CN213583875U - Water heat exchange membrane assembly, water heat exchange device, and fuel cell system - Google Patents
Water heat exchange membrane assembly, water heat exchange device, and fuel cell system Download PDFInfo
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- CN213583875U CN213583875U CN202022357223.7U CN202022357223U CN213583875U CN 213583875 U CN213583875 U CN 213583875U CN 202022357223 U CN202022357223 U CN 202022357223U CN 213583875 U CN213583875 U CN 213583875U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
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Abstract
The application discloses a water heat exchange membrane assembly, a water heat exchange device and a fuel cell system, wherein the water heat exchange membrane assembly comprises at least one water heat exchange membrane assembly unit, and the water heat exchange membrane assembly unit comprises a five-in-one membrane structure and a support framework which are stacked and formed in a composite mode; five unification diaphragm structures include from last down in proper order: the water-heat exchange membrane comprises a first hot melt adhesive layer, a first support net layer, a water-heat exchange membrane, a second support net layer and a second hot melt adhesive layer, wherein the first support net layer, the second support net layer, the water-heat exchange membrane, the second support net layer and the second hot melt adhesive layer are bonded together through the first hot melt adhesive layer and the second hot melt adhesive layer, the water-heat exchange membrane is a water-permeable and air-impermeable flexible porous material, and all water-heat exchange membrane components are stacked in pairs and then placed in an oven to complete the forming and sealing of a water-heat exchange device main body at one time.
Description
Technical Field
The present application relates to the field of fuel cells, and more particularly, to a water heat exchange device for a fuel cell.
Background
Fuel cells are clean, efficient, and long-lived power generation devices. Compared with the conventional power generation technology, the fuel cell has great advantages in the aspects of efficiency, safety, reliability, flexibility, cleanness, operation performance and the like, and has very wide application prospect.
Many fuel cells use internal membranes, such as PEM-type fuel cells that include proton exchange membranes (also known as polymer electrolyte membranes). In order to operate in a higher efficiency range, it is desirable to keep the membrane in a wet condition. Maintaining the humidity of the membrane helps to avoid damage or reduced life of the membrane, as well as maintain the desired operating efficiency. The lower water content of the membrane results in higher proton conduction resistance and thus higher ohmic voltage loss. Humidification of the inlet air (especially at the cathode inlet) is beneficial to maintain sufficient moisture content in the membrane.
The prior art water heat exchange device for fuel cells has a complex structure, and needs to adopt fasteners and sealing members, which on one hand causes cost increase, and on the other hand, the fasteners and the sealing members are easy to cause defects, and the service life is shortened.
Therefore, there is an urgent need in the art to develop a water heat exchange device for a fuel cell having a simple structure and a long service life.
Disclosure of Invention
The purpose of the present application is to provide a water heat exchange device for a fuel cell, which has a simple structure and a long service life.
The application provides a water heat exchange membrane assembly of a water heat exchange device for a fuel cell, which comprises at least one water heat exchange membrane assembly unit, wherein the water heat exchange membrane assembly unit comprises a five-in-one membrane structure and a support framework which are stacked and formed in a composite mode; five unification diaphragm structures include from last down in proper order: the water-heat exchange membrane comprises a first hot melt adhesive layer, a first supporting net layer, a water-heat exchange membrane, a second supporting net layer and a second hot melt adhesive layer, wherein the first supporting net layer, the second supporting net layer and the water-heat exchange membrane are bonded together through the first hot melt adhesive layer and the second hot melt adhesive layer, and the water-heat exchange membrane is a water-permeable and air-impermeable flexible porous material.
In another preferred embodiment, the five-in-one membrane structure and the supporting framework are alternately stacked.
In another preferred embodiment, the hydrothermal exchange membrane assembly comprises a five-in-one membrane structure and a supporting framework which are stacked together.
In another preferred example, the hydrothermal exchange membrane assembly comprises two five-in-one membrane structures stacked together, and a supporting framework located in the two five-in-one membrane structures.
In another preferred embodiment, a gas flow channel is arranged between two five-in-one membrane structures separated by the supporting framework.
In another preferred embodiment, the gas flow channel is an exhaust gas channel or an intake gas channel.
In another preferred embodiment, the adjacent exhaust and intake runners are opposite to each other.
In another preferred example, exhaust gas and intake gas respectively flow through both sides (i.e., both main surface sides) of the hydrothermal exchange membrane.
