WO2019113846A1 - Power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery - Google Patents

Power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery Download PDF

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Publication number
WO2019113846A1
WO2019113846A1 PCT/CN2017/115990 CN2017115990W WO2019113846A1 WO 2019113846 A1 WO2019113846 A1 WO 2019113846A1 CN 2017115990 W CN2017115990 W CN 2017115990W WO 2019113846 A1 WO2019113846 A1 WO 2019113846A1
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WO
WIPO (PCT)
Prior art keywords
gas
liquid
heat dissipation
heat
battery system
Prior art date
Application number
PCT/CN2017/115990
Other languages
French (fr)
Chinese (zh)
Inventor
许可勤
胡剑平
黄骏
毛小飞
Original Assignee
深圳市海梁科技有限公司
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Publication of WO2019113846A1 publication Critical patent/WO2019113846A1/en

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Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/61Types of temperature control
    • H01M10/613Cooling or keeping cold
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/63Control systems
    • H01M10/637Control systems characterised by the use of reversible temperature-sensitive devices, e.g. NTC, PTC or bimetal devices; characterised by control of the internal current flowing through the cells, e.g. by switching
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/65Means for temperature control structurally associated with the cells
    • H01M10/655Solid structures for heat exchange or heat conduction
    • H01M10/6554Rods or plates
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/65Means for temperature control structurally associated with the cells
    • H01M10/655Solid structures for heat exchange or heat conduction
    • H01M10/6556Solid parts with flow channel passages or pipes for heat exchange
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/65Means for temperature control structurally associated with the cells
    • H01M10/656Means for temperature control structurally associated with the cells characterised by the type of heat-exchange fluid
    • H01M10/6569Fluids undergoing a liquid-gas phase change or transition, e.g. evaporation or condensation
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2220/00Batteries for particular applications
    • H01M2220/20Batteries in motive systems, e.g. vehicle, ship, plane
    • 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
    • Y02E60/10Energy storage using batteries

Definitions

  • the invention is applicable to the technical field of vehicles, and more particularly to a power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery.
  • the natural heat dissipation method refers to the purpose of dissipating the heat of the power battery by the convection or heat of the external air to achieve heat dissipation.
  • This kind of heat dissipation method requires that the power battery charge and discharge rate is very low, resulting in low output power of the power battery, low heat dissipation efficiency, which is not conducive to popularization;
  • Air cooling and heat dissipation means that cold air is sent to the power through a fan or the like. The battery gap, which takes away the heat generated by the power battery.
  • the liquid cooling method refers to the heat band of the power battery through the cooling unit and the water cooling circuit. go.
  • the structure of the heat dissipation method is complicated, and if the power of the power battery pack is large, the requirements for the cooling system are high.
  • the heat dissipation method of the power battery has the problem of poor heat dissipation, and the heat of the power battery is directly discharged through the heat dissipation device, which not only causes pollution to the environment, but also has low energy utilization rate.
  • the object of the present invention is to provide a power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery, so as to solve the problem of low heat dissipation efficiency and waste of energy of the power battery existing in the prior art.
  • the technical solution adopted by the present invention is to provide a power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery, comprising a box body and a plurality of batteries disposed in the box body, the cabinet body being installed a plurality of liquid-gas conversion sheets for absorbing heat generated by each of the batteries, wherein each of the liquid-gas conversion sheets is provided with a storage space for storing a refrigerant, and each of the liquid-gas conversion sheets has a liquid inlet at a lower end thereof.
  • the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery further includes a gas current collector for collecting gas discharged from each of the liquid-gas conversion sheets, a gas-liquid converter that converts the gas collector exhaust gas into a liquid and a thermoelectric power generation piece that converts heat dissipated by the gas current collector into electric energy, the thermoelectric power generation sheet being attached to the gas current collector
  • a gas current collector for collecting gas discharged from each of the liquid-gas conversion sheets
  • a gas-liquid converter that converts the gas collector exhaust gas into a liquid
  • a thermoelectric power generation piece that converts heat dissipated by the gas current collector into electric energy
  • thermoelectric power generation sheet a heat sink for dissipating heat from the thermoelectric power generation sheet is further included, and the heat sink and the gas current collector cooperate to clamp the thermoelectric power generation sheet.
  • a communication pipe that communicates with each of the liquid inlets is further included, and the communication pipe is connected to an outlet of the gas-liquid converter.
  • a gas collecting pipe connecting each of the exhaust ports is further included, and the gas collecting pipe is connected to an inlet of the gas current collector.
  • the gas-liquid converter includes a liquid storage tank, and a bottom surface of the liquid storage tank is installed with an outlet pipe connecting each of the liquid inlets, and a side of the liquid storage tank is installed to communicate the gas current collection The intake pipe of the device.
  • a top surface of the liquid storage tank is provided with a liquid injection port, and the gas-liquid converter further includes a sealing cover covering the liquid injection opening.
  • the gas-liquid converter further includes a plurality of fins mounted on the liquid tank.
  • liquid-gas conversion sheet is provided with a partition plate that divides the storage space into a plurality of vertical DC channels.
  • the gas current collector includes a gas collecting box, and two sides of the gas collecting box are respectively provided with an inlet pipe and an outlet pipe, and the gas collecting box is provided with the inlet pipe and the outlet pipe. Bend the flow path.
  • the curved flow channel is laid in the gas collecting box in an S shape.
  • the utility model provides a power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery, which has the beneficial effects that the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery is provided in the cabinet body more than the prior art.
  • the liquid-gas conversion sheet, the liquid refrigerant in each liquid-gas conversion sheet is vaporized under the action of the high temperature of the battery, thereby absorbing the heat generated by the battery, and the heat dissipation effect of the battery is good.
  • the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery is further provided with a gas current collector, a gas-liquid converter and a thermoelectric power generation piece attached to the gas current collector,
  • the gas-liquid converter can be a gaseous refrigerant Re-converted to liquid refrigerant, the refrigerant can be recycled;
  • the thermoelectric sheet can convert the heat of the battery into electric energy, which is convenient for energy reuse. Therefore, the invention not only has good heat dissipation effect on the battery, but also the refrigerant can be repeatedly used, the heat of the battery can also be converted into electric energy, the energy is recycled, and the energy utilization rate is high.
  • FIG. 1 is a schematic structural diagram of a power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery according to an embodiment of the present invention
  • FIG. 2 is an exploded view of a power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery according to an embodiment of the present invention
  • FIG. 3 is a top plan view of an interior of a cabinet according to an embodiment of the present invention.
  • FIG. 4 is a front view of a liquid-gas conversion sheet according to an embodiment of the present invention.
  • Figure 5 is a cross-sectional view taken along line A-A of Figure 4.
  • FIG. 6 is a schematic structural diagram of a gas-liquid converter according to an embodiment of the present invention.
  • Figure 7 is a cross-sectional view of a gas current collector according to an embodiment of the present invention.
  • FIG. 8 is a schematic structural diagram of a thermoelectric power generation chip according to an embodiment of the present invention.
  • 3-liquid-gas conversion sheet 31-storage space; 32-inlet port; 33-exhaust port; 34-spacer plate;
  • 6-gas-liquid converter 61-injection port; 62-sealing cap; 63-outlet pipe; 64-intake pipe; 65-heat sink; 66-level indicator; 67-tank;
  • 8-temperature difference power generation sheet 8-temperature difference power generation sheet; 81-hot sheet; 82-cold sheet; 83-P type semiconductor; 84-N type semiconductor; 85-positive output terminal; 86-negative output terminal;
  • first and second are used for descriptive purposes only and are not to be construed as indicating or implying a relative importance or implicitly indicating the number of technical features indicated.
  • features defining “first” and “second” may include one or more of the features either explicitly or implicitly.
  • the meaning of "a plurality” is two or more unless specifically and specifically defined otherwise.
  • connection In the description of the present invention, it should be noted that the terms “installation”, “connected”, and “connected” are to be understood broadly, and may be fixed or detachable, for example, unless otherwise explicitly defined and defined. Connected, or integrally connected; may be mechanically connected or electrically connected; may be directly connected, or may be indirectly connected through an intermediate medium, may be internal communication of two elements or an interaction relationship of two elements. For those skilled in the art, the specific meanings of the above terms in the present invention can be understood on a case-by-case basis.
  • the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery includes a casing 1 and a plurality of batteries 2 disposed in the casing 1, and each of the liquid-gas conversion sheets 3 and the respective batteries 2 are alternately distributed.
  • the battery 2 may have any shape such as a circle or a square.
  • a battery 2 is disposed between two adjacent liquid-gas conversion sheets 3, and the contact surfaces of each of the liquid-gas conversion sheets 3 and the battery 2 are coated with a thermal conductive silica gel to reduce thermal resistance, and two of the batteries 2 are respectively The sides can be covered by the liquid-gas conversion sheet 3, so that the heat dissipation effect of each of the batteries 2 is good, and the temperature between the batteries 2 has a good consistency.
  • a plurality of liquid-gas conversion sheets 3 for absorbing heat generated by the plurality of batteries 2 are disposed in the casing 1, and each of the liquid-gas conversion sheets 3 is provided with a storage space 31 for storing the refrigerant.
  • the refrigerant is an organic mixture
  • the boiling point of the refrigerant is 37-45 °C.
  • the refrigerant is a mixture of ethanol having a mass fraction of 6%, cyclopentane having a mass fraction of 91%, and an antiknock agent having a mass fraction of 3%, the boiling point of the mixture being 44.7 ° C; or, the refrigerant is A mixture of 6.2% methanol, 91.8% by mass of methylene chloride and 2% by mass of antiknock agent having a boiling point of 37.8 °C.
  • a liquid inlet 32 is opened at a lower end of one side of each of the liquid-gas conversion sheets 3, and an exhaust port 33 is opened at an upper end of each of the opposite sides of each of the liquid-gas conversion sheets 3.
  • the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery further includes a gas current collector 7, a gas-liquid converter 6, and a thermoelectric power generation sheet 8 attached to the gas current collector 7.
  • the inlet of the gas-liquid converter 6 and the outlet of the gas collector 7 are communicated through the third connecting pipe 12, and the inlet of the gas current collector 7 communicates with each of the exhaust ports 33 through the second connecting pipe 11, the gas-liquid converter
  • the outlet of 6 communicates with each of the inlet ports 32 through the first connecting pipe 10.
