CN105928407A - Sleeve phase change heat storage heat exchanger - Google Patents

Sleeve phase change heat storage heat exchanger Download PDF

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Publication number
CN105928407A
CN105928407A CN201610471822.7A CN201610471822A CN105928407A CN 105928407 A CN105928407 A CN 105928407A CN 201610471822 A CN201610471822 A CN 201610471822A CN 105928407 A CN105928407 A CN 105928407A
Authority
CN
China
Prior art keywords
circular
end cover
radiated rib
heat exchanger
standpipe
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201610471822.7A
Other languages
Chinese (zh)
Inventor
程友良
韩健
王月坤
杜尚任
渠江曼
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
North China Electric Power University
Original Assignee
North China Electric Power University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by North China Electric Power University filed Critical North China Electric Power University
Priority to CN201610471822.7A priority Critical patent/CN105928407A/en
Publication of CN105928407A publication Critical patent/CN105928407A/en
Pending legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D20/00Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
    • F28D20/02Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat
    • F28D20/021Heat 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24SSOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
    • F24S60/00Arrangements for storing heat collected by solar heat collectors
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/24Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00Energy generation through renewable energy sources
    • Y02E10/40Solar thermal energy, e.g. solar towers
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/14Thermal energy storage

Abstract

The invention discloses a sleeve phase change heat storage heat exchanger. The sleeve phase change heat storage heat exchanger comprises circular cooling fins, a vertical pipe, an upper end cover, a shell cylinder and a lower end cover. The plurality of circular cooling fins are vertically distributed at intervals and arranged on the periphery of the vertical pipe in a sleeving manner. The upper end cover is located above the circular cooling fins and fixedly connected with the upper end of the shell cylinder. The lower end cover is located below the circular cooling fins and fixedly connected with the lower end of the shell cylinder. The upper end of the vertical pipe penetrates the upper end cover and is fixedly connected with a through hole in the upper end cover. The lower end of the vertical pipe penetrates the lower end cover and is fixedly connected with a through hole of the lower end cover. According to the sleeve phase change heat storage heat exchanger, phase change materials are heated through cooling of the circular cooling fins on the periphery of the internal flow guide vertical pipe, and the sleeve phase change heat storage heat exchanger has the beneficial effects that the structure is simple, the heat exchange area is enlarged, and the overall heat storage and release efficiency is improved.

Description

A kind of casing tube phase-change regenerative heat exchanger
Technical field
The present invention relates to technical field of heat exchange, especially a kind of casing tube phase-change regenerative heat exchanger.
Background technology
Thermal storage and energy accumulation technology be the existing energy of Appropriate application regenerative resource and improve efficiency of energy utilization weight Want technology.Heat storage technology currently mainly includes that sensible heat accumulation of heat, latent-heat storage, chemical reaction accumulation of heat and phase transformation store Heat.Phase-transition heat-storage utilizes the phase-change materials such as paraffin, aliphatic acid, fuse salt exactly, when material undergoes phase transition Absorb or release heat and reach to store or the purpose that releases energy, due to the latent heat of material than sensible heat big very Many, and phase-change material keeps temperature constant, so phase-change heat storage technology has energy storage density when undergoing phase transition The advantages such as height, exothermic process temperature fluctuation range are little.In recent years, phase-transition heat-storage is widely used in solar heat The energy-saving field such as utilization, industrial afterheat recovery and heating air conditioning.In applying as thermal storage and energy accumulation technology, core sets Standby phase change thermal storage heat exchanger has various structures form, and phase change heat accumulator of the prior art, due to structure Design makes the thermal conductivity factor of phase-change material the most relatively low, and heat exchange area is less, causes overall heat release and storage The thermal efficiency is relatively low.
Summary of the invention
The technical problem to be solved is to provide a kind of casing tube phase-change regenerative heat exchanger, utilizes internal leading The circular radiated rib heat radiation of stream standpipe periphery, heats phase-change material, has simple in construction, heat exchange area Increase, improve overall accumulation of heat and the feature of exothermal efficiency.
The technical solution used in the present invention is:
A kind of casing tube phase-change regenerative heat exchanger, including circular radiated rib, standpipe, upper end cover, outer shell barrel and Bottom end cover;Described circular radiated rib has a periphery being sleeved on standpipe multiple and the most spaced apart, described on End cap is positioned at above circular radiated rib and fixes with the upper end of outer shell barrel and is connected, and described bottom end cover is positioned at circle Fixing below radiated rib and with the lower end of outer shell barrel and be connected, described standpipe upper end is through upper end cover and upper end The through hole of lid is fixing to be connected, and lower riser end is through bottom end cover and fixing with the through hole of bottom end cover is connected.
Above-mentioned casing tube phase-change regenerative heat exchanger, described circular radiated rib is provided with triangle pod apertures and circle Pod apertures, described triangle pod apertures is distributed on the circular radiated rib of standpipe periphery, described circular water conservancy diversion On the pore size distribution circular radiated rib outside triangle pod apertures.
Above-mentioned casing tube phase-change regenerative heat exchanger, described circular radiated rib is paraboloid of revolution shape radiated rib.
Above-mentioned casing tube phase-change regenerative heat exchanger, described circular radiated rib is flat board circular radiating fin.
Above-mentioned casing tube phase-change regenerative heat exchanger, described circular radiated rib has two kinds, is positioned at the circle of riser upper Shape radiated rib is paraboloid of revolution shape radiated rib, and the circular radiated rib being positioned at standpipe bottom is flat board ring Shape radiated rib, the quantity of described paraboloid of revolution shape radiated rib is more than flat board circular radiating fin.
Above-mentioned casing tube phase-change regenerative heat exchanger, sets up communicating pipe, on upper end cover and bottom end cover respectively fixing even Siphunculus, described communicating pipe and outer shell barrel intracavity inter-connection, the external port of communicating pipe is provided with sealing lid.
The casing tube phase-change regenerative heat exchanger that the present invention provides, installs circular radiated rib, increases in standpipe periphery Add area of dissipation, the circular radiated rib of standpipe periphery arranged triangle pod apertures and circular pod apertures, Circular radiated rib arranges triangle pod apertures and circular pod apertures, Main Function are: paraffin is melting Time, solid-liquid confusion region can be there is between solid phase and liquid phase, the solidliquid mixture in solid-liquid confusion region is due to gravity Effect can slowly flow downward, have after circular radiated rib arranges triangle pod apertures and circular pod apertures Help the flowing of solidliquid mixture, i.e. enhance the free convection in phase change region.Meanwhile, rotation is used to throw Object plane shape radiated rib not perforate, when filling paraffin in outer shell barrel inner chamber, paraboloid of revolution shape cooling fin A lot of air can be remained on the downside of sheet, cause paraffin cannot fill up outer shell barrel inner chamber, so, fin perforate is favourable Filling in paraffin.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention;
Fig. 2 is the B-B sectional view in Fig. 1.
In figure, each label is expressed as: standpipe 1, upper end cover 2, outer shell barrel 3, outer shell barrel inner chamber 4, bottom end cover 5, communicating pipe 6, flat board circular radiating fin 7, triangle pod apertures 8, circular pod apertures 9, rotary parabolic Face shape radiated rib 10.
Detailed description of the invention
See Fig. 1,2.High temperature heat exchanging fluid can use the hot water of solar water heater, heat accumulating phase change material Optional paraffin, aliphatic acid or fuse salt, the heat accumulating phase change material of preferred version is paraffin, is stored by paraffin At inner sleeve inner chamber 4.Solar water is entered by standpipe 1 upper port, flows out from standpipe 1 lower port, opens During the beginning, the paraffin in outer shell barrel inner chamber 4 is solid-state, and solar water flows on the one hand heating paraffin wax, the opposing party Face transfers heat to paraffin by standpipe 1, and paraffin gradually melts, when paraffin melts completely after absorbing heat Time, i.e. completing the heat-accumulating process of phase change thermal storage heat exchanger, heat is just stored in paraffin with the form of latent heat. The reason of employing paraboloid of revolution shape radiated rib 10 is, first can from Unit Weight heat dissipation capacity optimality analysis Knowing, under certain heat dissipation capacity, the cross section molded line of optimum fin should be paraboloid of revolution shape;Additionally, due to shell Phase-change material gravity and the effect of free convection in tube inner chamber 4, along flow axes direction, phase change region Thermograde layer thickness constantly increases, and then expands to whole phase change region, and Isothermal Line Distribution is become by sparse Intensive, the temperature of upper end is higher than lower end, and now, the optimum shape of fin should be along the side of thermograde maximum To, use paraboloid of revolution shape radiated rib 10 maximal efficiency fin can be utilized to dispel the heat.
The circular radiated rib being positioned at standpipe 1 top is paraboloid of revolution shape radiated rib 10, is positioned at standpipe 1 The circular radiated rib of bottom is flat board circular radiating fin 7, the quantity of paraboloid of revolution shape radiated rib 10 More than flat board circular radiating fin 7.This scheme can with the heat exchange efficiency bottom stiffened shell tube inner chamber 4, Because generally the paraffin melting speed bottom outer shell barrel inner chamber 4 is the slowest.
Upper end cover 2 and bottom end cover 5 fix communicating pipe 6 respectively, multiple heat exchangers can be used in series, Increase the power of heat exchanger.
The present invention can be as the regenerative apparatus of solar energy thermal-power-generating, and phase-change material can use paraffin or molten Melt salt etc..As a example by solar energy thermal-power-generating hold over system, water is as low-temperature heat exchange fluid, through solar energy collection Thermal field is heated to be high temperature heat exchanging fluid, and major part high temperature fluid enters steam generator and produces steam for sending out Electricity, when solar energy resources is more rich, small part high temperature heat exchanging fluid flows into this phase change thermal storage heat exchanger, Heat exchanging fluid transfers heat to phase-change material, with the form of latent heat by heat storage in phase-change material, treat When needing to use, completing heat exchange low-temperature heat exchange fluid pumps into this heat exchanger, cryogen is heated After high temperature fluid, high temperature fluid produces steam through steam generator and is used for generating electricity.So, solar heat The impact that solar energy thermal-power-generating is brought by Changes in weather just can be independently tackled in generating, even completes power peak regulation Etc. task.

Claims (6)

1. a casing tube phase-change regenerative heat exchanger, it is characterised in that: include circular radiated rib, standpipe (1), upper end Lid (2), outer shell barrel (3) and bottom end cover (5);Described circular radiated rib has multiple and the most spaced apart Being sleeved on the periphery of standpipe (1), described upper end cover (2) is positioned at above circular radiated rib and and outer shell barrel (3) upper end is fixing to be connected, described bottom end cover (5) be positioned at below circular radiated rib and with outer shell barrel (3) Lower end fixing connect, described standpipe (1) upper end passes upper end cover (2) the through hole with upper end cover (2) Fixing connecting, standpipe (1) lower end is through bottom end cover (5) and fixing with the through hole of bottom end cover (5) is connected.
A kind of casing tube phase-change regenerative heat exchanger the most according to claim 1, it is characterised in that: described circular heat radiation Fin is provided with triangle pod apertures (8) and circular pod apertures (9), described triangle pod apertures (8) point Cloth is on the circular radiated rib of standpipe (1) periphery, and described circular pod apertures (9) is distributed in triangle and leads On the circular radiated rib of discharge orifice (8) outside.
A kind of casing tube phase-change regenerative heat exchanger the most according to claim 2, it is characterised in that: described circular heat radiation Fin is paraboloid of revolution shape radiated rib (10).
A kind of sleeve pipe radiated rib heat exchanger the most according to claim 2, it is characterised in that: described circular heat radiation Fin is flat board circular radiating fin (7).
A kind of casing tube phase-change regenerative heat exchanger the most according to claim 2, it is characterised in that: described circular heat radiation Fin has two kinds, and the circular radiated rib being positioned at standpipe (1) top is paraboloid of revolution shape radiated rib (10), The circular radiated rib being positioned at standpipe (1) bottom is flat board circular radiating fin (7), the described paraboloid of revolution The quantity of shape radiated rib (10) is more than flat board circular radiating fin (7).
6. according to a kind of casing tube phase-change regenerative heat exchanger described in claim 3,4 or 5, it is characterised in that: set up Communicating pipe (6), upper end cover (2) and bottom end cover (5) fix communicating pipe (6), described connection respectively Pipe (6) is connected with outer shell barrel inner chamber (4), and the external port of communicating pipe (6) is provided with sealing lid.
CN201610471822.7A 2016-06-25 2016-06-25 Sleeve phase change heat storage heat exchanger Pending CN105928407A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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Publications (1)

Publication Number Publication Date
CN105928407A true CN105928407A (en) 2016-09-07

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Country Status (1)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106225542A (en) * 2016-09-12 2016-12-14 重庆大学 A kind of active solid-liquid phase change material recuperated cycle system
CN106247434A (en) * 2016-09-23 2016-12-21 四川大学 A kind of based on phase-change accumulation energy and structure-integrated solar heating prefabricated panel
CN108775829A (en) * 2018-07-17 2018-11-09 南京工业大学 A kind of rotatable jacket type phase-change accumulation energy storage heater
CN111121512A (en) * 2020-02-24 2020-05-08 中国科学院理化技术研究所 Solid phase cold accumulator
CN113340137A (en) * 2021-06-08 2021-09-03 西安交通大学 Quick heat-retaining module that disturbance mixes

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106225542A (en) * 2016-09-12 2016-12-14 重庆大学 A kind of active solid-liquid phase change material recuperated cycle system
CN106225542B (en) * 2016-09-12 2018-01-09 重庆大学 A kind of active solid-liquid phase change material recuperated cycle system
CN106247434A (en) * 2016-09-23 2016-12-21 四川大学 A kind of based on phase-change accumulation energy and structure-integrated solar heating prefabricated panel
CN108775829A (en) * 2018-07-17 2018-11-09 南京工业大学 A kind of rotatable jacket type phase-change accumulation energy storage heater
CN111121512A (en) * 2020-02-24 2020-05-08 中国科学院理化技术研究所 Solid phase cold accumulator
CN113340137A (en) * 2021-06-08 2021-09-03 西安交通大学 Quick heat-retaining module that disturbance mixes
CN113340137B (en) * 2021-06-08 2024-01-26 西安交通大学 Disturbance mixed rapid heat storage module

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Application publication date: 20160907