CN111333868A - Composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities, preparation method and thermal management method - Google Patents

Composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities, preparation method and thermal management method Download PDF

Info

Publication number
CN111333868A
CN111333868A CN202010224414.8A CN202010224414A CN111333868A CN 111333868 A CN111333868 A CN 111333868A CN 202010224414 A CN202010224414 A CN 202010224414A CN 111333868 A CN111333868 A CN 111333868A
Authority
CN
China
Prior art keywords
hydrogel
waste heat
heat dissipation
heat recovery
composite
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
CN202010224414.8A
Other languages
Chinese (zh)
Inventor
刘抗
胡雪蛟
蒲诗睿
廖雨田
傅佳
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.)
Wuhan University WHU
Original Assignee
Wuhan University WHU
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 Wuhan University WHU filed Critical Wuhan University WHU
Priority to CN202010224414.8A priority Critical patent/CN111333868A/en
Publication of CN111333868A publication Critical patent/CN111333868A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/02Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
    • C08J3/03Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in aqueous media
    • C08J3/075Macromolecular gels
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00Processes of polymerisation
    • C08F2/46Polymerisation initiated by wave energy or particle radiation
    • C08F2/48Polymerisation initiated by wave energy or particle radiation by ultraviolet or visible light
    • C08F2/50Polymerisation initiated by wave energy or particle radiation by ultraviolet or visible light with sensitising agents
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/52Amides or imides
    • C08F220/54Amides, e.g. N,N-dimethylacrylamide or N-isopropylacrylamide
    • C08F220/56Acrylamide; Methacrylamide
    • HELECTRICITY
    • H05ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05KPRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
    • H05K7/00Constructional details common to different types of electric apparatus
    • H05K7/20Modifications to facilitate cooling, ventilating, or heating
    • H05K7/2029Modifications to facilitate cooling, ventilating, or heating using a liquid coolant with phase change in electronic enclosures
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2335/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a carboxyl radical, and containing at least one other carboxyl radical in the molecule, or of salts, anhydrides, esters, amides, imides or nitriles thereof; Derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/16Halogen-containing compounds
    • C08K2003/162Calcium, strontium or barium halides, e.g. calcium, strontium or barium chloride
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/16Halogen-containing compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/28Nitrogen-containing compounds

Abstract

The invention discloses a composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities, a preparation method and a thermal management method. Firstly, preparing hydrogel with a cross-linked structure; and then heating and drying the hydrogel with the cross-linked structure, and then soaking the dried hydrogel in a solution formed by hygroscopic salt and a chemical thermoelectric material until the hydrogel is completely swelled, and taking out the hydrogel to obtain the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities. The hydrogel can take away a large amount of heat by water evaporation at high temperature, and simultaneously converts a part of heat into electric energy for output in a chemical thermoelectric conversion mode; the water in the air can be absorbed at low temperature for automatic water replenishing. The invention has the characteristics of simple structure, excellent performance, convenience and intelligence, can synchronously remove waste heat and recover waste heat for a heating object, and solves the problem of waste of high-heat and low-grade heat energy.

