage material of surrounding, melts the heat storage material of surrounding at first, causes electric heating first
Micropore around part expands.Under the action of circulating pump, circulation of fluid collects via fluid collector and pumps double-tube heat exchanger
Enter heat-accumulator tank bottom after heat exchange, the upward forced flow of fluid is promoted by fluid distributor, realizes interior circulation, heat will be carried
Hot fluid force to carry out heat exchange with the cold fluid of surrounding and heat storage material, heat is gradually spread to surrounding fluid and accumulation of heat object
Matter, system are gradually warming up to the complete phase transformation of heat storage material, and heat-accumulating process is completed.
Paddy electricity heat release: starting circulating pump, under suction, circulation of fluid passes through the aperture at the top of fluid collector branch pipe
Incoming fluid collector branch pipe, and enter circulating pump after being pooled to fluid collector supervisor, it is pumped into double-tube heat exchanger inner tube, is fed
Enter the intracorporal fluid heating of double-tube heat exchanger outer sleeve chamber, recycle stream temperature reduction enters after coming out from double-tube heat exchanger
The fluid distributor of storage heater bottom is responsible for, and so that fluid is forced up flowing by each aperture of fluid distributor branch pipe, with
Circulation of fluid and the heat storage material heat exchange of surrounding, gradually reach at the top of storage heater, and temperature rises, and are again introduced into fluid collector and join
Solid-state is transformed by liquid, heat release is completed up to heat storage material complete phase transformation with heat exchange cycle next time.
Waste heat accumulation of heat: the fluid for carrying waste heat enters in storage heater inner sleeve heat exchange of heat pipe outer sleeve cavity, on the one hand gives
Circulation of fluid heat exchange outside double-tube heat exchanger, increases micropore between the solid-state heat storage material of surrounding, promotes the interior flowing recycled；
On the other hand the fluid and double-tube heat exchanger inner tube circulation of fluid for carrying waste heat exchange heat, and release after heat outside double-tube heat exchanger
Storage heater is flowed out in parts casing pipe cavity.And on the one hand storage heater fluid circulating promotes double-tube heat exchanger in the case where recycling pumping action
The fluid that surrounding absorbs heat heats up and gradually spreads；On the other hand by forced circulation, make sleeve pipe inner tube of heat exchanger
Circulation of fluid is diffused into around the heat storage material in storage heater after absorbing heat by storage heater bottom flow distributor, by changing
Heat increases heat storage material temperature, until undergoing phase transition completely, accumulation of heat is completed.
Waste heat heat release: user's fluid from outside fluid inlet enters storage heater inner sleeve heat exchange of heat pipe outer sleeve cavity, and one
Aspect absorbs the energy of heat storage material in storage heater cavity, and on the other hand the circulation of fluid with sleeve pipe inner tube of heat exchanger is changed
Heat flows out after the heating of user's fluid from double-tube heat exchanger outer sleeve, and the circulation of fluid of double-tube heat exchanger inner tube reduces temperature
Afterwards, enter the fluid distributor of storage heater bottom from the outflow of double-tube heat exchanger inner tube in the case where recycling pumping action, and be forced up stream
Dynamic that heat exchange occurs with heat storage material, temperature enters circulating pump from the fluid collector at the top of storage heater after increasing and participates in changing again
Heat is transformed into solid-state by liquid until heat storage material heat release is completed in storage heater.
The embodiment of the present invention is illustrated with reference to the accompanying drawing:
Present device had both been suitable for paddy electricity downloading accumulation of heat and has been also suitable for utilizing the accumulation of heat of industrial exhaust heat and waste heat, passed through vehicle-mounted shape
Thermal energy is shifted utilization by formula, paddy electricity by electrical heating elements (105) heat form and waste heat in the form of steam or hot water via
Double pipe heat exchanger (110) heat transfer form inputs mobile accumulation of heat vehicle.
With reference to attached drawing 1, the storage heater (101) of storage thermal energy is installed in accumulation of heat car body (116).Storage heater (101) passes through
Storage heater supports (115) and sweep to keep certain distance.Between accumulation of heat car body (116) and storage heater (101) and sweep with
Thermal insulation material (117) are filled between storage heater (101) prevents heat waste.Heat storage material (102) are placed in storage heater (101) stores energy
Amount, related heat storage material (102) both include solid ceramic heat-storing sphere, encapsulate inorganic/organic phase change material heat-storing sphere with
And there is obvious density contrast between circulation of fluid (103) and do not react immiscible organic matter in use temperature range and make
For heat storage material (102).The circulation of fluid (103) being suitble to has high temperature resistant, low-vapor pressure, low viscosity and the spy for stablizing safety
Point can be used including water, fused salt, xylyl ether, hydrogenated terphenyl, organic silicone oil, biphenyl-biphenyl ether mixture, ethylene glycol
Aqueous solution.