In another preferred example, the hydrothermal exchange membrane assembly comprises 2N +1 five-in-one membrane structures and 2N supporting frameworks which are alternately stacked, wherein N is a positive integer larger than or equal to 1.
In another preferred example, the hydrothermal exchange membrane assembly comprises 2N five-in-one membrane structures and 2N +1 supporting frameworks which are alternately stacked, wherein N is a positive integer larger than or equal to 1.
In another preferred example, a resin is filled in the surface or the gap of the hydrothermal exchange membrane.
In another preferred embodiment, the resin includes, but is not limited to, a sulfonic acid resin, or a perfluorosulfonic acid resin.
In another preferred example, the hydrothermal exchange membrane assembly is of a plate type structure.
In another preferred example, the thickness of the five-in-one membrane structure is 0.4mm-0.6 mm.
In another preferred example, the five-in-one film structure further comprises a sealing frame formed by the first and/or second hot melt adhesive layers.
In another preferred example, the area ratio of the first or second hot melt adhesive layer, the first or second support net layer and the hydrothermal exchange membrane is (0.1-0.3): 1.0: (0.6-0.9).
In another preferred example, the first hot melt adhesive layer and the second hot melt adhesive layer are arranged on the periphery of the supporting net layer.
In another preferred embodiment, the first and second layers of hot melt adhesive are identical.
In another preferred embodiment, the hydrothermal exchange membrane is selected from the group consisting of: expanded polytetrafluoroethylene film and ultrahigh molecular weight polyethylene film.
In another preferred embodiment, the meshes of the first and/or second supporting net layer are between 5 meshes and 500 meshes.
In another preferred embodiment, the first supporting web layer and the second supporting web layer are the same.
In another preferred embodiment, said first and/or second supporting web layer is in the form of a woven or biaxially oriented web.
In another preferred embodiment, the material of the first and/or second supporting net layer is selected from the following group: nylon, PVC and PET.
In another preferred example, the supporting framework is a rectangular crisscross framework structure.
In another preferred embodiment, the supporting framework is made of plastic and is formed by injection molding.
In another preferred example, support points are arranged on the criss-cross points of the support framework, and the distance between every two adjacent support points is 5-20 mm.
In another preferred embodiment, the thickness of the support skeleton is 1-3mm, preferably 2 mm.
In another preferred embodiment, the support framework is provided with an inlet structure and an outlet structure for gas to enter and exit, the inlet structure and the outlet structure are arranged at the opposite corners of the support framework, and the inlet structure and the outlet structure are matched with the adjacent five-in-one membrane structure to form an inlet or an outlet of a gas flow channel.
The present application further provides a water heat exchange device for a fuel cell, the water heat exchange device comprising one or more water heat exchange membrane assemblies as described in any one of the above.
In another preferred example, two adjacent supporting skeletons of the hydrothermal exchange membrane assembly unit are stacked in opposite directions, so that the adjacent gas flow channels are two independent gas flow channels which are crossed.
In another preferred example, the water heat exchange device comprises 20-200 five-in-one membrane structures.
In another preferred embodiment, the height of the water heat exchange device is 10-100cm, preferably 20-50 cm.
The application also provides a fuel cell system, which comprises a fuel cell unit and the water heat exchange device for the fuel cell, which is connected with the fuel cell unit.
The application also provides a preparation method of the hydrothermal exchange membrane assembly, which comprises the following steps:
(a) providing a stacking structure, wherein the stacking structure comprises a plurality of stacking structure units, and each stacking structure unit comprises a five-in-one membrane structure and a supporting framework which are stacked together; five unification diaphragm structures include from last down in proper order: the water-heat exchange membrane comprises a first hot melt adhesive layer, a first support net layer, a water-heat exchange membrane, a second support net layer and a second hot melt adhesive layer, wherein the first and second support net layers and the water-heat exchange membrane are bonded together through the first and second hot melt adhesive layers, and the water-heat exchange membrane is a water-permeable and air-impermeable flexible porous material;
(b) heating the stacked structure to melt the hot melt adhesive in the stacked structure; and
(c) and cooling the stacked structure so as to solidify the molten hot melt adhesive, thereby forming the hydrothermal exchange membrane assembly.
In another preferred embodiment, in step (b), heating is carried out to a temperature T1, where T1 is the melting point of the hot melt adhesive ± 10 ℃, preferably T1 is the melting point of the hot melt adhesive.