Description

Composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities, preparation method and thermal management method
Technical Field
The invention belongs to the field of heat dissipation and waste heat recovery, relates to a synchronous heat dissipation and waste heat recovery technology, and particularly relates to a composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities, a preparation method and a heat management method.
Background
The miniaturization and integration of modern electronic devices make the electronic devices have huge energy density during operation, and most of energy is finally converted into heat energy, so that the devices face the problem of overhigh temperature. The poor temperature not only affects the stability of the device operation, but also causes problems of safety and service life. Therefore, solving the high temperature problem of the device is crucial to improving the energy efficiency of the device, promoting economic prosperity, energy safety and environmental protection. In addition, waste heat generated when electronic devices work generally belongs to low-grade waste heat, and plays an important role in the strategy of energy conservation and emission reduction for recycling the low-grade waste heat under the background of global environmental pollution, energy shortage and low energy utilization rate. Modern electronic devices have high requirements for efficient heat dissipation and waste heat recovery because these two components are related to device reliability and energy efficiency.
The existing heat dissipation methods mainly include two types: passive heat dissipation and active heat dissipation. Modern electronic devices have extremely high energy density, and the low heat dissipation capability of common passive methods is difficult to meet the requirements of high energy density devices. Although the active cooling methods such as forced air cooling and water cooling have high cooling performance, the energy consumption is high, and complex auxiliary accessories (such as a fan, a water pump and the like) are required. Conventional heat recovery methods, such as thermoelectric modules, in direct contact with a heat source typically introduce additional thermal resistance, hinder heat dissipation, and result in high temperatures in the core components of these electronic devices. However, efficient heat dissipation is often energy intensive, as it requires auxiliary equipment such as fans or pumps, which is undesirable for the purpose of improving the energy efficiency of the device. Thus, efficient heat removal and waste heat recovery are two conflicting processes so far that they cannot be achieved simultaneously. Moreover, the effective heat dissipation and waste heat recovery method must also follow the development direction of modern electronic devices.
Hydrogels, a class of materials with extremely high water content (which can exceed 90%), are capable of retaining their three-dimensional network structure and are in a solid state. The hydrogel can be used for reducing the surface temperature of an object greatly when the surface temperature of the object is increased, and is an excellent passive heat dissipation material. In addition, the liquid water in the hydrogel can prevent the actions of ion diffusion and transmission and the like from being influenced. However, conventional hydrogels lose water continuously, and even at room temperature, the water content in the hydrogel gradually decreases until the hydrogel is completely dried, and thus the hydrogel is not environmentally stable. In addition, the water loss of common hydrogel can not be automatically reversed, and the hydrogel can be recovered only by soaking the hydrogel in liquid water, and then normally works. These drawbacks make the application of hydrogels limited, and frequent manual water replenishment also affects the stability and effectiveness of the hydrogel structure and properties. Therefore, it is important to find an intelligent, simple and efficient heat dissipation and waste heat recovery mode.
Disclosure of Invention
In order to solve the problems of high heat and waste heat waste of various heat sources and solve the problems that hydrogel at the present stage does not have environmental stability and cannot realize automatic water replenishing, the invention provides the composite hydrogel which can realize synchronous heat dissipation and waste heat recovery and can realize automatic water replenishing, and the composite hydrogel can be applied to the fields of heat management and waste heat recycling. The intelligent type water heater has the characteristics of intelligence, convenience, repeatable work, adjustable volume, zero noise, low manufacturing cost and wide application range. The method can be suitable for the surfaces of various heat source objects, such as: electronic equipment, houses, automobiles, and the like.
In order to solve the technical problems, the invention adopts the technical scheme that:
the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities is characterized in that: the hydrogel is a composite hydrogel composed of hydrogel with a three-dimensional cross-linked structure, hygroscopic salt with a certain concentration and a chemical thermoelectric material mixed solution. Moreover, the hydrogel can have the capabilities of heat dissipation, waste heat recovery and automatic regeneration.
Preferably, the hydrogel with the three-dimensional crosslinking structure is any one or a combination of several of polyacrylamide hydrogel, sodium polyacrylate hydrogel, sodium alginate hydrogel and polyvinyl alcohol hydrogel.
A preparation method of hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability is characterized by comprising the following steps:
step 1, preparing hydrogel with a three-dimensional cross-linked structure;
step 2, heating and drying the hydrogel prepared in the step 1 until the hydrogel is completely dried;
step 3, soaking the dried polyacrylamide hydrogel in a mixed solution consisting of hygroscopic salt and a chemical thermoelectric material;
and 4, taking out the hydrogel until the hydrogel is completely swelled, thereby obtaining the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities.