  • the gas current collector 7 collects the gas discharged from the plurality of liquid-gas conversion sheets 3, and transfers the heat of the gas to the thermoelectric power generation sheet 8, which converts the heat into electric energy and stores it.
  • the gas-liquid converter 6 can re-convert the gas discharged from the gas collector 7 into a liquid.
  • the liquid-gas conversion sheet 3 and the gas-liquid converter 6 are preferably made of an aluminum alloy or a copper alloy material.
  • the refrigerant may also be other organic mixtures according to actual needs; the liquid-gas conversion sheet 3 and the gas-liquid converter 6 may also be made of other materials having good heat conductivity, which are not limited herein.
  • the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery has a plurality of liquid gases disposed in the casing 1 in the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery compared with the prior art.
  • the liquid refrigerant in each of the liquid-gas conversion sheets 3 is vaporized by the high temperature of the battery 2, thereby absorbing the heat generated by the battery 2, and the heat dissipation effect of the battery 2 is good.
  • the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery is further provided with a gas current collector 7, a gas-liquid converter 6, and a thermoelectric power generation sheet 8 attached to the gas current collector 7, the gas-liquid converter 6
  • the gaseous refrigerant can be reconverted into a liquid refrigerant, and the refrigerant can be recycled; the thermoelectric power generation sheet 8 can convert the heat of the battery 2 into electric energy, thereby facilitating the reuse of energy. Therefore, the invention not only has good heat dissipation effect on the battery 2, but also the refrigerant can be repeatedly used, the heat of the battery 2 can also be converted into electric energy, the energy is recycled, and the energy utilization rate is high.
  • FIG. 1 and FIG. 8 together as a specific embodiment of a power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery provided by the present invention, which is based on gas-liquid two-phase heat dissipation and heat energy recovery.
  • the battery system further includes a heat sink 9 for dissipating heat from the thermoelectric power generation sheet 8, and the heat sink 9 and the gas current collector 7 cooperate to sandwich the thermoelectric power generation sheet 8.
  • a thermoelectric power generation sheet 8 for converting heat of the battery 2 into electric energy is disposed on one side of the gas current collector 7, and is disposed on the opposite side of the thermoelectric power generation sheet 8 for heat dissipation.
  • Radiator 9 is preferably made of a material having a high thermal conductivity such as an aluminum alloy or a copper alloy. In other embodiments, the heat sink 9 can also be made of other materials having excellent thermal conductivity, which is not limited herein.
  • the thermoelectric power generation sheet 8 includes a heat sheet 81 and a cold sheet 82.
  • the hot sheet 81 and the cold sheet 82 are preferably made of a material having good thermal conductivity such as an aluminum alloy or a copper alloy.
  • a plurality of P-type semiconductors 83 and a plurality of N-type semiconductors 84 are alternately arranged between the hot sheet 81 and the cold sheet 82.
  • the thermoelectric power generation sheet 8 further includes a positive output terminal for supplying power to a battery (not shown). 85 and negative output 86.
  • the voltage of the battery is preferably 24V.
  • thermoelectric power generation sheet 8 is bonded to the gas current collector 7, and the cold sheet 82 of the thermoelectric power generation sheet 8 is bonded to the heat sink 9.
  • Two adjacent P-type semiconductors 83 and N-type semiconductors 84 are connected by a metal made of an excellent thermal conductive material such as an aluminum alloy or a copper alloy to form a PN junction, and a plurality of PN sections are connected in parallel or in series, and the positive output is
  • the terminal 85 and the negative output terminal 86 are disposed on the P-type semiconductor 83 or the N-type semiconductor 84.
  • the contact faces of the gas current collector 7 and the thermoelectric power generation sheet 8 are made of a thermally conductive metal material, and the other sides of the gas current collector 7 are made of a heat insulating material.
  • the metal material is preferably an aluminum alloy or a copper alloy.
  • the gaseous refrigerant from the liquid-gas conversion sheet 3 with a large amount of heat enters the gas collector 7, and the gas collector 7 transfers the heat to the hot sheet 81 of the thermoelectric power generation sheet 8, in the radiator 9 and the air Under the action of heat transfer, a temperature gradient is generated between the hot sheet 81 of the thermoelectric power generation sheet 8 and the cold sheet 82, and the Seebeck effect is a voltage difference between two substances due to temperature differences between two different electrical conductors or semiconductors.
  • the thermal energy is converted into electric energy by the P-type semiconductor 83, the N-type semiconductor 84 and the PN junction, and the electric energy is stored in the storage battery through the positive output terminal 85 and the negative output terminal 86, so that the heat energy of the battery 2 is recovered.
  • the hot sheet 81 and the cold sheet 82 may also be made of other materials having excellent thermal conductivity; the voltage of the battery may also be other values, which is not limited herein.
  • the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery As a specific implementation manner of the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery provided by the present invention, the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery
  • the communication pipe 4 that connects the respective liquid inlets 32 is connected, and the communication pipe 4 is connected to the outlet of the gas-liquid converter 6.
  • the gas-liquid converter 6 has a function of replenishing and storing a liquid refrigerant.
  • the liquid refrigerant in the gas-liquid converter 6 flows out from the outlet of the gas-liquid converter 6, and follows the first connecting pipe 10 and the connecting pipe 4
  • the liquid inlet 32 of the liquid-gas conversion sheet 3 flows into the storage space 31 of each liquid-gas conversion sheet 3, the liquid refrigerant vaporizes under the high temperature released by the battery 2, the liquid refrigerant is converted into a gaseous refrigerant, and the battery 2 is absorbed.
  • the large amount of heat, the gaseous refrigerant carrying a large amount of heat is discharged from the exhaust port 33 of the liquid-gas conversion sheet 3, thereby achieving the effect of lowering the temperature of the battery 2, and the heat dissipation effect of the battery 2 is good.
  • the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery As a specific implementation manner of the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery provided by the present invention, the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery A gas collecting pipe 5 is connected to each of the exhaust ports 33, and the gas collecting pipe 5 is connected to the inlet of the gas current collector 7.
  • the gaseous refrigerant carrying a large amount of heat is discharged from the exhaust port 33 of the liquid-gas conversion sheet 3, and enters the gas current collector 7 along the gas collecting pipe 5 and the second connecting pipe 11, and the gas current collector 7 transfers heat.
  • the temperature difference power generating sheet 8 is given, and under the heat transfer action of the heat sink 9 and the air, a temperature gradient is generated between the hot sheet 81 of the thermoelectric power generation sheet 8 and the cold sheet 82, and the heat energy is converted into electric energy by the Seebeck effect.
  • the electric energy is stored in the battery through the positive output terminal 85 and the negative output terminal 86. Therefore, the thermal energy of the battery 2 can be converted into electric energy, the energy can be reused, and the energy utilization rate is high.
  • the gas-liquid converter 6 includes a liquid storage tank 67, the liquid storage tank An outlet pipe 63 that connects each of the liquid inlets 32 is attached to the bottom surface of the liquid storage port 67, and an intake pipe 64 that communicates with the gas current collector 7 is attached to the side surface of the liquid storage tank 67.
  • the reservoir 67 has a function of storing a liquid refrigerant.
  • the liquid injection pipe 63 communicates with the communication pipe 4 through the first connecting pipe 10, and the intake pipe 64 communicates with the gas current collector 7 through the second connecting pipe 11, so that the liquid-gas conversion sheet 3, the gas current collector 7, and the gas can be
  • the liquid converter 6 is in communication.
  • the liquid refrigerant stored in the liquid storage tank 67 flows into the liquid-gas conversion sheet 3, and the liquid refrigerant vaporizes into a gaseous refrigerant, and absorbs the heat of the battery 2.
  • the gaseous refrigerant carrying a large amount of heat enters the gas current collector 7, and converts the heat of the battery 2 into electric energy storage under the action of the thermoelectric power generation sheet 8 and the heat sink 9, and the gaseous refrigerant enters the liquid storage tank 67 and is liquefied.
  • the gaseous refrigerant is reconverted to a liquid refrigerant. Therefore, the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery can not only convert the heat energy of the battery 2 into electric energy, but also the refrigerant can be reused, and the energy utilization rate is high.
  • the outlet tube 63 and the inlet tube 64 may also be disposed at other locations, which are not limited herein.
  • the bottom surface of the reservoir tank 67 is higher than the surface of the liquid-gas conversion sheet 3.
  • the liquid refrigerant in the reservoir tank 67 flows into the liquid-gas conversion sheet 3 through the outlet pipe 63. Since the bottom surface of the reservoir tank 67 is higher than the surface of the liquid-gas conversion sheet 3, the pressure in the reservoir tank 67 is high. It is higher than the pressure in the liquid-gas conversion sheet 3, and under the action of the pressure difference, the liquid refrigerant can fill the entire liquid-gas conversion sheet 3, and the liquid refrigerant can cover both sides of the battery 2, thereby facilitating the improvement of the battery 2 The amount of heat absorbed, thereby improving the heat dissipation efficiency of the battery 2.
  • FIG. 6 a specific embodiment of the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery provided by the present invention.
  • the top surface of the liquid storage tank 67 is provided with a liquid injection port 61.
  • the liquid exchanger 6 also includes a sealing cover 62 that covers the liquid inlet 61.
  • the liquid injection port 61 is for adding a liquid refrigerant to the liquid storage tank 67, so that the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery can operate normally.
  • the sealing cover 62 functions to seal the liquid filling port 61.
  • the sealing cover 62 prevents overflow and leakage of the gaseous refrigerant, thereby improving energy usage.
  • the liquid inlet 61 can also be disposed at other locations, which is not limited herein.
  • a liquid level indicator 66 for monitoring the refrigerant is provided in the reservoir tank 67.
  • the alarm device (not shown) issues an alarm to remind the user to add the refrigerant, thereby contributing to improving the heat dissipation efficiency of the battery 2 and improving Safety of use of power battery systems based on gas-liquid two-phase heat dissipation and heat recovery.
  • the level indicator 66 can also be disposed at other locations, which is not uniquely limited herein.
  • the gas-liquid converter 6 further includes a liquid storage tank 6 mounted on the liquid storage tank 67.