In another preferred example, in the step (b), the method comprises the steps of: clamping the stacked structure and then heating the clamped stacked structure.
In another preferred embodiment, the support frames of two adjacent stacked structural units are stacked in opposite directions, so that the gas flow channels of two adjacent support frames are two independent gas flow channels which intersect.
In another preferred example, in step (c), the temperature is reduced to room temperature.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below. It is understood that the drawings in the following description are merely exemplary of the invention, and that those skilled in the art will be able to derive other embodiments without the exercise of inventive faculty.
FIG. 1 is a top view of a five-in-one diaphragm structure according to the present application;
FIG. 2 is a top view of a support armature according to the present application;
fig. 3 is a cross-sectional view of a water heat exchange device for a fuel cell according to the present application;
FIG. 4 is a cross-sectional view of a five-in-one diaphragm structure according to the present application;
FIG. 5 is a top view of a support web layer of a five-in-one membrane structure according to the present application.
In the drawings, the designations are as follows:
1-Water heat exchange Membrane Module Unit
10-five-in-one diaphragm structure
11-water heat exchange membrane
121-first supporting web layer
122-second supporting network layer
13-Hot melt adhesive layer
131-first hot melt adhesive layer
132-second hotmelt adhesive layer
14-sealing frame
20-support framework
21-support point
22-inlet structure
23-outlet structure
Detailed Description
The present inventors have conducted extensive and intensive studies and, for the first time, have developed a water heat exchange device for a fuel cell having a novel structure, which is simple in structure and directly replaces a thin plate with a hot melt adhesive without using the thin plate, wherein a water-permeable film is wrapped in the middle by two layers of hot melt adhesive films. When the hot melt adhesive is prepared, the hot melt adhesive pieces in two groups of different directions are stacked together, and then the hot melt adhesive pieces are baked, so that the whole fusion can be realized, the water-permeable film and the hot melt adhesive form an integral structure, the structure is firmer, and the water heat exchange efficiency is higher. In addition, the utility model is used for fuel cell's water heat exchange device can keep the fuel cell membrane at humid situation, long service life moreover high-efficiently at the during operation.
The main advantages of the utility model
(a) The hydrothermal exchange device of this application is with all five unification membrane structures and support skeleton lamination back, has realized connecting and sealing through the hot melt adhesive, does not use fastener and sealing member.
(b) The fine net in the water heat exchange device and the supporting points in the framework form good support for the water heat exchange membrane, and can bear the pressure difference within 2 bar.
(c) The water heat exchange device is simple in structure, high in space utilization rate, low in manufacturing cost and suitable for batch production.
In the following description, numerous technical details are set forth in order to provide a better understanding of the present application. However, it will be understood by those skilled in the art that the technical solutions claimed in the present application may be implemented without these technical details and with various changes and modifications based on the following embodiments.
Term(s) for
The terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus. Without further limitation, the use of the verb "comprise a" to define an element does not exclude the presence of another, same element in a process, method, article, or apparatus that comprises the element. In the present patent application, if it is mentioned that a certain action is executed according to a certain element, it means that the action is executed according to at least the element, and two cases are included: performing the action based only on the element, and performing the action based on the element and other elements. The expression of a plurality of, a plurality of and the like includes 2, 2 and more than 2, more than 2 and more than 2.
In the present invention, all the directional indicators (such as up, down, left, right, front, rear, etc.) are only used to explain the relative position relationship between the components, the motion situation, etc. in a specific posture (as shown in the drawings), and if the specific posture is changed, the directional indicator is changed accordingly.
The structure of the five-in-one membrane:
the utility model discloses a five unification diaphragm structures include from last to down in proper order: the first hot melt adhesive layer, the first supporting net layer, the hydrothermal exchange membrane, the second hot melt adhesive layer and the second supporting net layer are bonded together through the hot melt adhesive layers. That is, the middle layer is a water-heat exchange membrane, and the two surfaces closely attached to the middle layer water-heat exchange membrane are support nets. Preferably, the area ratio of the hot melt adhesive layer, the support net layer and the hydrothermal exchange membrane is (0.1-0.3): 1.0: (0.6-0.9) because the shape of the humidifier varies from one specification to another. Preferably, the hot melt adhesive layer is arranged around the support net layer.
The five-in-one membrane structure is not only provided with five layers, but is a five-layer structure after hot-pressing compounding. The five-in-one membrane structure can sequentially comprise a first hot melt adhesive layer, a first supporting net layer, a second hot melt adhesive layer hydrothermal exchange membrane, a third hot melt adhesive layer, a second supporting net layer and a fourth hot melt adhesive layer from top to bottom.