As an improvement, the hygroscopic salt is lithium bromide, lithium chloride or calcium chloride salt, and the molar concentration of the hygroscopic salt is 0-17.3 mol/L.
As an improvement, the chemical thermoelectric material is potassium ferricyanide/potassium ferrocyanide or potassium ferricyanide/ammonium ferrocyanide, and the molar concentration of the chemical thermoelectric material is 0-0.4 mol/L.
A thermal management-waste heat recovery method using the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability is characterized in that: placing the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities on the surface of a heat source, wherein when the temperature of the surface of the heat source rises, water in the hydrogel starts to evaporate, the surface temperature of a heating element is greatly reduced, and meanwhile, a part of heat is converted into electric energy through chemical thermoelectric conversion and is output; when the surface temperature of the heat source is reduced, the composite hydrogel with the synchronous evaporation heat dissipation and waste heat recovery capabilities spontaneously absorbs the moisture in the surrounding air, so that the composite hydrogel with the synchronous evaporation heat dissipation and waste heat recovery capabilities swells again. The circulation work is carried out in this way, and the surface temperature control and the waste heat reutilization of the heat source are completed.
As an improvement, the heat source is a solar cell, a house, an automobile, a chip, a battery, and an integrated circuit.
The invention has the beneficial effects that:
in summary, the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability of the present invention has the functions of evaporation heat dissipation, waste heat recovery and automatic regeneration. The hydrogel temperature control method belongs to a passive heat dissipation method, has a simple structure and excellent heat dissipation capacity, and can intelligently and effectively dissipate heat for various objects (electronic equipment, houses, automobiles and the like) needing temperature management. The thermoelectric conversion mode in the invention belongs to a chemical thermoelectric conversion mode, and the entropy change of redox couple in a thermoelectric chemical material in the processes of migration in a solution and electron transfer is the root cause of energy conversion.
The automatic regeneration function of the hydrogel is regulated and controlled by hygroscopic salt, the hygroscopic salt can obviously reduce the vapor pressure of the hydrogel, and the evaporation-regeneration rate of the hydrogel can be controlled by regulating the concentration of the hygroscopic salt. The hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability is formed by compounding hydrogel with a three-dimensional cross-linked structure, hygroscopic salt and a thermoelectric chemical material solution. The working mode is as follows: under high temperature, water in the hydrogel can be evaporated to take away a large amount of heat, the temperature of a heat source is controlled, and the thermoelectric conversion is synchronously realized to convert redundant heat energy into electric energy for output; at low temperature, the hydrogel can automatically absorb water in the air to automatically supplement water and restore the swelling state. The hydrogel can be reused and has automatic circulation capability. The device does not need external power during working, and has the characteristics of no noise, small volume, low manufacturing cost, convenience, intelligence, adjustable volume, zero noise and wide application range.
Drawings
FIG. 1 is a schematic diagram of the cyclic evaporation-moisture absorption process of the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability used in example 1 when the chip works, wherein E represents evaporation, and R represents water absorption.
FIG. 2 is a schematic diagram showing the heat dissipation performance of the chip made of the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities in example 1;
FIG. 3 is a schematic diagram of the waste heat recovery performance of the chip made of the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities in example 1.
FIG. 4 is a schematic diagram illustrating the heat dissipation performance of the lithium ion battery of the mobile phone in the case of using the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability in example 2;
fig. 5 shows the waste heat recovery capability (I-V curve) of the lithium ion battery of the mobile phone, which is the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability used in example 2.
Fig. 6 shows the time required for automatic water replenishment when the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capacity used in example 2 is a lithium ion battery for a mobile phone.
FIG. 7 is a schematic diagram showing the heat dissipation performance of the perovskite solar cell panel used in example 3, wherein the composite hydrogel having the synchronous evaporation heat dissipation and waste heat recovery capabilities is used;
FIG. 8 is the waste heat recovery capability (I-V curve) of perovskite solar cell panel used as the composite hydrogel with synchronous evaporative heat dissipation and waste heat recovery capability in example 3.
Detailed Description
The embodiments of the present invention will be described in further detail with reference to the drawings and examples. The following examples are intended to illustrate the present invention, but are not intended to limit the scope of the present invention, and the examples of the present invention are illustrated by taking polyacrylamide hydrogel as an example, and other hydrogels are also applicable.