Expansion tube (104) are placed in two sides at the top of storage heater (101), and expansion tube (104) bottom is higher than storage heater (101) top
Portion, for receiving fluid high-temperature expansion part；Storage heater (101) top center position is that electrical heating elements (105) are passed directly to
Storage heater (101) bottom；Top tail end middle position is cylindrical groove (106), installs circulating pump (107) in cylindrical groove (106), is
Be easily installed while saving space, cylindrical groove (106) is partially submerged into storage heater (101), but cylindrical groove (106) bottom it is closed with
Storage heater (101) fluid circulating inside (103) isolation, fluid collection pipe pass through cylindrical groove (106) connection circulating pump (107) and enter
Mouthful, circulating pump (107) outlet is connected with another pipeline for passing through cylindrical groove (106), the pipeline and double-tube heat exchanger inner tube (402)
Cavity is connected.
Double-tube heat exchanger inner tube (402) cavity outlet end is communicated with the fluid distributor of storage heater (101) bottom.It follows first
Circulation body (103) enters around the aperture extruding that fluid distributor supervisor (111) then passes through on fluid distributor branch pipe (112)
Upward fluid.The angle a range of fluid distributor branch pipe aperture (503) and level is two sides pair between 15 degree to 90 degree
Claim aperture, each hole size is to be divided between 20 millimeters to 200 millimeters between each aperture between 2 millimeters to 10 millimeters.Fortune upwards
Dynamic circulation of fluid (103) and heat storage material (102) carries out heat exchange, and temperature reaches at the top of storage heater (101) after gradually rising,
Into fluid collector branch pipe (602) and it is pooled to fluid collector supervisor (601).The aperture of fluid collector branch pipe (603) position
It sets at top, prevents solid particle from entering blocking pipeline.Fluid collector branch pipe aperture (603) size is at 2 millimeters to 10 millimeters
Between, each pitch of holes is between 20 millimeters to 200 millimeters.Circulation of fluid (103) is from fluid collector supervisor (601) by cylindrical groove
(106) circulating pump (107) suction pump in is into double-tube heat exchanger inner tube (402), into storage heater (101) bottom after exchanging heat
Fluid distributor, which is responsible in (501), carries out next heat exchange cycle.Double-tube heat exchanger outer sleeve import (403) and sleeve heat exchange
Device outer sleeve exports (404) pipeline and passes through storage heater (101) bottom and draw from storage vehicle side or tail portion and external fluid
Inlet and outlet be connected.
As shown in Fig. 4, structure is serpentine configuration to double-tube heat exchanger (110), is disposed vertically, with electrical heating elements (105)
Intersect installation, convenient for passing through electrical heating elements (105) or double-tube heat exchanger outer sleeve in heat storage material (102) heat-accumulating process
(401) outer wall heating melting ambient substance expands micropore, accelerates fluid circulation, improves heat storage efficiency, when reducing accumulation of heat completion
Between.Double-tube heat exchanger (110) main material is stainless steel material, and wherein double-tube heat exchanger outer sleeve (401) may be selected stainless
Steel seamless pipe or corrugated stainless steel tubing, this will be determined according to resistance to pressure request, when selection corrugated stainless steel tubing good effect of heat exchange.Circulation
Fluid (103) sleeve pipe inner tube of heat exchanger (402), and external fluid sleeve pipe heat exchanger outer sleeve (401), mainly
Consider fluid and double-tube heat exchanger inner tube (402) fluid heat transfer that external fluid can be external with double-tube heat exchanger (110) simultaneously, changes
Heat area increases, and effect improves.
Claims (8)
1. the vehicle-mounted type thermal storage equipment that a kind of packaged type is used for energy storage, it is characterised in that: place accumulation of heat object in storage heater
Matter stores energy, and expansion tube is placed in two sides at the top of storage heater；Storage heater top center position is that electrical heating elements are passed directly to store
Hot device bottom；Tail end middle position is cylindrical groove at the top of storage heater, and cylindrical groove is partially submerged into storage heater, and cylindricality trench bottom is closed
It is isolated with storage heater fluid circulating inside；Circulating pump is installed in cylindrical groove；Circulation of fluid collecting pipe passes through cylindrical groove connection circulation
Pump intake；Circulating-pump outlet is connected with another pipeline for passing through cylindrical groove, which is connected with tube chamber in double-tube heat exchanger；Set
Heat exchange of heat pipe is snakelike, right angle setting, and straight pipe part intersects installation with electric heating tube；Tube chamber is another in double-tube heat exchanger
End is communicated with the fluid distributor of storage heater bottom；The import of double-tube heat exchanger outer sleeve and the outlet of double-tube heat exchanger outer sleeve
Pipeline passes through storage heater bottom and draws from accumulation of heat vehicle side or tail portion to be connected with the inlet and outlet of external fluid.