The hydrothermal exchange membrane is a flexible porous material, including but not limited to an expanded polytetrafluoroethylene film, an ultra-high molecular polyethylene film and the like, the surface or pores of the membrane are filled with resin, and the resin includes but not limited to perfluorosulfonic acid resin, so that the membrane has the functions of water permeation and air impermeability.
Preferably, the first and/or second support web layers are identical; the mesh of the first and/or second support mesh layer is from 5 mesh to 500 mesh, preferably 15 mesh to 50 mesh, in the form of a woven or biaxially oriented mesh, including but not limited to nylon, PVC, PET, etc.
The five-in-one membrane structure is combined together by hot melt adhesive, and the hot melt adhesive not only bonds the water heat exchange membrane and the support net together, but also forms a frame with certain thickness. The thickness of the five-in-one film structure is in the range of 0.4mm-0.6 mm.
Supporting the framework:
the supporting framework is made of plastic and formed by injection molding, the thickness of the supporting framework is 1-3mm, the optimal thickness is 2mm, the middle of the supporting framework is provided with reticular supporting points, and the distance between the supporting points is 5-20 mm. The support framework is provided with an inlet structure and an outlet structure for gas to enter and exit, the inlet structure and the outlet structure are arranged at the opposite corners of the support framework, and the inlet structure and the outlet structure are matched with an adjacent five-in-one membrane structure to form an inlet or an outlet of a gas flow channel.
Water heat exchange membrane assembly of water heat exchange device for fuel cell
The water heat exchange membrane component comprises at least one water heat exchange component unit, and the water heat exchange component unit comprises a five-in-one membrane structure and a supporting framework which are stacked and formed in a composite mode. Wherein, five-in-one membrane structure and support skeleton stack in turn, be equipped with gas flow path between two five-in-one membrane structures that a support skeleton separates. The gas flow passage is an exhaust gas flow passage or an intake gas flow passage.
The hydrothermal exchange membrane assembly may include a five-in-one membrane structure and a support frame stacked together. The hydrothermal exchange membrane assembly can comprise two five-in-one membrane structures which are stacked together and a supporting framework positioned on the two five-in-one membrane structures. Preferably, the hydrothermal exchange membrane assembly is of a plate type structure.
Preferably, the hydrothermal exchange membrane assembly can comprise 2N +1 five-in-one membrane structures and 2N supporting frameworks which are alternately stacked, wherein N is a positive integer larger than or equal to 1.
Preferably, the hydrothermal exchange membrane assembly can comprise 2N five-in-one membrane structures and 2N +1 supporting frameworks which are alternately stacked, wherein N is a positive integer larger than or equal to 1.
Water heat exchange device for fuel cell
The water heat exchange device comprises a plurality of water heat exchange membrane assemblies which are stacked together, wherein the support frameworks of two adjacent water heat exchange membrane assembly units are stacked along opposite directions, so that the gas flow channels of the two adjacent support frameworks are two crossed independent gas flow channels.
Preferably, the hydrothermal exchange device comprises 20-200 hydrothermal exchange membrane assembly units.
Preferably, the height of the hydrothermal exchange device is 20cm-50 cm.
Fuel cell system
The fuel cell system of the present application includes a fuel cell unit, and the above-described water heat exchange device for a fuel cell connected to the fuel cell unit.
The preparation method of the hydrothermal exchange membrane component comprises the following steps:
(a) providing a stacking structure, wherein the stacking structure comprises a plurality of stacking structure units, and each stacking structure unit comprises a five-in-one membrane structure and a supporting framework which are stacked together; five unification diaphragm structures include from last down in proper order: the water-heat exchange membrane comprises a first hot melt adhesive layer, a first support net layer, a water-heat exchange membrane, a second support net layer and a second hot melt adhesive layer, wherein the first and second support net layers and the water-heat exchange membrane are bonded together through the first and second hot melt adhesive layers, and the water-heat exchange membrane is a water-permeable and air-impermeable flexible porous material;
(b) heating the stacked structure to melt the hot melt adhesive in the stacked structure; and
(c) and cooling the stacked structure so as to solidify the molten hot melt adhesive, thereby forming the hydrothermal exchange membrane assembly.