The invention provides a composite hydrogel for heat management and waste heat recycling of a heat source surface, which is a material consisting of polyacrylamide hydrogel, hygroscopic salt with a certain concentration and a chemical thermoelectric material solution. The hygroscopic salt is lithium bromide, lithium chloride, calcium chloride and the like, and the molar concentration is 0-17.3 mol/L. The chemical thermoelectric material is potassium ferricyanide/potassium ferrocyanide or potassium ferricyanide/ammonium ferrocyanide and the like, and the molar concentration is 0-0.4 mol/L. The composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability has a smooth surface and can be directly covered on the surface of a heat source. The concentration of the mixed solution consisting of hygroscopic salt and chemical thermoelectric material in the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability is adjustable, so that effective moisture absorption, heat dissipation and waste heat recovery under different environments and different heating element surface temperatures are realized. The preparation method of the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capacity comprises the following steps:
step 1, preparation of polyacrylamide hydrogel
And 2, completely drying a certain amount of polyacrylamide hydrogel.
And 3, soaking the dried polyacrylamide hydrogel in a mixed solution consisting of hygroscopic salts and the chemical thermoelectric material, wherein the hygroscopic salts are as follows: lithium bromide, lithium chloride, calcium chloride and the like, and the molar concentration is 0-17.3 mol/L; the chemical thermoelectric material is potassium ferricyanide/potassium ferrocyanide or potassium ferricyanide/ammonium ferrocyanide, etc. and its molar concentration is 0-0.4 mol/L.
And 4, taking out the hydrogel until the hydrogel is completely swelled. Namely the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability.
In the invention, when the surface temperature of heating elements such as electronic equipment, houses, automobiles and the like is overhigh, the water in the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability can be evaporated, the surface temperature of a heat source is reduced, and meanwhile, a part of heat energy is converted into electric energy. When the electronic equipment is in a standby state, a house is in a night period and an automobile is not used, automatic water absorption and regeneration from the surrounding environment can be realized. The whole process is temperature controlled and works automatically. The speed of the hydrogel in the evaporation and water absorption processes is controlled by the molar concentration of the hygroscopic salt solution, and the concentration of the hygroscopic salt solution can be regulated and controlled according to different working conditions of a heat source, so that effective heat dissipation and waste heat recycling are realized.
The principle used by the invention is as follows: the principle of automatic regeneration of the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability is that the saturated vapor pressure of hygroscopic salt is very low, and when the composite hydrogel contains the hygroscopic salt, the vapor pressure of the composite hydrogel is controlled by the concentration of the hygroscopic salt. When the vapor pressure of the composite hydrogel is lower than that of the environment, the composite hydrogel can automatically absorb water from the environment. The heat dissipation mechanism is that the saturated vapor pressure of the composite hydrogel with the synchronous evaporation heat dissipation and waste heat recovery capabilities at high temperature is higher than that of the environment, so that when the surface temperature of a heat source is too high, water can be evaporated from the composite hydrogel with the synchronous evaporation heat dissipation and waste heat recovery capabilities, and a large amount of heat can be taken away due to the large latent heat of water. The principle of thermoelectric conversion is that when temperature difference exists between two surfaces of the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities, oxidation reaction occurs on an anode and reduction reaction occurs on a cathode of an oxidation-reduction pair in a chemical thermoelectric material due to the fact that the oxidation-reduction reaction has temperature dependence, and entropy change in the processes of ion migration in a solution and electron transfer is a main reason of energy conversion in the processes.
Example 1
The specific preparation method of the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability provided by the embodiment is as follows:
step 1, 2M acrylamide is taken as a monomer, 0.001M N N '-dimethyl bisacrylamide is taken as a cross-linking agent, and 0.002M 2-hydroxy-4' - (2-hydroxyethoxy) -2-methyl propiophenone is taken as an ultraviolet initiator to prepare a mixed solution.
Step 2, pouring the solution obtained in the step 1 into 10 × 5 × 3.6.6 cm3In the mold of (1).
And 3, curing for 8 hours in a nitrogen atmosphere by using an ultraviolet lamp to obtain the polyacrylamide hydrogel.
And 4, taking the polyacrylamide hydrogel out of the mold, and placing the polyacrylamide hydrogel on a heating table at 60 ℃ until the polyacrylamide hydrogel is completely dried.
And 5, immersing the dried polyacrylamide hydrogel into a mixed solution of potassium ferricyanide/potassium ferrocyanide (0.1M) and lithium bromide (9.4M) until the polyacrylamide hydrogel is completely swelled.
And 6, taking out the gel, and wiping redundant solution on the surface to form the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities.
The composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability in the embodiment is used for testing the synchronous heat dissipation, waste heat recovery and automatic water replenishing performance of the chip as follows:
the evaporation-moisture absorption cycle capacity test is carried out at the ambient temperature of 25 ℃, the ambient relative humidity of 70 percent and the hydrogel sample size of 30mm × 25mm × 3.6.6 mm, the evaporation of the hydrogel is carried out at the temperature of 50 ℃, the moisture absorption is carried out under the ambient condition, the weight change of the hydrogel is recorded by a balance with the precision of 0.01mg, the water loss in the whole evaporation process is 0.418g, the evaporation time is 1.7h, the time required by the hydrogel to return to the initial state in the automatic water replenishing process is 5.88h, the water evaporation amount of the hydrogel is consistent after 4 cycle tests, the time required by evaporation and regeneration is also basically consistent, the power density is 1333W/m at the ambient temperature of 25 ℃, the ambient relative humidity of 70 percent and the hydrogel sample size of 30mm × 25mm × 3.6.6 mm2The chip carries out synchronous heat dissipation and waste heat recovery capability test. A titanium sheet is arranged between the heating sheet and the hydrogel, the surface of the hydrogel is a titanium net, the titanium sheet and the titanium net are used as electrodes to collect output current and voltage of the hydrogel, and the titanium net covers the surface of the hydrogel to ensure that water vapor can pass through. In the case of sweating cooling with hydrogel, the chip surface temperature would be kept between 39 ℃ and 45 ℃ with the chip temperature rising to 61 ℃ without any heat dissipation measures, which is the maximum chip temperature of 22 ℃. At the same time, 0.28. mu.W of electric power was output at 120 minutes.