  • a plurality of fins 65 When the gaseous refrigerant flows out of the gas current collector 7 and enters the liquid storage tank 67, the temperature in the liquid storage tank 67 is lowered by the action of the plurality of fins 65, and the gaseous refrigerant is liquefied, and the gaseous refrigerant is converted into a liquid state. Refrigerant, so as to achieve the purpose of refrigerant recycling, thereby increasing energy reuse rate and saving energy.
  • the fins 65 may also be disposed at other locations of the reservoir 67, which are not specifically limited herein.
  • the liquid-gas conversion sheet 3 is provided with the storage space 31 divided into several A spacer plate 34 of a vertical DC channel.
  • the partition plate 34 can slow down the rate at which the liquid refrigerant fills the liquid-gas conversion sheet 3, absorbs the heat of the battery 2 for the liquid refrigerant, and provides sufficient time for vaporization to convert into a gaseous refrigerant, thereby improving the vaporization efficiency of the liquid refrigerant;
  • the partition plate 34 has a contact surface in which the respective liquid-gas conversion sheets 3 are attached to the corresponding battery 2 in a harmonica tubular shape.
  • the heat generated by the battery 2 is transferred to the liquid-gas conversion sheet 3 through the tubular spacer 34 of the harmonica, and not only the liquid refrigerant in the storage space 31 can be vaporized, but also the liquid refrigerant can be converted into a gaseous refrigerant.
  • Capillary action refers to the phenomenon that the immersion liquid rises in the thin tube and the non-wetting liquid descends in the thin tube
  • the liquid refrigerant can smoothly flow in the partition plate 34, and the bottom surface of the liquid storage tank 67 is high
  • the liquid refrigerant can be filled with the entire liquid-gas conversion sheet 3, thereby achieving a good heat dissipation effect.
  • the contact surface may also be in other configurations, which is not limited herein.
  • the gas current collector 7 includes a gas collection box 71, and the gas collection box An inlet pipe 72 and an outlet pipe 73 are respectively disposed on both sides of the 71, and the gas collecting box 71 is provided with a curved flow passage 74 communicating with the inlet pipe 72 and the outlet pipe 73.
  • the two sides of the gas collector 7 are respectively provided with an inlet pipe 72 communicating with the gas collecting pipe 5 through the second connecting pipe 11 and an inlet pipe 64 communicating with the gas-liquid converter 6 through the third connecting pipe 12
  • the outlet pipe 73 and the gas current collector 7 are provided with a curved flow path 74 for transferring the refrigerant.
  • the gaseous refrigerant having a large amount of heat of the battery 2 enters the gas collecting box 71 through the inlet pipe 72, and the curved flow path 74 is preferably laid in the gas collecting box 71 in an S-shape, so that the gaseous refrigerant can be increased through the gas current collector 7.
  • the length of the route facilitates the transfer of a large amount of thermal energy carried by the gaseous refrigerant to the thermoelectric power generation sheet 8, thereby improving the heat transfer efficiency, thereby improving the efficiency of converting thermal energy into electrical energy and improving energy conversion efficiency.
  • the curved flow path 74 can also be configured in other configurations, which is not limited herein.
  • the specific operation flow of the present invention is as follows: the liquid refrigerant is injected into the liquid storage tank 67 from the liquid injection port 61 of the gas-liquid converter 6, and after the liquid filling is completed, the liquid filling port 61 is sealed by the sealing cover 62. Since the bottom surface of the liquid storage tank 67 is higher than the surface of the liquid-gas conversion sheet 3, the liquid refrigerant passes through the first connecting pipe 10, the communication pipe 4, and the liquid inlet 32 under the pressure difference and the capillary action of the harmonical tubular spacer 34.
  • the heat generated by the battery 2 vaporizes and converts the liquid refrigerant into a gaseous refrigerant, and the heat generated by the battery 2 is absorbed in the process of converting the liquid from the liquid state to the gaseous state, and the gaseous refrigerant is from the liquid gas.
  • the exhaust port 33 of the conversion sheet 3 is discharged, and the gaseous refrigerant enters the gas current collector 7 through the gas collecting pipe 5, the second connecting pipe 11 and the inlet pipe 72 of the gas current collector 7, and the large amount of the battery which the gaseous refrigerant will carry 2
  • the generated heat is transferred to the heat sheet 81 of the thermoelectric power generation sheet 8, and under the heat transfer action of the heat sink 9 and the air, a temperature gradient is generated between the heat sheet 81 of the thermoelectric power generation sheet 8 and the cold sheet 82, and in the Seebeck effect Under the action, the thermal energy is converted into electric energy, and the electric energy is stored in the storage battery through the positive output terminal 85 and the negative output terminal 86.
  • the gaseous refrigerant is discharged from the outlet pipe 73 of the gas collector 7, passes through the third connecting pipe 12 and the intake pipe 64 of the gas-liquid converter 6, enters the gas-liquid converter 6, and is subjected to the heat transfer of the fins 65 and the air.
  • the gaseous refrigerant liquefies and is converted into a liquid refrigerant.
  • the communication tube 4, the air collection tube 5, the first connection tube 10, the second connection tube 11 and the third connection tube 12 are all made of a plastic material having a low thermal conductivity to prevent heat loss. In other embodiments, other materials having a lower thermal conductivity may also be made.
  • the gas-liquid conversion sheet 6, the heat sink 65, the gas current collector 7, the thermoelectric power generation sheet 8, and the heat sink 9 are all disposed outside the casing 1, and are disposed in a well-ventilated place.
  • the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery can be used for heat dissipation treatment of the battery 2, and is particularly suitable for a high-power power battery, and has good heat dissipation effect, and can also convert the heat generated by the battery 2 into Energy, energy can be recycled to improve energy utilization.
  • the refrigerant can be converted from a liquid state to a gaseous state, and then from a gaseous state to a liquid state, so that the refrigerant can be reused, further improving the energy use efficiency and saving the use cost.

Abstract

Disclosed is a power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery, comprising a case (1) and a plurality of batteries (2), with a plurality of liquid-to-gas conversion plates (3) being mounted in the case (1); and further comprising a gas collector (7), a vapor-to-liquid converter (6), and a temperature-difference power generation plate (8), wherein an inlet of the vapor-to-liquid converter (6) is in communication with an outlet of the gas collector (7), an inlet of the gas collector (7) is in communication with each vent (33), and an outlet of the gas-to-liquid converter (6) is in communication with each liquid inlet (32). Each liquid-to-gas conversion plate (3) absorbs the heat produced by the batteries (2), so that the batteries (2) have a good heat dissipation effect; the vapor-to-liquid converter (6) can convert a gaseous refrigerant into a liquid refrigerant, so that the refrigerant can be recycled; and the temperature-difference power generation plate (8) can convert the heat from the batteries (2) into electric energy. Therefore, the above-mentioned system is not only beneficial for the heat dissipation effect of the batteries (2), but also allows the refrigerant and heat energy to be recycled, so that the energy utilization rate is also high.

Description

基于气液两相散热及热能回收的动力电池系统Power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery 技术领域Technical field
本发明适用于车辆技术领域,更具体地说,是涉及一种基于气液两相散热及热能回收的动力电池系统。The invention is applicable to the technical field of vehicles, and more particularly to a power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery.
背景技术Background technique
随着石油资源的枯竭和日益增加的环保压力,用新能源车辆替代传统的燃油车,成为社会发展的必然趋势。目前,新能源车辆是通过动力电池的电能驱动车辆行驶。但是动力电池在充放电的过程中会产生大量的热量,若不能及时地将动力电池产生的热量排出,不仅严重影响动力电池的使用寿命,而且动力电池可能会因为热量过高而发生爆炸、燃烧等现象,从而引起严重的安全问题。With the depletion of petroleum resources and increasing environmental protection pressure, replacing traditional fuel vehicles with new energy vehicles has become an inevitable trend of social development. At present, new energy vehicles drive vehicles through the power of the power battery. However, the power battery generates a large amount of heat during charging and discharging. If the heat generated by the power battery cannot be discharged in time, it not only seriously affects the service life of the power battery, but also the power battery may explode and burn because of excessive heat. And so on, causing serious security problems.
技术问题technical problem
现有技术中,对动力电池进行热量处理有以下三种方式:1、自然散热方式,是指通过外部空气对流或热量的扩散,将动力电池的热量带走以实现散热的目的。这种散热方式要求动力电池充放电的倍率很低,导致动力电池的输出功率不高,散热效率低,不利于推广使用;2、风冷散热方式,是指通过风扇等设备将冷风送入动力电池间隙,从而将动力电池产生的热量带走。这种散热方式会导致单个动力电池之间存在较大的温度差,不利于对动力电池的包装,散热效果差;3、液体冷却方式,是指通过冷却机组和水冷回路将动力电池的热量带走。这种散热方式的结构复杂,若动力电池组的功率较大,对冷却系统的要求很高。In the prior art, there are three ways for heat treatment of a power battery: 1. The natural heat dissipation method refers to the purpose of dissipating the heat of the power battery by the convection or heat of the external air to achieve heat dissipation. This kind of heat dissipation method requires that the power battery charge and discharge rate is very low, resulting in low output power of the power battery, low heat dissipation efficiency, which is not conducive to popularization; 2. Air cooling and heat dissipation means that cold air is sent to the power through a fan or the like. The battery gap, which takes away the heat generated by the power battery. This kind of heat dissipation method will cause a large temperature difference between the single power batteries, which is not conducive to the packaging of the power battery, and the heat dissipation effect is poor; 3. The liquid cooling method refers to the heat band of the power battery through the cooling unit and the water cooling circuit. go. The structure of the heat dissipation method is complicated, and if the power of the power battery pack is large, the requirements for the cooling system are high.
综上所述,目前动力电池的散热方式均存在散热效果差的问题,而且动力电池的热量直接经散热设备排出,不仅对环境造成污染,而且能源利用率低。In summary, at present, the heat dissipation method of the power battery has the problem of poor heat dissipation, and the heat of the power battery is directly discharged through the heat dissipation device, which not only causes pollution to the environment, but also has low energy utilization rate.
技术解决方案Technical solution
本发明的目的在于提供一种基于气液两相散热及热能回收的动力电池系统,以解决现有技术中存在的动力电池散热效率低,能源浪费的问题。The object of the present invention is to provide a power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery, so as to solve the problem of low heat dissipation efficiency and waste of energy of the power battery existing in the prior art.