Preferably, in step (b), heating is carried out to a temperature T1, said T1 being the melting point of the hot melt adhesive ± 10 ℃, preferably T1 being the melting point of the hot melt adhesive.
Preferably, in the step (b), the method comprises the steps of: clamping the stacked structure and then heating the clamped stacked structure.
Preferably, the support frameworks of two adjacent stacked structural units are stacked in opposite directions, so that the gas flow channels of two adjacent support frameworks are two independent gas flow channels which intersect.
Preferably, in step (c), the temperature is reduced to room temperature.
Example 1
Referring to fig. 1 to 5, the present invention provides a water heat exchange device for a fuel cell, the water heat exchange device comprises a plurality of water heat exchange membrane assemblies, each water heat exchange membrane assembly comprises a plurality of water heat exchange membrane assembly units 1, and preferably, the water heat exchange membrane assemblies are of a plate structure;
the hydrothermal exchange membrane component unit 1 comprises 3 five-in-one membrane structures 10 and 2 supporting frameworks 20 which are stacked together, wherein the five-in-one membrane structures 10 and the supporting frameworks 20 are stacked alternately. Wherein, a gas flow channel is arranged between two five-in-one membrane structures separated by a supporting framework. Specifically, the support frame 20 is provided with an inlet structure 22 and an outlet structure 23 for gas to enter and exit, the inlet structure 22 and the outlet structure 23 are arranged at the diagonal of the support frame 20, and the inlet structure 22 and the outlet structure 23 are matched with the adjacent five-in-one membrane structure to form an inlet or an outlet of a gas flow channel. Wherein, the gas flow channel is an exhaust flow channel or an intake flow channel. The adjacent exhaust and intake runners are opposite to each other. That is, two adjacent supporting skeletons of the hydrothermal exchange membrane module unit 1 are stacked in opposite directions so that the adjacent gas flow paths are two independent gas flow paths which intersect.
This five unification diaphragm structures 10 includes from last down in proper order: the membrane comprises a first hot melt adhesive layer 131, a first support net layer 121, a hydrothermal exchange membrane 11, a second support net layer 122 and a second hot melt adhesive layer 132, wherein the first and/or second support net layer and the hydrothermal exchange membrane are bonded together through the first and/or second hot melt adhesive layer, and the hydrothermal exchange membrane 11 is a water-permeable and air-impermeable flexible porous material, including but not limited to an expanded polytetrafluoroethylene film or an ultra-high molecular polyethylene film; in other implementations, this five-in-one diaphragm structure 1 includes first hot melt adhesive layer, first support stratum reticulare, second hot melt adhesive layer hydrothermal exchange membrane, third hot melt adhesive layer, second support stratum reticulare, fourth hot melt adhesive layer from last to down in proper order also saying, the utility model discloses a five-in-one diaphragm structure is not only five layers, but is five layers of structures after the hot pressing is compound.
Wherein the first hot melt adhesive layer 131 and the second hot melt adhesive layer 132 are the same, the first support web layer 121 and the second support web layer 122 are the same, and the area ratio of the first and/or second hot melt adhesive layer, the first and/or second support web layer and the hydrothermal exchange membrane is (0.1-0.3): 1.0: (0.6-0.9), the hydrothermal exchange membrane may have different sizes because the humidifier may have different shapes with different specifications. The hot melt adhesive layer 13 not only bonds the support mesh layer and the hydrothermal exchange membrane 11 together, but also forms a sealing frame 14 with a certain thickness at the periphery of the support mesh layer.
Exhaust gas and intake gas flow through both sides (i.e., both main surface sides) of the water heat exchange membrane, respectively. The surface or the gap of the hydrothermal exchange membrane 11 is filled with resin, including but not limited to perfluorosulfonic acid resin. The supporting net layer (the first supporting net layer 121 and/or the second supporting net layer 122) is in the form of a woven net or a bidirectional stretching net, the meshes of the supporting net layer (the first supporting net layer 121 and/or the second supporting net layer 122) are between 5 meshes and 500 meshes, and the material of the first and/or the second supporting net layer can be nylon, PVC or PET.
In this embodiment, the supporting frame 20 is a rectangular criss-cross frame structure, the supporting frame is made of plastic, and is formed by injection molding, supporting points 21 are arranged at criss-cross points of the supporting frame 20, preferably, the distance between adjacent supporting points 21 is 5-20mm, and the thickness of the supporting frame 20 is 1-3 mm.