Example 2
The specific preparation method of the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability provided by the embodiment is as follows:
step 1, 2M acrylamide is taken as a monomer, 0.001M N N '-dimethyl bisacrylamide is taken as a cross-linking agent, and 0.002M 2-hydroxy-4' - (2-hydroxyethoxy) -2-methyl propiophenone is taken as an ultraviolet initiator to prepare a mixed solution.
Step 2, mixing the mixed solution obtained in the step 1Pouring 10 × 6 × 2cm3In the mold of (1).
And 3, curing for 8 hours in a nitrogen atmosphere by using an ultraviolet lamp to obtain the polyacrylamide hydrogel.
And 4, taking the polyacrylamide hydrogel out of the mold, and placing the polyacrylamide hydrogel on a heating table at 60 ℃ until the polyacrylamide hydrogel is completely dried.
And 5, immersing the dried polyacrylamide hydrogel in a mixed solution of potassium ferricyanide/potassium ferrocyanide (0.1M) and lithium bromide (5.4M) until the polyacrylamide hydrogel is completely swelled.
And 6, taking out the gel, and wiping redundant solution on the surface to form the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities.
The composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability in the embodiment is used for synchronous heat dissipation and waste heat recovery and automatic water replenishing performance tests of the lithium ion battery of the mobile phone as follows:
RH., testing the natural heat dissipation effect of the lithium ion battery and the heat dissipation effect of the hydrogel sweating cooling mode under different discharge rates and testing the waste heat utilization capacity of the lithium ion battery under the heat dissipation of the hydrogel, wherein the environment temperature and the humidity are respectively 26 ℃ and 80%, the capacity of the lithium ion battery is 5000mAh, the rated voltage is 3.7V, and the size of the hydrogel is 10cm × 6cm × 2mm, under the condition that no heat dissipation measures are adopted, the surface temperature of the lithium ion battery reaches 49 ℃, 62 ℃, 69 ℃ and 78 ℃ under the discharge rates of 1.6C, 1.8C, 2.0C and 2.2C, the temperature of the battery can be respectively reduced by 6.5 ℃, 13.2 ℃, 15.7 ℃ and 20 ℃ under the condition that the hydrogel dissipates heat, the hydrogel outputs 14.5mV voltage and 1.4mA current under the discharge rate of 2.2C, 5 uW of electric energy is additionally obtained through the hydrogel, under the same environment condition, the test shows that the lithium ion battery stops working after the work at different discharge rates, the automatic water replenishment time is 16min, the water replenishment time is 1.193 min, and the water replenishment time is respectively 1.8.2 min, the regeneration time is 1.8C, the water replenishment time is 1.2 min, the automatic regeneration time is 1.2 min, the water replenishment time is 1.2.2.2.
Example 3
The specific preparation method of the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability provided by the embodiment is as follows:
step 1, 2M acrylamide is taken as a monomer, 0.001M N N '-dimethyl bisacrylamide is taken as a cross-linking agent, and 0.002M 2-hydroxy-4' - (2-hydroxyethoxy) -2-methyl propiophenone is taken as an ultraviolet initiator to prepare a mixed solution.
And 2, pouring the mixed solution obtained in the step 1 into a mold of 10 × 10 and 10 × 4cm 3.
And 3, curing for 8 hours in a nitrogen atmosphere by using an ultraviolet lamp to obtain the polyacrylamide hydrogel.
And 4, taking the polyacrylamide hydrogel out of the mold, and placing the polyacrylamide hydrogel on a heating table at 60 ℃ until the polyacrylamide hydrogel is completely dried.
And 5, immersing the dried polyacrylamide hydrogel in a mixed solution of potassium ferricyanide/potassium ferrocyanide (0.1M) and lithium bromide (5.4M) until the polyacrylamide hydrogel is completely swelled.
And 6, taking out the gel, and wiping redundant solution on the surface to form the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities.
The performance test of the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability used for the synchronous heat dissipation and the waste heat recovery of the solar cell in the embodiment is as follows:
in one sun (100 mW/cm)2) Under the illumination of light, the surface temperature of the perovskite cell capable of naturally dissipating heat reaches 73 ℃, while the surface temperature of the solar cell panel using hydrogel (with the size of 10cm × 10cm × 4mm) for dissipating heat is only 53 ℃ in the initial stage, the temperature is gradually increased to 58 ℃ after 6.5 hours, the temperature is reduced by 15 ℃ to 20 ℃, an I-V curve output by the hydrogel is scanned within 6.5 hours while the TG hydrogel is subjected to sweating cooling, the current at the moment is 1.27mA, the voltage can reach 10mV, and the extra electric gain obtained by the hydrogel at the moment is 3.2 muW.
The above embodiments are merely illustrative of the present invention and are not to be construed as limiting the invention. Although the present invention has been described in detail with reference to the embodiments, it should be understood by those skilled in the art that various combinations, modifications or equivalents may be made to the technical solution of the present invention without departing from the spirit and scope of the technical solution of the present invention, and the technical solution of the present invention is covered by the claims of the present invention.