为实现上述目的,本发明采用的技术方案是:提供一种基于气液两相散热及热能回收的动力电池系统,包括箱体和设于所述箱体内的多个电池,所述箱体内安装有用于吸收各所述电池发出热量的多个液气转换片,各所述液气转换片中设有存储制冷剂的存储空间,各所述液气转换片的下端设有进液口,各所述液气转换片的上端开设有排气口;所述基于气液两相散热及热能回收的动力电池系统还包括用于收集各所述液气转换片排出的气体的气体集流器、将所述气体集流器排出气体转换为液体的气液转换器和将所述气体集流器散出的热量转换为电能的温差发电片,所述温差发电片贴于所述气体集流器上,所述气液转换器的入口与所述气体集流器的出口相连通,所述气体集流器的入口与各所述排气口相连通,所述气液转换器的出口与各所述进液口相连通。In order to achieve the above object, the technical solution adopted by the present invention is to provide a power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery, comprising a box body and a plurality of batteries disposed in the box body, the cabinet body being installed a plurality of liquid-gas conversion sheets for absorbing heat generated by each of the batteries, wherein each of the liquid-gas conversion sheets is provided with a storage space for storing a refrigerant, and each of the liquid-gas conversion sheets has a liquid inlet at a lower end thereof. The upper end of the liquid-gas conversion sheet is provided with an exhaust port; the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery further includes a gas current collector for collecting gas discharged from each of the liquid-gas conversion sheets, a gas-liquid converter that converts the gas collector exhaust gas into a liquid and a thermoelectric power generation piece that converts heat dissipated by the gas current collector into electric energy, the thermoelectric power generation sheet being attached to the gas current collector Above, an inlet of the gas-liquid converter is in communication with an outlet of the gas current collector, an inlet of the gas current collector is connected to each of the exhaust ports, and an outlet of the gas-liquid converter and each The liquid inlets are in communication.
进一步地,还包括用于对所述温差发电片进行散热的散热器,所述散热器和所述气体集流器配合夹持所述温差发电片。Further, a heat sink for dissipating heat from the thermoelectric power generation sheet is further included, and the heat sink and the gas current collector cooperate to clamp the thermoelectric power generation sheet.
进一步地,还包括连通各所述进液口的连通管,所述连通管与所述气液转换器的出口相连。Further, a communication pipe that communicates with each of the liquid inlets is further included, and the communication pipe is connected to an outlet of the gas-liquid converter.
进一步地,还包括连通各所述排气口的集气管,所述集气管与所述气体集流器的入口相连。Further, a gas collecting pipe connecting each of the exhaust ports is further included, and the gas collecting pipe is connected to an inlet of the gas current collector.
进一步地,所述气液转换器包括储液箱,所述储液箱的底面安装有连接各所述进液口的出液管,所述储液箱的侧面安装有连通所述气体集流器的进气管。Further, the gas-liquid converter includes a liquid storage tank, and a bottom surface of the liquid storage tank is installed with an outlet pipe connecting each of the liquid inlets, and a side of the liquid storage tank is installed to communicate the gas current collection The intake pipe of the device.
进一步地,所述储液箱的顶面设有注液口,所述气液转换器还包括盖于所述注液口上的密封盖。Further, a top surface of the liquid storage tank is provided with a liquid injection port, and the gas-liquid converter further includes a sealing cover covering the liquid injection opening.
进一步地,所述气液转换器还包括安装于所述储液箱上的若干散热片。Further, the gas-liquid converter further includes a plurality of fins mounted on the liquid tank.
进一步地,所述液气转换片中设有将所述存储空间分隔成若干竖直流道的间隔板。Further, the liquid-gas conversion sheet is provided with a partition plate that divides the storage space into a plurality of vertical DC channels.
进一步地,所述气体集流器包括集气盒,所述集气盒的两侧分别设有进口管和出口管,所述集气盒中设有连通所述进口管与所述出口管的弯曲流道。Further, the gas current collector includes a gas collecting box, and two sides of the gas collecting box are respectively provided with an inlet pipe and an outlet pipe, and the gas collecting box is provided with the inlet pipe and the outlet pipe. Bend the flow path.
进一步地,所述弯曲流道呈S型铺设于所述集气盒中。Further, the curved flow channel is laid in the gas collecting box in an S shape.
有益效果Beneficial effect
本发明提供的基于气液两相散热及热能回收的动力电池系统的有益效果在于:与现有技术相比,该基于气液两相散热及热能回收的动力电池系统在箱体内设置有多个液气转换片,各液气转换片中的液态制冷剂在电池的高温作用下汽化,从而吸收电池产生的热量,电池的散热效果好。该基于气液两相散热及热能回收的动力电池系统还设置有气体集流器、气液转换器和贴于该气体集流器上的温差发电片,该气液转换器可将气态制冷剂重新转变为液态制冷剂,制冷剂可以循环使用;该温差发电片可将电池的热量转变为电能,便于能源的重复利用。因此本发明不仅对电池的散热效果好,而且制冷剂可以重复使用,电池的热量还可以转换为电能,能源得到循环利用,能源利用率高。The utility model provides a power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery, which has the beneficial effects that the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery is provided in the cabinet body more than the prior art. The liquid-gas conversion sheet, the liquid refrigerant in each liquid-gas conversion sheet is vaporized under the action of the high temperature of the battery, thereby absorbing the heat generated by the battery, and the heat dissipation effect of the battery is good. The power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery is further provided with a gas current collector, a gas-liquid converter and a thermoelectric power generation piece attached to the gas current collector, the gas-liquid converter can be a gaseous refrigerant Re-converted to liquid refrigerant, the refrigerant can be recycled; the thermoelectric sheet can convert the heat of the battery into electric energy, which is convenient for energy reuse. Therefore, the invention not only has good heat dissipation effect on the battery, but also the refrigerant can be repeatedly used, the heat of the battery can also be converted into electric energy, the energy is recycled, and the energy utilization rate is high.
附图说明DRAWINGS
为了更清楚地说明本发明实施例中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动性的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the technical solutions in the embodiments of the present invention, the drawings used in the embodiments or the description of the prior art will be briefly described below. It is obvious that the drawings in the following description are only the present invention. For some embodiments, other drawings may be obtained from those of ordinary skill in the art in light of the inventive workability.
图1为本发明实施例提供的基于气液两相散热及热能回收的动力电池系统的结构示意图;1 is a schematic structural diagram of a power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery according to an embodiment of the present invention;
图2为本发明实施例提供的基于气液两相散热及热能回收的动力电池系统的爆炸图;2 is an exploded view of a power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery according to an embodiment of the present invention;
图3为本发明实施例提供的箱体内部的俯视图;3 is a top plan view of an interior of a cabinet according to an embodiment of the present invention;
图4为本发明实施例提供的液气转换片的主视图;4 is a front view of a liquid-gas conversion sheet according to an embodiment of the present invention;
图5为图4中A-A方向的剖视图;Figure 5 is a cross-sectional view taken along line A-A of Figure 4;
图6为本发明实施例提供的气液转换器的结构示意图;6 is a schematic structural diagram of a gas-liquid converter according to an embodiment of the present invention;
图7为本发明实施例提供的气体集流器的剖视图;Figure 7 is a cross-sectional view of a gas current collector according to an embodiment of the present invention;
图8为本发明实施例提供的温差发电片的结构示意图。FIG. 8 is a schematic structural diagram of a thermoelectric power generation chip according to an embodiment of the present invention.
其中,图中各附图主要标记:Among them, the figures in the figure are mainly marked:
1-箱体;2-电池;1-box; 2-battery;
3-液气转换片;31-存储空间;32-进液口;33-排气口;34-间隔板;3-liquid-gas conversion sheet; 31-storage space; 32-inlet port; 33-exhaust port; 34-spacer plate;
4-连通管;5-集气管;4-connected pipe; 5-collector;
6-气液转换器;61-注液口;62-密封盖;63-出液管;64-进气管;65-散热片;66-液位指示器;67-储液箱;6-gas-liquid converter; 61-injection port; 62-sealing cap; 63-outlet pipe; 64-intake pipe; 65-heat sink; 66-level indicator; 67-tank;
7-气体集流器;71-集气盒;72-进口管;73-出口管;74-弯曲流道;7-gas current collector; 71-gas box; 72-inlet tube; 73-outlet tube; 74-bent flow channel;
8-温差发电片;81-热片;82-冷片;83-P型半导体;84-N型半导体;85-正极输出端;86-负极输出端;8-temperature difference power generation sheet; 81-hot sheet; 82-cold sheet; 83-P type semiconductor; 84-N type semiconductor; 85-positive output terminal; 86-negative output terminal;
9-散热器;10-第一连接管;11-第二连接管;12-第三连接管。9-heat sink; 10-first connecting tube; 11-second connecting tube; 12-third connecting tube.
本发明的实施方式Embodiments of the invention
为了使本发明所要解决的技术问题、技术方案及有益效果更加清楚明白,以下结合附图及实施例,对本发明进行进一步详细说明。应当理解,此处所描述的具体实施例仅仅用以解释本发明,并不用于限定本发明。The present invention will be further described in detail below with reference to the accompanying drawings and embodiments. It is understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
需要说明的是,当元件被称为“固定于”或“设置于”另一个元件,它可以直接在另一个元件上或者间接在该另一个元件上。当一个元件被称为是“连接于”另一个元件,它可以是直接连接到另一个元件或间接连接至该另一个元件上。It is to be noted that when an element is referred to as being "fixed" or "in" another element, it can be directly on the other element or indirectly. When an element is referred to as being "connected" to another element, it can be directly connected to the other element or indirectly connected to the other element.
此外,术语“第一”、“第二”仅用于描述目的,而不能理解为指示或暗示相对重要性或者隐含指明所指示的技术特征的数量。由此,限定有“第一”、“第二”的特征可以明示或者隐含地包括一个或者更多个该特征。在本发明的描述中,“多个”的含义是两个或两个以上,除非另有明确具体的限定。Moreover, the terms "first" and "second" are used for descriptive purposes only and are not to be construed as indicating or implying a relative importance or implicitly indicating the number of technical features indicated. Thus, features defining "first" and "second" may include one or more of the features either explicitly or implicitly. In the description of the present invention, the meaning of "a plurality" is two or more unless specifically and specifically defined otherwise.