2. heat storage material as described in claim 1 includes solid ceramic heat-storing sphere, the accumulation of heat for encapsulating inorganic/organic phase change material
Ball and has between circulation of fluid and apparent density contrast and do not react immiscible organic matter in use temperature range.
3. fluid collector as described in claim 1 collects the main pipeline of fluid every a distance connecting branch, branch pipe
Head clearance certain distance opens 2 millimeters to 10 millimeters of diameter of diameter of hole to collect fluid.
4. fluid distributor as described in claim 1, fluid distributes main pipeline every on a distance connecting branch, branch pipe
Spaced apart symmetrically to open 2 millimeters to 10 millimeters of diameter of diameter of hole to distribute fluid, institute's aperture is with horizontal sextant angle range
15 degree to 90 degree.
5. expansion bottom of the tube needs to be higher than at the top of storage heater as described in claim 1.
6. double-tube heat exchanger as described in claim 1 be stainless steel material, outer sleeve may be selected stainless steel seamless pipe or
Person's corrugated stainless steel tubing.
7. fluid is external fluid, double-tube heat exchanger inner tube in double-tube heat exchanger outer sleeve cavity as described in claim 1
Fluid is storage heater fluid circulating.
8. circulation of fluid as described in claim 1, including water, fused salt, xylyl ether, hydrogenated terphenyl, organic silicone oil, connection
Benzene-biphenyl ether mixture, glycol water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810465946.3A CN110500908A (en) | 2018-05-16 | 2018-05-16 | A kind of mobile thermal storage equipment of vehicle-mounted type |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810465946.3A CN110500908A (en) | 2018-05-16 | 2018-05-16 | A kind of mobile thermal storage equipment of vehicle-mounted type |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110500908A true CN110500908A (en) | 2019-11-26 |
Family
ID=68584608
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810465946.3A Pending CN110500908A (en) | 2018-05-16 | 2018-05-16 | A kind of mobile thermal storage equipment of vehicle-mounted type |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110500908A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113446882A (en) * | 2021-06-24 | 2021-09-28 | 中国科学院广州能源研究所 | Heat storage type efficient compact heat exchanger |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201093907Y (en) * | 2007-07-05 | 2008-07-30 | 上海海事大学 | Novel phase change type heat tube heat accumulator |
| CN202378765U (en) * | 2011-07-29 | 2012-08-15 | 圣火科技(河南)有限责任公司 | Mobile heat accumulation vehicle capable of supplying steam and hot water |
| CN102829663A (en) * | 2012-08-16 | 2012-12-19 | 圣火科技(河南)有限责任公司 | Replaceable phase-change heat accumulator |
| CN206018776U (en) * | 2016-08-31 | 2017-03-15 | 天津道一节能科技有限公司 | Solar energy and electric energy synthesis storing energy and supplying hot system |
| CN206905600U (en) * | 2017-05-04 | 2018-01-19 | 西安交通大学 | A kind of mobile heat supply car using phase change heat storage balls |
| CN208333200U (en) * | 2018-05-16 | 2019-01-04 | 江苏瑞旭新能源科技有限公司 | A kind of vehicular thermal storage equipment |
-
2018
- 2018-05-16 CN CN201810465946.3A patent/CN110500908A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201093907Y (en) * | 2007-07-05 | 2008-07-30 | 上海海事大学 | Novel phase change type heat tube heat accumulator |
| CN202378765U (en) * | 2011-07-29 | 2012-08-15 | 圣火科技(河南)有限责任公司 | Mobile heat accumulation vehicle capable of supplying steam and hot water |
| CN102829663A (en) * | 2012-08-16 | 2012-12-19 | 圣火科技(河南)有限责任公司 | Replaceable phase-change heat accumulator |
| CN206018776U (en) * | 2016-08-31 | 2017-03-15 | 天津道一节能科技有限公司 | Solar energy and electric energy synthesis storing energy and supplying hot system |
| CN206905600U (en) * | 2017-05-04 | 2018-01-19 | 西安交通大学 | A kind of mobile heat supply car using phase change heat storage balls |
| CN208333200U (en) * | 2018-05-16 | 2019-01-04 | 江苏瑞旭新能源科技有限公司 | A kind of vehicular thermal storage equipment |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113446882A (en) * | 2021-06-24 | 2021-09-28 | 中国科学院广州能源研究所 | Heat storage type efficient compact heat exchanger |
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