Claims (10)

1. The composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities is characterized in that: the hydrogel is a composite hydrogel composed of hydrogel with a three-dimensional cross-linked structure, hygroscopic salt with a certain concentration and a chemical thermoelectric material mixed solution.
2. The composite hydrogel of claim 1, wherein: the hydrogel with the three-dimensional crosslinking structure is any one or a combination of several of polyacrylamide hydrogel, sodium polyacrylate hydrogel, sodium alginate hydrogel and polyvinyl alcohol hydrogel.
3. The composite hydrogel of claim 1, wherein: the hygroscopic salt is lithium bromide, lithium chloride or calcium chloride salt, and the molar concentration of the hygroscopic salt is 0-17.3 mol/L.
4. The composite hydrogel of claim 1, wherein: the chemical thermoelectric material is potassium ferricyanide/potassium ferrocyanide or potassium ferricyanide/ammonium ferrocyanide, and the molar concentration of the chemical thermoelectric material is 0-0.4 mol/L.
5. A preparation method of composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability is characterized by comprising the following steps:
step 1, preparing hydrogel with a three-dimensional cross-linked structure;
step 2, heating and drying the hydrogel prepared in the step 1 until the hydrogel is completely dried;
step 3, soaking the dried hydrogel in a mixed solution consisting of hygroscopic salt and a chemical thermoelectric material;
and 4, taking out the hydrogel until the hydrogel is completely swelled, thereby obtaining the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities.
6. The method for preparing the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability according to claim 5, wherein the method comprises the following steps: the hygroscopic salt is lithium bromide, lithium chloride or calcium chloride salt, and the molar concentration of the hygroscopic salt is 0-17.3 mol/L.
7. The method for preparing composite hydrogel with synchronous heat dissipation and waste heat recovery capability according to claim 5, wherein the chemical thermoelectric material is potassium ferricyanide/potassium ferrocyanide or potassium ferricyanide/ammonium ferrocyanide, and the molar concentration of the chemical thermoelectric material is 0-0.4 mol/L.
8. The method for preparing the composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capability according to claim 5, wherein the method comprises the following steps: the hydrogel in the step 1 is polyacrylamide hydrogel, and the preparation method of the polyacrylamide hydrogel comprises the following steps:
step 1.1, preparing a mixed solution by using acrylamide as a monomer, N '-dimethyl bisacrylamide as a cross-linking agent and 2-hydroxy-4' - (2-hydroxyethoxy) -2-methyl propiophenone as an ultraviolet initiator;
step 1.2, pouring the mixed solution obtained in the step 1.1 into a mold;
and step 1.3, curing for 6-10 hours under the nitrogen atmosphere by using an ultraviolet lamp to obtain the polyacrylamide hydrogel.
9. A method for heat management-waste heat recovery using the composite hydrogel according to any one of claims 1 to 5, wherein: placing the hydrogel on the surface of a heat source, gradually evaporating moisture in the hydrogel when the temperature of the surface of the heat source is increased, reducing the surface temperature of the heat source, and converting a part of heat into electric energy through chemical thermoelectric conversion for output; when the surface temperature of the heat source is reduced, the hydrogel can spontaneously absorb the moisture in the surrounding air, so that the hydrogel is regenerated and automatically and circularly works to finish the surface temperature reduction and waste heat recycling of the heat source, and then is automatically regenerated.
10. The thermal management-waste heat recovery method of claim 9, wherein: the heat source is a solar panel, a house, an automobile, a chip, a battery or an integrated circuit.
CN202010224414.8A 2020-03-26 2020-03-26 Composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities, preparation method and thermal management method Pending CN111333868A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202010224414.8A CN111333868A (en) 2020-03-26 2020-03-26 Composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities, preparation method and thermal management method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202010224414.8A CN111333868A (en) 2020-03-26 2020-03-26 Composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities, preparation method and thermal management method