在本发明的描述中,需要理解的是,术语“中心”、“长度”、“宽度”、“厚度”、“上”、“下”、“前”、“后”、“左”、“右”、“竖直”、“水平”、“顶”、“底”、“内”、“外”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本发明和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本发明的限制。In the description of the present invention, it is to be understood that the terms "center", "length", "width", "thickness", "upper", "lower", "front", "back", "left", " The orientation or positional relationship of the indications of "right", "vertical", "horizontal", "top", "bottom", "inside", "outside", etc. is based on the orientation or positional relationship shown in the drawings, only for convenience. The present invention and the simplifications of the invention are not to be construed as limiting or limiting the scope of the invention.
在本发明的描述中,需要说明的是,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或一体地连接;可以是机械连接,也可以是电连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通或两个元件的相互作用关系。对于本领域的普通技术人员而言,可以根据具体情况理解上述术语在本发明中的具体含义。In the description of the present invention, it should be noted that the terms "installation", "connected", and "connected" are to be understood broadly, and may be fixed or detachable, for example, unless otherwise explicitly defined and defined. Connected, or integrally connected; may be mechanically connected or electrically connected; may be directly connected, or may be indirectly connected through an intermediate medium, may be internal communication of two elements or an interaction relationship of two elements. For those skilled in the art, the specific meanings of the above terms in the present invention can be understood on a case-by-case basis.
请一并参阅图1至图8,现对本发明提供的基于气液两相散热及热能回收的动力电池系统进行说明。该基于气液两相散热及热能回收的动力电池系统包括箱体1和设置在箱体1内的多个电池2,各液气转换片3与各电池2形成交替分布。此处,电池2可以为圆形、方形等任意形状。具体地,相邻两个液气转换片3之间均设置有一电池2,各液气转换片3与电池2的接触面均涂覆有导热硅胶,以减小热阻,各电池2的两侧都能被液气转换片3覆盖,因此各电池2的散热效果好,而且各电池2之间的温度具有良好的一致性。箱体1内设置有用于吸收多个电池2发出热量的多个液气转换片3,各液气转换片3中均设置有用于存储制冷剂的存储空间31。此处,制冷剂为有机混合物,制冷剂的沸点为37-45℃。优选地,制冷剂为质量分数为6%的乙醇、质量分数为91%的环戊烷和质量分数为3%的抗爆剂组成的混合物,该混合物的沸点为44.7℃;或者,制冷剂为质量分数为6.2%的甲醇、质量分数为91.8%的二氯甲烷和质量分数为2%的抗爆剂组成的混合物,该混合物的沸点为37.8℃。由于制冷剂的沸点很低,在电池2产生的热量的作用下,存储空间31中的液态制冷剂会受热汽化转变为气态制冷剂。各液气转换片3的一侧面的下端均开设有进液口32,各液气转换片3的对立侧面的上端均开设有排气口33。Referring to FIG. 1 to FIG. 8 together, the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery provided by the present invention will now be described. The power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery includes a casing 1 and a plurality of batteries 2 disposed in the casing 1, and each of the liquid-gas conversion sheets 3 and the respective batteries 2 are alternately distributed. Here, the battery 2 may have any shape such as a circle or a square. Specifically, a battery 2 is disposed between two adjacent liquid-gas conversion sheets 3, and the contact surfaces of each of the liquid-gas conversion sheets 3 and the battery 2 are coated with a thermal conductive silica gel to reduce thermal resistance, and two of the batteries 2 are respectively The sides can be covered by the liquid-gas conversion sheet 3, so that the heat dissipation effect of each of the batteries 2 is good, and the temperature between the batteries 2 has a good consistency. A plurality of liquid-gas conversion sheets 3 for absorbing heat generated by the plurality of batteries 2 are disposed in the casing 1, and each of the liquid-gas conversion sheets 3 is provided with a storage space 31 for storing the refrigerant. Here, the refrigerant is an organic mixture, and the boiling point of the refrigerant is 37-45 °C. Preferably, the refrigerant is a mixture of ethanol having a mass fraction of 6%, cyclopentane having a mass fraction of 91%, and an antiknock agent having a mass fraction of 3%, the boiling point of the mixture being 44.7 ° C; or, the refrigerant is A mixture of 6.2% methanol, 91.8% by mass of methylene chloride and 2% by mass of antiknock agent having a boiling point of 37.8 °C. Since the boiling point of the refrigerant is very low, the liquid refrigerant in the storage space 31 is converted into a gaseous refrigerant by the thermal vaporization under the action of the heat generated by the battery 2. A liquid inlet 32 is opened at a lower end of one side of each of the liquid-gas conversion sheets 3, and an exhaust port 33 is opened at an upper end of each of the opposite sides of each of the liquid-gas conversion sheets 3.
该基于气液两相散热及热能回收的动力电池系统还包括气体集流器7、气液转换器6和贴于该气体集流器7上的温差发电片8。气液转换器6的入口与气体集流器7的出口通过第三连接管12相连通,气体集流器7的入口与各排气口33通过第二连接管11相连通,气液转换器6的出口与各进液口32通过第一连接管10相连通。气体集流器7可将多个液气转换片3排出的气体收集,并将该气体的热量传递至温差发电片8,该温差发电片8可将热量转换为电能并存储。气液转换器6可将气体集流器7排出的气体重新转换为液体。The power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery further includes a gas current collector 7, a gas-liquid converter 6, and a thermoelectric power generation sheet 8 attached to the gas current collector 7. The inlet of the gas-liquid converter 6 and the outlet of the gas collector 7 are communicated through the third connecting pipe 12, and the inlet of the gas current collector 7 communicates with each of the exhaust ports 33 through the second connecting pipe 11, the gas-liquid converter The outlet of 6 communicates with each of the inlet ports 32 through the first connecting pipe 10. The gas current collector 7 collects the gas discharged from the plurality of liquid-gas conversion sheets 3, and transfers the heat of the gas to the thermoelectric power generation sheet 8, which converts the heat into electric energy and stores it. The gas-liquid converter 6 can re-convert the gas discharged from the gas collector 7 into a liquid.
其中,液气转换片3和气液转换器6优选为铝合金或者铜合金材料制成。在其它实施例中,根据实际需要,制冷剂也可以为其它有机混合物;液气转换片3和气液转换器6还可以由其它导热良好的材料制成,在此不作唯一限定。Among them, the liquid-gas conversion sheet 3 and the gas-liquid converter 6 are preferably made of an aluminum alloy or a copper alloy material. In other embodiments, the refrigerant may also be other organic mixtures according to actual needs; the liquid-gas conversion sheet 3 and the gas-liquid converter 6 may also be made of other materials having good heat conductivity, which are not limited herein.
本发明提供的基于气液两相散热及热能回收的动力电池系统,与现有技术相比,该基于气液两相散热及热能回收的动力电池系统在箱体1内设置有多个液气转换片3,各液气转换片3中的液态制冷剂在电池2的高温作用下汽化,从而吸收电池2产生的热量,电池2的散热效果好。该基于气液两相散热及热能回收的动力电池系统还设置有气体集流器7、气液转换器6和贴于该气体集流器7上的温差发电片8,该气液转换器6可将气态制冷剂重新转变为液态制冷剂,制冷剂可以循环使用;该温差发电片8可将电池2的热量转变为电能,便于能源的重复利用。因此本发明不仅对电池2的散热效果好,而且制冷剂可以重复使用,电池2的热量还可以转换为电能,能源得到循环利用,能源利用率高。The power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery provided by the present invention has a plurality of liquid gases disposed in the casing 1 in the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery compared with the prior art. In the conversion sheet 3, the liquid refrigerant in each of the liquid-gas conversion sheets 3 is vaporized by the high temperature of the battery 2, thereby absorbing the heat generated by the battery 2, and the heat dissipation effect of the battery 2 is good. The power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery is further provided with a gas current collector 7, a gas-liquid converter 6, and a thermoelectric power generation sheet 8 attached to the gas current collector 7, the gas-liquid converter 6 The gaseous refrigerant can be reconverted into a liquid refrigerant, and the refrigerant can be recycled; the thermoelectric power generation sheet 8 can convert the heat of the battery 2 into electric energy, thereby facilitating the reuse of energy. Therefore, the invention not only has good heat dissipation effect on the battery 2, but also the refrigerant can be repeatedly used, the heat of the battery 2 can also be converted into electric energy, the energy is recycled, and the energy utilization rate is high.
进一步地,请一并参阅图1和图8,作为本发明提供的基于气液两相散热及热能回收的动力电池系统的一种具体实施方式,该基于气液两相散热及热能回收的动力电池系统还包括用于对温差发电片8进行散热的散热器9,该散热器9和气体集流器7配合夹持该温差发电片8。具体地,在气体集流器7的一侧面上紧贴设置有用于将电池2的热量转换为电能的温差发电片8,在温差发电片8的相对立的侧面上紧贴设置有用于散热的散热器9。此处,散热器9优选为铝合金或者铜合金等高导热系数材料制成。在其它实施例中,散热器9也可以为其它导热性能优良的材料制成,在此不作唯一限定。Further, please refer to FIG. 1 and FIG. 8 together as a specific embodiment of a power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery provided by the present invention, which is based on gas-liquid two-phase heat dissipation and heat energy recovery. The battery system further includes a heat sink 9 for dissipating heat from the thermoelectric power generation sheet 8, and the heat sink 9 and the gas current collector 7 cooperate to sandwich the thermoelectric power generation sheet 8. Specifically, a thermoelectric power generation sheet 8 for converting heat of the battery 2 into electric energy is disposed on one side of the gas current collector 7, and is disposed on the opposite side of the thermoelectric power generation sheet 8 for heat dissipation. Radiator 9. Here, the heat sink 9 is preferably made of a material having a high thermal conductivity such as an aluminum alloy or a copper alloy. In other embodiments, the heat sink 9 can also be made of other materials having excellent thermal conductivity, which is not limited herein.