The method for preparing the water heat exchange device for the fuel cell is specifically as follows, stacking 2N +1 five-in-one membrane structures 10 and 2N support skeletons 20(N is a natural number, and the size of N is selected according to requirements), wherein two adjacent support skeletons 20 are stacked in opposite directions, so that the gas flow channels of the two adjacent support skeletons are two crossed independent gas flow channels. That is, after the two sides of the supporting framework 20 are combined with the five-in-one membrane structure 10, a closed channel is formed inside the supporting framework 20; then, the other supporting framework 20 is reversely superposed and is compounded with a five-in-one membrane structure 10, so that two crossed independent flow channels are formed, namely, the supporting frameworks 20 of odd number pieces are placed in the same direction, but the supporting frameworks 20 of even number pieces are placed in an inverted manner (in the opposite direction) relative to the supporting frameworks 20 of the adjacent odd number pieces; the front and the back are superposed, so that two gas channel groups which are alternated layer by layer are formed. And then clamping the plurality of stacked water heat exchange membrane assemblies by using a clamping tool, then putting the assemblies into an oven to be heated to the melting point of the hot melt adhesive, and finally cooling to room temperature, thereby forming the water heat exchange device for the fuel cell.
All documents mentioned in this application are to be considered as being incorporated in their entirety into the disclosure of this application so as to be subject to modification as necessary. Further, it is understood that various changes or modifications may be made to the present application by those skilled in the art after reading the above disclosure of the present application, and such equivalents are also within the scope of the present application as claimed.
Claims (10)
1. A hydrothermal exchange membrane component of a hydrothermal exchange device for a fuel cell is characterized by comprising at least one hydrothermal exchange membrane component unit, wherein the hydrothermal exchange membrane component unit comprises a five-in-one membrane structure and a support framework which are stacked and formed in a composite mode; five unification diaphragm structures include from last down in proper order: the water-heat exchange membrane comprises a first hot melt adhesive layer, a first supporting net layer, a water-heat exchange membrane, a second supporting net layer and a second hot melt adhesive layer, wherein the first supporting net layer, the second supporting net layer and the water-heat exchange membrane are bonded together through the first hot melt adhesive layer and the second hot melt adhesive layer, and the water-heat exchange membrane is a water-permeable and air-impermeable flexible porous material.
2. The hydrothermal exchange membrane module of claim 1 wherein a gas flow path is provided between two pentahapto membrane structures separated by a support framework.
3. The membrane assembly of claim 1, wherein the membrane assembly comprises 2N +1 membrane structures and 2N supporting frames stacked alternately, wherein N is a positive integer greater than or equal to 1.
4. The hydrothermal exchange membrane assembly of claim 1, wherein said five-in-one membrane structure further comprises a sealed border formed by said first and/or second hot melt adhesive layers.
5. The hydrothermal exchange membrane assembly of claim 1, wherein the ratio of the area of the first or second hot melt adhesive layer, the first or second support mesh layer and the hydrothermal exchange membrane is (0.1-0.3): 1.0: (0.6-0.9).
6. The hydrothermal exchange membrane assembly of claim 1, wherein the five-in-one membrane structure has a thickness of 0.4mm to 0.6 mm.
7. The hydrothermal exchange membrane assembly of claim 1, wherein the support frame is provided with an inlet structure and an outlet structure for gas to enter and exit, the inlet structure and the outlet structure are arranged at opposite corners of the support frame, and the inlet structure and the outlet structure cooperate with the adjacent five-in-one membrane structure to form an inlet or an outlet of the gas flow channel.
8. The hydrothermal exchange membrane assembly of claim 1, wherein the mesh openings of the first and/or second support mesh layers are between 5 mesh and 500 mesh.
9. A water heat exchange device for a fuel cell, wherein the water heat exchange device comprises one or more water heat exchange membrane assemblies according to any one of claims 1 to 8.
10. A fuel cell system characterized by comprising a fuel cell unit, and the water heat exchange device for a fuel cell according to claim 9 connected to the fuel cell unit.
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| Application Number | Priority Date | Filing Date | Title |
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| CN202022357223.7U CN213583875U (en) | 2020-10-21 | 2020-10-21 | Water heat exchange membrane assembly, water heat exchange device, and fuel cell system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN202022357223.7U CN213583875U (en) | 2020-10-21 | 2020-10-21 | Water heat exchange membrane assembly, water heat exchange device, and fuel cell system |
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| CN213583875U true CN213583875U (en) | 2021-06-29 |
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