Publications (1)

Publication Number Publication Date
CN111333868A true CN111333868A (en) 2020-06-26

Family

ID=71178461

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202010224414.8A Pending CN111333868A (en) 2020-03-26 2020-03-26 Composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities, preparation method and thermal management method

Country Status (1)

Country Link
CN (1) CN111333868A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112103560A (en) * 2020-09-16 2020-12-18 武汉大学 Hygroscopic hydrogel-based battery and preparation method thereof
CN112652698A (en) * 2020-12-23 2021-04-13 广东省科学院化工研究所 Thermoelectric conversion material and thermoelectric conversion device
CN113178515A (en) * 2021-04-26 2021-07-27 重庆大学 Hydrogel thermoelectric material based on ionic liquid and preparation method thereof
CN113644785A (en) * 2021-10-14 2021-11-12 启东市飞宏自动化设备有限公司 Heat dissipation protection device for motor
CN113741095A (en) * 2021-08-27 2021-12-03 Tcl华星光电技术有限公司 Heat dissipation gel, heat dissipation device, light source module and display panel
CN113881068A (en) * 2021-11-01 2022-01-04 南开大学 Preparation method and application of high-performance thermoelectric hydrogel based on ion conduction
CN114479332A (en) * 2021-12-29 2022-05-13 广东省科学院化工研究所 Ion conductor thermoelectric material and preparation method and application thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070295616A1 (en) * 2006-06-27 2007-12-27 Agamatrix, Inc. Detection of Analytes in a Dual-mediator Electrochemical Test Strip
CN109943002A (en) * 2019-04-02 2019-06-28 武汉大学 It is a kind of from moisture absorption hydrogel, preparation method and based on its thermal management algorithm
CN110156943A (en) * 2019-06-24 2019-08-23 四川轻化工大学 A kind of preparation method and application of hydrogel material

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070295616A1 (en) * 2006-06-27 2007-12-27 Agamatrix, Inc. Detection of Analytes in a Dual-mediator Electrochemical Test Strip
CN109943002A (en) * 2019-04-02 2019-06-28 武汉大学 It is a kind of from moisture absorption hydrogel, preparation method and based on its thermal management algorithm
CN110156943A (en) * 2019-06-24 2019-08-23 四川轻化工大学 A kind of preparation method and application of hydrogel material