温差发电片8包括热片81与冷片82。此处,热片81和冷片82优选为铝合金或者铜合金等导热性能良好的材料制成。热片81与冷片82之间设有交替分布的多个P型半导体83和多个N型半导体84,温差发电片8还包括用于为蓄电池(图中未画出)供电的正极输出端85和负极输出端86。此处,蓄电池的电压优选为24V。具体地,温差发电片8的热片81与气体集流器7贴合,温差发电片8的冷片82与散热器9贴合。两个相邻的P型半导体83和N型半导体84之间通过铝合金或者铜合金等优良的热导材料制成的金属连接形成一个PN节,多个PN节之间并联或者串联,正极输出端85和负极输出端86设置在P型半导体83或N型半导体84上。The thermoelectric power generation sheet 8 includes a heat sheet 81 and a cold sheet 82. Here, the hot sheet 81 and the cold sheet 82 are preferably made of a material having good thermal conductivity such as an aluminum alloy or a copper alloy. A plurality of P-type semiconductors 83 and a plurality of N-type semiconductors 84 are alternately arranged between the hot sheet 81 and the cold sheet 82. The thermoelectric power generation sheet 8 further includes a positive output terminal for supplying power to a battery (not shown). 85 and negative output 86. Here, the voltage of the battery is preferably 24V. Specifically, the hot sheet 81 of the thermoelectric power generation sheet 8 is bonded to the gas current collector 7, and the cold sheet 82 of the thermoelectric power generation sheet 8 is bonded to the heat sink 9. Two adjacent P-type semiconductors 83 and N-type semiconductors 84 are connected by a metal made of an excellent thermal conductive material such as an aluminum alloy or a copper alloy to form a PN junction, and a plurality of PN sections are connected in parallel or in series, and the positive output is The terminal 85 and the negative output terminal 86 are disposed on the P-type semiconductor 83 or the N-type semiconductor 84.
气体集流器7与温差发电片8贴合的接触面由导热的金属材料制成,气体集流器7的其它侧面均由绝热材料制成。此处,该金属材料优选为铝合金或者铜合金。此结构,当携带大量热量的气态制冷剂进入气体集流器7中后,气体集流器7通过与温差发电片8的接触面集中将热量传递至温差发电片8的热片81,热量不会从气体集流器7的其它侧面扩散出去,或者从气体集流器7的其它侧面扩散出去的热量很少,从而提高了热量的的传递效率,提高了能源的利用率。在其它实施例中,气体集流器7与温差发电片8贴合的接触面也可以由其它导热性能优良的材料制成,在此不作唯一限定。The contact faces of the gas current collector 7 and the thermoelectric power generation sheet 8 are made of a thermally conductive metal material, and the other sides of the gas current collector 7 are made of a heat insulating material. Here, the metal material is preferably an aluminum alloy or a copper alloy. With this configuration, when the gaseous refrigerant carrying a large amount of heat enters the gas current collector 7, the gas current collector 7 concentrates the heat to the heat sheet 81 of the thermoelectric power generation sheet 8 through the contact surface with the thermoelectric power generation sheet 8, and the heat is not It will diffuse out from the other side of the gas collector 7, or have little heat diffused from the other side of the gas collector 7, thereby improving the heat transfer efficiency and improving the energy utilization rate. In other embodiments, the contact surface of the gas current collector 7 and the thermoelectric power generation sheet 8 may be made of other materials having excellent thermal conductivity, which is not limited herein.
从液气转换片3出来的并带有大量热量的气态制冷剂进入气体集流器7中,气体集流器7将热量传递到温差发电片8的热片81,在散热器9和空气的传热作用下,温差发电片8的热片81与冷片82之间产生温度梯度,在塞贝克效应(是指由于两种不同电导体或者半导体的温度差异而引起两种物质间的电压差的热电现象)的作用下,热能通过P型半导体83、N型半导体84和PN节转变为电能,电能通过正极输出端85和负极输出端86储存在蓄电池中,因此电池2的热能得到回收,减少了能源的浪费。在其它实施例中,热片81和冷片82也可以为其它导热性能优良的材料制成;蓄电池的电压还可以为其它数值,在此不作唯一限定。The gaseous refrigerant from the liquid-gas conversion sheet 3 with a large amount of heat enters the gas collector 7, and the gas collector 7 transfers the heat to the hot sheet 81 of the thermoelectric power generation sheet 8, in the radiator 9 and the air Under the action of heat transfer, a temperature gradient is generated between the hot sheet 81 of the thermoelectric power generation sheet 8 and the cold sheet 82, and the Seebeck effect is a voltage difference between two substances due to temperature differences between two different electrical conductors or semiconductors. Under the action of the thermoelectric phenomenon, the thermal energy is converted into electric energy by the P-type semiconductor 83, the N-type semiconductor 84 and the PN junction, and the electric energy is stored in the storage battery through the positive output terminal 85 and the negative output terminal 86, so that the heat energy of the battery 2 is recovered. Reduced energy waste. In other embodiments, the hot sheet 81 and the cold sheet 82 may also be made of other materials having excellent thermal conductivity; the voltage of the battery may also be other values, which is not limited herein.
进一步地,请一并参阅图2,作为本发明提供的基于气液两相散热及热能回收的动力电池系统的一种具体实施方式,该基于气液两相散热及热能回收的动力电池系统还包括连通各进液口32的连通管4,该连通管4与气液转换器6的出口相连。气液转换器6具有补给和存储液态制冷剂的作用。当电池2在充放电的过程中,需要给电池2降温时,气液转换器6中的液态制冷剂从气液转换器6的出口流出,并顺着第一连接管10和连通管4从液气转换片3的进液口32流进各液气转换片3的存储空间31中,液态制冷剂在电池2释放的高温作用下汽化,液态制冷剂转换为气态制冷剂,并吸收电池2的大量热量,携带大量热量的气态制冷剂从液气转换片3的排气口33排出,从而达到对电池2降温的作用,且电池2的散热效果好。Further, please refer to FIG. 2 together, as a specific implementation manner of the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery provided by the present invention, the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery The communication pipe 4 that connects the respective liquid inlets 32 is connected, and the communication pipe 4 is connected to the outlet of the gas-liquid converter 6. The gas-liquid converter 6 has a function of replenishing and storing a liquid refrigerant. When the battery 2 is in the process of charging and discharging, when the battery 2 needs to be cooled, the liquid refrigerant in the gas-liquid converter 6 flows out from the outlet of the gas-liquid converter 6, and follows the first connecting pipe 10 and the connecting pipe 4 The liquid inlet 32 of the liquid-gas conversion sheet 3 flows into the storage space 31 of each liquid-gas conversion sheet 3, the liquid refrigerant vaporizes under the high temperature released by the battery 2, the liquid refrigerant is converted into a gaseous refrigerant, and the battery 2 is absorbed. The large amount of heat, the gaseous refrigerant carrying a large amount of heat is discharged from the exhaust port 33 of the liquid-gas conversion sheet 3, thereby achieving the effect of lowering the temperature of the battery 2, and the heat dissipation effect of the battery 2 is good.
进一步地,请一并参阅图2,作为本发明提供的基于气液两相散热及热能回收的动力电池系统的一种具体实施方式,该基于气液两相散热及热能回收的动力电池系统还包括连通各排气口33的集气管5,该集气管5与气体集流器7的入口相连。携带大量热量的气态制冷剂从液气转换片3的排气口33排出,并顺着集气管5和第二连接管11一并进入气体集流器7中,气体集流器7将热量传递给温差发电片8,并在散热器9和空气的传热作用下,温差发电片8的热片81与冷片82之间产生温度梯度,并且在塞贝克效应的作用下,热能转变为电能,电能经过正极输出端85和负极输出端86储存在蓄电池中,因此,电池2的热能可以转换为电能,能量得以重复利用,能源利用率高。Further, please refer to FIG. 2 together, as a specific implementation manner of the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery provided by the present invention, the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery A gas collecting pipe 5 is connected to each of the exhaust ports 33, and the gas collecting pipe 5 is connected to the inlet of the gas current collector 7. The gaseous refrigerant carrying a large amount of heat is discharged from the exhaust port 33 of the liquid-gas conversion sheet 3, and enters the gas current collector 7 along the gas collecting pipe 5 and the second connecting pipe 11, and the gas current collector 7 transfers heat. The temperature difference power generating sheet 8 is given, and under the heat transfer action of the heat sink 9 and the air, a temperature gradient is generated between the hot sheet 81 of the thermoelectric power generation sheet 8 and the cold sheet 82, and the heat energy is converted into electric energy by the Seebeck effect. The electric energy is stored in the battery through the positive output terminal 85 and the negative output terminal 86. Therefore, the thermal energy of the battery 2 can be converted into electric energy, the energy can be reused, and the energy utilization rate is high.
进一步地,请一并参阅图6,作为本发明提供的基于气液两相散热及热能回收的动力电池系统的一种具体实施方式,气液转换器6包括储液箱67,该储液箱67的底面安装有连接各进液口32的出液管63,储液箱67的侧面安装有连通气体集流器7的进气管64。储液箱67具有储存液态制冷剂的作用。注液管63通过第一连接管10与连通管4相连通,进气管64通过第二连接管11与气体集流器7相连通,因此可将液气转换片3、气体集流器7和气液转换器6连通。存储在储液箱67中的液态制冷剂流入液气转换片3中,液态制冷剂汽化转变为气态制冷剂,并吸收电池2的热量。携带有大量热量的气态制冷剂进入气体集流器7中,在温差发电片8和散热器9的作用下将电池2的热量转换为电能储存,气态制冷剂进入储液箱67中并液化,气态制冷剂重新转变为液态制冷剂。因此,该基于气液两相散热及热能回收的动力电池系统不仅能够将电池2的热能转换为电能,制冷剂也能重复使用,能源的利用率高。在其它实施例中,出液管63和进气管64也可以设置在其它位置处,在此不作唯一限定。Further, please refer to FIG. 6 as a specific embodiment of the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery provided by the present invention, the gas-liquid converter 6 includes a liquid storage tank 67, the liquid storage tank An outlet pipe 63 that connects each of the liquid inlets 32 is attached to the bottom surface of the liquid storage port 67, and an intake pipe 64 that communicates with the gas current collector 7 is attached to the side surface of the liquid storage tank 67. The reservoir 67 has a function of storing a liquid refrigerant. The liquid injection pipe 63 communicates with the communication pipe 4 through the first connecting pipe 10, and the intake pipe 64 communicates with the gas current collector 7 through the second connecting pipe 11, so that the liquid-gas conversion sheet 3, the gas current collector 7, and the gas can be The liquid converter 6 is in communication. The liquid refrigerant stored in the liquid storage tank 67 flows into the liquid-gas conversion sheet 3, and the liquid refrigerant vaporizes into a gaseous refrigerant, and absorbs the heat of the battery 2. The gaseous refrigerant carrying a large amount of heat enters the gas current collector 7, and converts the heat of the battery 2 into electric energy storage under the action of the thermoelectric power generation sheet 8 and the heat sink 9, and the gaseous refrigerant enters the liquid storage tank 67 and is liquefied. The gaseous refrigerant is reconverted to a liquid refrigerant. Therefore, the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery can not only convert the heat energy of the battery 2 into electric energy, but also the refrigerant can be reused, and the energy utilization rate is high. In other embodiments, the outlet tube 63 and the inlet tube 64 may also be disposed at other locations, which are not limited herein.
并且,储液箱67的底面高于液气转换片3的表面。此结构,储液箱67中的液态制冷剂经出液管63流入液气转换片3中,由于储液箱67的底面高于液气转换片3的表面,因此储液箱67中的压强要高于液气转换片3中的压强,在压强差的作用下,液态制冷剂可以充满整个液气转换片3,液态制冷剂可将电池2的两侧面覆盖,从而有利于提高对电池2的热量的吸收量,进而提高电池2的散热效率。Further, the bottom surface of the reservoir tank 67 is higher than the surface of the liquid-gas conversion sheet 3. With this configuration, the liquid refrigerant in the reservoir tank 67 flows into the liquid-gas conversion sheet 3 through the outlet pipe 63. Since the bottom surface of the reservoir tank 67 is higher than the surface of the liquid-gas conversion sheet 3, the pressure in the reservoir tank 67 is high. It is higher than the pressure in the liquid-gas conversion sheet 3, and under the action of the pressure difference, the liquid refrigerant can fill the entire liquid-gas conversion sheet 3, and the liquid refrigerant can cover both sides of the battery 2, thereby facilitating the improvement of the battery 2 The amount of heat absorbed, thereby improving the heat dissipation efficiency of the battery 2.
进一步地,请一并参阅图6,作为本发明提供的基于气液两相散热及热能回收的动力电池系统的一种具体实施方式,储液箱67的顶面设有注液口61,气液转换器6还包括盖于注液口61上的密封盖62。注液口61用于向储液箱67中添加液态制冷剂,使得该基于气液两相散热及热能回收的动力电池系统能够正常工作。密封盖62起到密封注液口61的作用。当气态制冷剂从气体集流器7流出并进入储液箱67后,密封盖62可防止气态制冷剂的溢出和泄露,提高能源的使用率。在其它实施例中,注液口61也可以设置在其它位置处,在此不作唯一限定。Further, please refer to FIG. 6 as a specific embodiment of the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery provided by the present invention. The top surface of the liquid storage tank 67 is provided with a liquid injection port 61. The liquid exchanger 6 also includes a sealing cover 62 that covers the liquid inlet 61. The liquid injection port 61 is for adding a liquid refrigerant to the liquid storage tank 67, so that the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery can operate normally. The sealing cover 62 functions to seal the liquid filling port 61. When the gaseous refrigerant flows out of the gas current collector 7 and enters the liquid storage tank 67, the sealing cover 62 prevents overflow and leakage of the gaseous refrigerant, thereby improving energy usage. In other embodiments, the liquid inlet 61 can also be disposed at other locations, which is not limited herein.
储液箱67内设有用于监测制冷剂的液位指示器66。当气液转换器6中的液态制冷剂的液面低于设定值时,报警装置(图中未画出)发出警报,提醒用户添加制冷剂,从而有利于提高电池2的散热效率,提高基于气液两相散热及热能回收的动力电池系统的使用安全性。在其它实施例中,液位指示器66也可以设置在其它位置处,在此不作唯一限定。A liquid level indicator 66 for monitoring the refrigerant is provided in the reservoir tank 67. When the liquid level of the liquid refrigerant in the gas-liquid converter 6 is lower than the set value, the alarm device (not shown) issues an alarm to remind the user to add the refrigerant, thereby contributing to improving the heat dissipation efficiency of the battery 2 and improving Safety of use of power battery systems based on gas-liquid two-phase heat dissipation and heat recovery. In other embodiments, the level indicator 66 can also be disposed at other locations, which is not uniquely limited herein.
进一步地,请一并参阅图6,作为本发明提供的基于气液两相散热及热能回收的动力电池系统的一种具体实施方式,气液转换器6还包括安装于储液箱67上的若干散热片65。当气态制冷剂从气体集流器7流出并进入储液箱67后,在若干散热片65的作用下,降低储液箱67中的温度,并使气态制冷剂液化,气态制冷剂转化为液态制冷剂,从而达到制冷剂循环使用的目的,进而提高能源的重复使用率,节约能源。在其它实施例中,散热片65也可以设置在储液箱67的其它位置处,在此不作唯一限定。Further, please refer to FIG. 6 as a specific embodiment of the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery provided by the present invention. The gas-liquid converter 6 further includes a liquid storage tank 6 mounted on the liquid storage tank 67. A plurality of fins 65. When the gaseous refrigerant flows out of the gas current collector 7 and enters the liquid storage tank 67, the temperature in the liquid storage tank 67 is lowered by the action of the plurality of fins 65, and the gaseous refrigerant is liquefied, and the gaseous refrigerant is converted into a liquid state. Refrigerant, so as to achieve the purpose of refrigerant recycling, thereby increasing energy reuse rate and saving energy. In other embodiments, the fins 65 may also be disposed at other locations of the reservoir 67, which are not specifically limited herein.
进一步地,请一并参阅图5,作为本发明提供的基于气液两相散热及热能回收的动力电池系统的一种具体实施方式,液气转换片3中设有将存储空间31分隔成若干竖直流道的间隔板34。间隔板34一方面能够减缓液态制冷剂填充液气转换片3的速率,为液态制冷剂吸收电池2的热量,并汽化转变为气态制冷剂提供充足的时间,提高液态制冷剂的汽化效率;另一方面,间隔板34使得各液气转换片3与对应的电池2贴合的接触面呈口琴管状。此结构,电池2产生的热量通过该口琴管状的间隔板34传递至液气转换片3中,不仅可以将存储空间31中的液态制冷剂汽化,使液态制冷剂转变为气态制冷剂,还能起到毛细作用(是指浸润液体在细管里升高的现象和不浸润液体在细管里下降的现象),液态制冷剂在间隔板34中能够顺利流动,加之储液箱67的底面高于液气转换片3的表面,能够使液态制冷剂能够充满整个液气转换片3,从而达到很好的散热效果。在其它实施例中,该接触面也可以为其它构型,在此不作唯一限定。Further, please refer to FIG. 5 together, as a specific implementation manner of the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery provided by the present invention, the liquid-gas conversion sheet 3 is provided with the storage space 31 divided into several A spacer plate 34 of a vertical DC channel. On the one hand, the partition plate 34 can slow down the rate at which the liquid refrigerant fills the liquid-gas conversion sheet 3, absorbs the heat of the battery 2 for the liquid refrigerant, and provides sufficient time for vaporization to convert into a gaseous refrigerant, thereby improving the vaporization efficiency of the liquid refrigerant; On the one hand, the partition plate 34 has a contact surface in which the respective liquid-gas conversion sheets 3 are attached to the corresponding battery 2 in a harmonica tubular shape. With this configuration, the heat generated by the battery 2 is transferred to the liquid-gas conversion sheet 3 through the tubular spacer 34 of the harmonica, and not only the liquid refrigerant in the storage space 31 can be vaporized, but also the liquid refrigerant can be converted into a gaseous refrigerant. Capillary action (refers to the phenomenon that the immersion liquid rises in the thin tube and the non-wetting liquid descends in the thin tube), the liquid refrigerant can smoothly flow in the partition plate 34, and the bottom surface of the liquid storage tank 67 is high On the surface of the liquid-gas conversion sheet 3, the liquid refrigerant can be filled with the entire liquid-gas conversion sheet 3, thereby achieving a good heat dissipation effect. In other embodiments, the contact surface may also be in other configurations, which is not limited herein.
进一步地,请一并参阅图7,作为本发明提供的基于气液两相散热及热能回收的动力电池系统的一种具体实施方式,气体集流器7包括集气盒71,该集气盒71的两侧分别设有进口管72和出口管73,集气盒71中设有连通进口管72与出口管73的弯曲流道74。具体地,气体集流器7的两个侧面上分别设有通过第二连接管11与集气管5连通的进口管72和通过第三连接管12与气液转换器6的进气管64连通的出口管73,气体集流器7内设有用于传递制冷剂的弯曲流道74。带有大量电池2热量的气态制冷剂通过进口管72进入集气盒71中,弯曲流道74优选呈S型铺设在集气盒71中,因此可以增加气态制冷剂通过气体集流器7的路线长度,便于将气态制冷剂携带的大量热能传递至温差发电片8,提高热能的传递效率,从而提高热能转变为电能的效率,提高能源转化效率。在其它实施例中,弯曲流道74也可以设置成其它构型,在此不作唯一限定。Further, please refer to FIG. 7 as a specific embodiment of the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery provided by the present invention, the gas current collector 7 includes a gas collection box 71, and the gas collection box An inlet pipe 72 and an outlet pipe 73 are respectively disposed on both sides of the 71, and the gas collecting box 71 is provided with a curved flow passage 74 communicating with the inlet pipe 72 and the outlet pipe 73. Specifically, the two sides of the gas collector 7 are respectively provided with an inlet pipe 72 communicating with the gas collecting pipe 5 through the second connecting pipe 11 and an inlet pipe 64 communicating with the gas-liquid converter 6 through the third connecting pipe 12 The outlet pipe 73 and the gas current collector 7 are provided with a curved flow path 74 for transferring the refrigerant. The gaseous refrigerant having a large amount of heat of the battery 2 enters the gas collecting box 71 through the inlet pipe 72, and the curved flow path 74 is preferably laid in the gas collecting box 71 in an S-shape, so that the gaseous refrigerant can be increased through the gas current collector 7. The length of the route facilitates the transfer of a large amount of thermal energy carried by the gaseous refrigerant to the thermoelectric power generation sheet 8, thereby improving the heat transfer efficiency, thereby improving the efficiency of converting thermal energy into electrical energy and improving energy conversion efficiency. In other embodiments, the curved flow path 74 can also be configured in other configurations, which is not limited herein.
本发明的具体操作流程如下:将液态制冷剂从气液转换器6的注液口61注入储液箱67中,注液完成后,通过密封盖62将注液口61密封。由于储液箱67的底面高于液气转换片3的表面,在压强差和口琴管状的间隔板34的毛细作用下,液态制冷剂通过第一连接管10、连通管4和进液口32流入各液气转换片3中,电池2产生的热量将液态制冷剂汽化并转变为气态制冷剂,制冷剂由液态转变为气态的过程中,吸收电池2产生的热量,气态制冷剂从液气转换片3的排气口33排出,气态制冷剂经过集气管5、第二连接管11和气体集流器7的进口管72进入气体集流器7中,气态制冷剂将携带的大量电池2产生的热量传递至温差发电片8的热片81,在散热器9和空气的传热作用下,温差发电片8的热片81与冷片82之间产生温度梯度,并且在塞贝克效应的作用下,将热能转变为电能,电能经过正极输出端85和负极输出端86储存在蓄电池中。气态制冷剂从气体集流器7的出口管73排出,经过第三连接管12和气液转换器6的进气管64进入气液转换器6中,并在散热片65和空气的传热作用下,气态制冷剂液化并转变为液态制冷剂。The specific operation flow of the present invention is as follows: the liquid refrigerant is injected into the liquid storage tank 67 from the liquid injection port 61 of the gas-liquid converter 6, and after the liquid filling is completed, the liquid filling port 61 is sealed by the sealing cover 62. Since the bottom surface of the liquid storage tank 67 is higher than the surface of the liquid-gas conversion sheet 3, the liquid refrigerant passes through the first connecting pipe 10, the communication pipe 4, and the liquid inlet 32 under the pressure difference and the capillary action of the harmonical tubular spacer 34. Flowing into each of the liquid-gas conversion sheets 3, the heat generated by the battery 2 vaporizes and converts the liquid refrigerant into a gaseous refrigerant, and the heat generated by the battery 2 is absorbed in the process of converting the liquid from the liquid state to the gaseous state, and the gaseous refrigerant is from the liquid gas. The exhaust port 33 of the conversion sheet 3 is discharged, and the gaseous refrigerant enters the gas current collector 7 through the gas collecting pipe 5, the second connecting pipe 11 and the inlet pipe 72 of the gas current collector 7, and the large amount of the battery which the gaseous refrigerant will carry 2 The generated heat is transferred to the heat sheet 81 of the thermoelectric power generation sheet 8, and under the heat transfer action of the heat sink 9 and the air, a temperature gradient is generated between the heat sheet 81 of the thermoelectric power generation sheet 8 and the cold sheet 82, and in the Seebeck effect Under the action, the thermal energy is converted into electric energy, and the electric energy is stored in the storage battery through the positive output terminal 85 and the negative output terminal 86. The gaseous refrigerant is discharged from the outlet pipe 73 of the gas collector 7, passes through the third connecting pipe 12 and the intake pipe 64 of the gas-liquid converter 6, enters the gas-liquid converter 6, and is subjected to the heat transfer of the fins 65 and the air. The gaseous refrigerant liquefies and is converted into a liquid refrigerant.
其中,连通管4、集气管5、第一连接管10、第二连接管11和第三连接管12均由导热系数较低的塑胶材料制成,可防止热量的散失。在其它实施例中,也可以由其它导热系数较低的材料制成。气液转换片6、散热片65、气体集流器7、温差发电片8和散热器9均设置在箱体1的外侧,并设置在通风良好的地方。The communication tube 4, the air collection tube 5, the first connection tube 10, the second connection tube 11 and the third connection tube 12 are all made of a plastic material having a low thermal conductivity to prevent heat loss. In other embodiments, other materials having a lower thermal conductivity may also be made. The gas-liquid conversion sheet 6, the heat sink 65, the gas current collector 7, the thermoelectric power generation sheet 8, and the heat sink 9 are all disposed outside the casing 1, and are disposed in a well-ventilated place.
本发明提供的基于气液两相散热及热能回收的动力电池系统可用于对电池2的散热处理,特别适用于大功率的动力电池,且散热效果好,还能将电池2产生的热量转变为电能,能量得以回收利用,提高能量的利用率。制冷剂可由液态转变为气态,再从气态转变为液态,因此制冷剂可以重复使用,进一步提高能源的使用效率,节约使用成本。The power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery provided by the invention can be used for heat dissipation treatment of the battery 2, and is particularly suitable for a high-power power battery, and has good heat dissipation effect, and can also convert the heat generated by the battery 2 into Energy, energy can be recycled to improve energy utilization. The refrigerant can be converted from a liquid state to a gaseous state, and then from a gaseous state to a liquid state, so that the refrigerant can be reused, further improving the energy use efficiency and saving the use cost.
以上所述仅为本发明的较佳实施例而已,并不用以限制本发明,凡在本发明的精神和原则之内所作的任何修改、等同替换和改进等,均应包含在本发明的保护范围之内。The above is only the preferred embodiment of the present invention, and is not intended to limit the present invention. Any modifications, equivalent substitutions and improvements made within the spirit and principles of the present invention should be included in the protection of the present invention. Within the scope.

Claims (10)

  1. 基于气液两相散热及热能回收的动力电池系统,包括箱体和设于所述箱体内的多个电池,其特征在于:所述箱体内安装有用于吸收各所述电池发出热量的多个液气转换片,各所述液气转换片中均设有用于存储制冷剂的存储空间,各所述液气转换片的下端设有进液口,各所述液气转换片的上端开设有排气口;所述基于气液两相散热及热能回收的动力电池系统还包括用于收集各所述液气转换片排出的气体的气体集流器、将所述气体集流器排出气体转换为液体的气液转换器和将所述气体集流器散出的热量转换为电能的温差发电片,所述温差发电片贴于所述气体集流器上,所述气液转换器的入口与所述气体集流器的出口相连通,所述气体集流器的入口与各所述排气口相连通,所述气液转换器的出口与各所述进液口相连通。A power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery, comprising a box body and a plurality of batteries disposed in the box body, wherein: a plurality of batteries for absorbing heat generated by each of the batteries are installed in the box body a liquid-gas conversion sheet, wherein each of the liquid-gas conversion sheets is provided with a storage space for storing a refrigerant, and a liquid inlet port is disposed at a lower end of each of the liquid-gas conversion sheets, and an upper end of each of the liquid-gas conversion sheets is opened An exhaust port; the power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery further includes a gas current collector for collecting gas discharged from each of the liquid-gas conversion sheets, and converting the gas collector exhaust gas a gas-liquid converter for liquid and a thermoelectric power generation sheet for converting heat dissipated from the gas current collector into electrical energy, the thermoelectric power generation sheet being attached to the gas current collector, the inlet of the gas-liquid converter An inlet of the gas current collector is in communication with an outlet of the gas current collector, and an outlet of the gas-liquid converter is in communication with each of the liquid inlets.
  2. 如权利要求1所述的基于气液两相散热及热能回收的动力电池系统,其特征在于:还包括用于对所述温差发电片进行散热的散热器,所述散热器和所述气体集流器配合夹持所述温差发电片。A power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery according to claim 1, further comprising: a heat sink for dissipating heat of said thermoelectric power generation piece, said heat sink and said gas set The flow device cooperates to clamp the thermoelectric power generation piece.
  3. 如权利要求1所述的基于气液两相散热及热能回收的动力电池系统,其特征在于:还包括连通各所述进液口的连通管,所述连通管与所述气液转换器的出口相连。A power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery according to claim 1, further comprising: a communication pipe that communicates with each of said liquid inlets, said communication pipe and said gas-liquid converter Exports are connected.
  4. 如权利要求1所述的基于气液两相散热及热能回收的动力电池系统,其特征在于:还包括连通各所述排气口的集气管,所述集气管与所述气体集流器的入口相连。A power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery according to claim 1, further comprising: a gas collecting pipe that communicates with each of said exhaust ports, said gas collecting pipe and said gas current collector The entrance is connected.
  5. 如权利要求1所述的基于气液两相散热及热能回收的动力电池系统,其特征在于:所述气液转换器包括储液箱,所述储液箱的底面安装有连接各所述进液口的出液管,所述储液箱的侧面安装有连通所述气体集流器的进气管。A gas-liquid two-phase heat dissipation and heat energy recovery power battery system according to claim 1, wherein said gas-liquid converter comprises a liquid storage tank, and said bottom surface of said liquid storage tank is connected with said each An outlet pipe of the liquid port, the side of the liquid storage tank is provided with an intake pipe that communicates with the gas current collector.
  6. 如权利要求5所述的基于气液两相散热及热能回收的动力电池系统,其特征在于:所述储液箱的顶面设有注液口,所述气液转换器还包括盖于所述注液口上的密封盖。The power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery according to claim 5, wherein the top surface of the liquid storage tank is provided with a liquid injection port, and the gas-liquid converter further comprises a cover Describe the sealing cap on the liquid port.
  7. 如权利要求5所述的基于气液两相散热及热能回收的动力电池系统,其特征在于:所述气液转换器还包括安装于所述储液箱上的若干散热片。The power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery according to claim 5, wherein the gas-liquid converter further comprises a plurality of fins mounted on the liquid storage tank.
  8. 如权利要求1所述的基于气液两相散热及热能回收的动力电池系统,其特征在于:所述液气转换片中设有将所述存储空间分隔成若干竖直流道的间隔板。The power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery according to claim 1, wherein the liquid-gas conversion sheet is provided with a partition plate that divides the storage space into a plurality of vertical DC channels.
  9. 如权利要求1所述的基于气液两相散热及热能回收的动力电池系统,其特征在于:所述气体集流器包括集气盒,所述集气盒的两侧分别设有进口管和出口管,所述集气盒中设有连通所述进口管与所述出口管的弯曲流道。The gas battery system for gas-liquid two-phase heat dissipation and heat energy recovery according to claim 1, wherein the gas current collector comprises a gas collecting box, and two sides of the gas collecting box are respectively provided with an inlet pipe and An outlet pipe, wherein the gas collecting box is provided with a curved flow passage connecting the inlet pipe and the outlet pipe.
  10. 如权利要求9所述的基于气液两相散热及热能回收的动力电池系统,其特征在于:所述弯曲流道呈S型铺设于所述集气盒中。The power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery according to claim 9, wherein the curved flow path is S-shaped and laid in the gas collecting box.
PCT/CN2017/115990 2017-12-11 2017-12-13 Power battery system based on gas-liquid two-phase heat dissipation and heat energy recovery WO2019113846A1 (en)

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