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
RUSSO, MATTHEW ET AL.: "Hydrogels Containing the Ferri/Ferrocyanide Redox Couple and Ionic Liquids for Thermocells", 《AUSTRALIAN JOURNAL OF CHEMISTRY》 *

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112103560A (en) * 2020-09-16 2020-12-18 武汉大学 Hygroscopic hydrogel-based battery and preparation method thereof
CN112103560B (en) * 2020-09-16 2021-11-26 武汉大学 Hygroscopic hydrogel-based battery and preparation method thereof
CN112652698A (en) * 2020-12-23 2021-04-13 广东省科学院化工研究所 Thermoelectric conversion material and thermoelectric conversion device
CN113178515A (en) * 2021-04-26 2021-07-27 重庆大学 Hydrogel thermoelectric material based on ionic liquid and preparation method thereof
CN113178515B (en) * 2021-04-26 2022-11-01 重庆大学 Hydrogel thermoelectric material based on ionic liquid and preparation method thereof
CN113741095A (en) * 2021-08-27 2021-12-03 Tcl华星光电技术有限公司 Heat dissipation gel, heat dissipation device, light source module and display panel
CN113644785A (en) * 2021-10-14 2021-11-12 启东市飞宏自动化设备有限公司 Heat dissipation protection device for motor
CN113881068A (en) * 2021-11-01 2022-01-04 南开大学 Preparation method and application of high-performance thermoelectric hydrogel based on ion conduction
CN114479332A (en) * 2021-12-29 2022-05-13 广东省科学院化工研究所 Ion conductor thermoelectric material and preparation method and application thereof
CN114479332B (en) * 2021-12-29 2023-12-05 广东省科学院化工研究所 Ion conductor thermoelectric material and preparation method and application thereof

Similar Documents

Publication Publication Date Title
CN111333868A (en) Composite hydrogel with synchronous evaporation heat dissipation and waste heat recovery capabilities, preparation method and thermal management method
CN109943002B (en) Self-moisture-absorption hydrogel, preparation method and heat management method based on same
JP3599859B2 (en) Porous substance-polymer solid electrolyte composite, method for producing the same, and photoelectric conversion element using the same
CN109921154B (en) Flexible zinc-air battery based on polymer electrolyte
CN110212242B (en) Porous gel polymer electrolyte and preparation method thereof
CN202996862U (en) Backboard and photovoltaic assembly
KR20140144117A (en) electrode modification method for all vanadium redox flow battery using hydrophilic polymer
CN111952675A (en) High-performance all-solid-state sodium ion battery and preparation method thereof
Li et al. A hygroscopic composite backplate enabling passive cooling of photovoltaic panels
CN113690344A (en) Preparation and application of high-water-absorptivity hydrogel for heat dissipation of solar cell back panel
Zeng et al. Moisture thermal battery with autonomous water harvesting for passive electronics cooling
CN112103560B (en) Hygroscopic hydrogel-based battery and preparation method thereof
CN114695973A (en) Preparation method of low-temperature zinc ion battery
CN113506910A (en) Sodium ion composite solid electrolyte and preparation method thereof
CN114058060A (en) Conductive polymer hydrogel, preparation method thereof and electricity generating device
CN114400706A (en) Control method and system of photovoltaic power generation system
CN107293799B (en) Cyanoethyl cellulose glycerol ether film, cyanoethyl cellulose glycerol ether gel polymer electrolyte and preparation method thereof
CN116111142A (en) Alkaline negative electrode electrolyte and alkaline zinc-iron flow battery assembled by same
CN114539703A (en) Intelligent color-changing heat dissipation hydrogel and application thereof
CN106848395B (en) A kind of low cost solid electrolyte film
CN111732804B (en) Temperature control piece with adhesive property, and manufacturing method and application thereof
CN114109221B (en) Energy-saving and power generation integrated intelligent window and preparation thereof
CN218038858U (en) Dry capacitor with moisture-proof assembly
CN107845506A (en) A kind of reinforced stone mertenyl ultracapacitor and preparation method thereof
CN117186475B (en) Preparation method of organic carboxylic ether modified cation exchange membrane for alkaline flow battery

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination