High-efficiency methanol reforming hydrogen production power system and method
By using gas treatment systems with components such as cooling blowers and calcium chloride columns in the high-efficiency methanol reforming hydrogen production power system, the problem of gas exchange cooling cannot effectively remove gaseous water, and efficient cooling and low humidity system operation is achieved.
Patent Information
- Application Number
- CN202510611672.4
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2025-05-13
- Publication Date
- 2025-08-15
- Estimated Expiration
- Not applicable · inactive patent
AI Technical Summary
In the existing high-efficiency methanol reforming hydrogen production power system, the gas exchange cooling method cannot effectively remove gaseous water, resulting in excessive humidity in the shell and insufficient cooling efficiency.
A gas treatment system consisting of components such as cooling blowers, calcium chloride columns and directing sheets is used to ensure low gas humidity and efficient cooling through low-temperature gas exchange and screening of calcium chloride columns.
It realizes efficient removal of gaseous water, reduces system humidity, prevents mechanism failure, and ensures long-term and stable operation of the system.
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Figure CN120479325A_ABST
Abstract
Description
Technical Field
[0001] The present invention belongs to the technical field of hydrogen production power, and in particular relates to a high-efficiency methanol reforming hydrogen production power system and method. Background Art
[0002] With the increasing global emphasis on environmental protection and sustainable development, the search for clean and efficient energy alternatives has become an urgent need. Hydrogen, as a clean and efficient renewable energy source, is considered an ideal alternative to fossil fuels due to its pollution-free nature and high energy density. Against the backdrop of the "carbon peak and carbon neutrality" goals, the development of hydrogen energy has garnered widespread attention and support.
[0003] In terms of application, high-efficiency methanol reforming hydrogen production power systems have been widely used in mobile hydrogen production, energy supply, transportation, military and other fields. Especially with the application and promotion of hydrogen fuel cells, stable and reliable hydrogen sources have gradually become a key issue in hydrogen energy applications. High-efficiency methanol reforming hydrogen production power systems can provide fuel cells with a safe and stable hydrogen source, opening up the entire hydrogen energy industry chain.
[0004] During hydrogen production, the purity of the hydrogen must be ensured before it is introduced into the fuel cell, which necessitates the use of a hydrogen purification device. During operation, cooling is generally achieved through gas exchange, but this operation fails to remove gaseous water, resulting in high humidity in the shell over a long period of time. High humidity in the introduced gas will only worsen the situation, and conventional gas introduction methods are not efficient enough for cooling. Therefore, a high-efficiency methanol reforming hydrogen production power system and method are proposed. Summary of the Invention
[0005] The present invention provides a high-efficiency methanol reforming hydrogen production power system and method, which aims to solve the problem that during operation, cooling is generally achieved through gas exchange. Such operation cannot remove gaseous water, resulting in high humidity in the shell for a long time. If the humidity of the introduced gas is high, the situation will be made worse. In addition, the general gas introduction method is not efficient enough for cooling.
[0006] An embodiment of the present invention provides a high-efficiency methanol reforming hydrogen production power system, comprising a plurality of hydrogen storage tanks, the hydrogen storage tanks being connected to the input end of a methanol reforming reactor via a pipeline, the output end of the methanol reforming reactor being connected to the input end of a hydrogen purification device via a pipeline, the output end of the hydrogen purification device being connected to a fuel cell, an outer shell being arranged on the outside of the hydrogen purification device, the outer shell being located above a support platform and being fixedly connected to the support platform, a side wall of the outer shell being fixedly connected to a gas processing shell near the upper area, one end of the gas processing shell being connected to the inside of the outer shell. The reverse corner areas of the upper wall of the outer shell are fixedly connected to several cooling blowers at the same distance, the inner wall of the outer shell at the tail of the cooling blower is vertically fixedly connected to a cooling assembly piece, the front and reverse wall areas of the tail inside the outer shell are respectively fixedly connected to a receiving shell, and a shielding piece is fixedly connected to the inner side of the outer shell between the two receiving shells on the front and back sides, the cooling assembly piece includes a pointing piece, and a vertically installed pointing piece is fixed on the cooling assembly piece, the front end of the pointing piece is placed inside the outer shell, and the reverse end of the pointing piece is in contact with the reverse side of the outer shell.
[0007] Furthermore, the supporting platform includes a liquid storage shell and a discharge channel. The square liquid storage shell is fixedly connected to the upper wall of the supporting platform. The tail area of the right wall of the liquid storage shell is fixedly connected to the discharge channel connected to the outside at a 90-degree angle. The lower wall inside the liquid storage shell is installed in a slope.
[0008] Furthermore, the outer shell includes an inlet hole, an air inlet hole, a storage chamber and a leakage hole. A square inlet hole is reserved in the area where the right wall of the outer shell and the gas processing shell are adapted to each other. A square air inlet hole is reserved in the area at the tail of the cooling assembly piece inside the outer shell. A storage chamber is reserved in the outer shell on the opposite side of the air inlet hole. Leakage holes that penetrate the liquid storage shell are reserved on both sides of the front wall of the storage chamber.
[0009] Furthermore, the gas processing shell includes calcium chloride columns, the front of the gas processing shell is slidably embedded with equidistantly installed calcium chloride columns at a 90-degree angle, the tail of the gas processing shell is open and installed crookedly.
[0010] Furthermore, the two pointing pieces form a pair, and the two pointing pieces in a pair are arranged in a mirror-image curved structure.
[0011] Furthermore, the two receiving shells on the front and back sides both have a triangular prism structure with an angle of ninety degrees, and the slopes of the two receiving shells are opposite to each other.
[0012] Furthermore, the shielding piece includes a supporting piece, which is in a curved structure protruding upward, and the protruding central area of the shielding piece is fixedly connected to the supporting piece at 90 degrees toward the tail, and the two sides of the supporting piece are fixedly connected to the two inner sides of the outer shell.
[0013] A high-efficiency methanol reforming hydrogen production method comprises the following steps:
[0014] S1: The methanol in the hydrogen storage tank is sent to the methanol reforming reactor through a pipeline for reforming reaction, and then sent to the hydrogen purification device through a pipeline for purification and then sent to the fuel cell for power generation.
[0015] S2: During normal operation of the hydrogen purification device, the surrounding low-temperature gas flows in from the inlet hole, moves toward the tail through the upper part of the outer shell, and carries the high-temperature gas inside out through the air inlet hole and out through the back of the cooling assembly plate toward the top. During the discharge, the reverse movement of gaseous water energy gathers in the holding chamber and is discharged from the leakage hole to the liquid storage shell for accumulation.
[0016] S3: The tail of the gas treatment shell is tilted to introduce low-temperature gas from the side of the gas treatment shell. The tilted introduction hole structure can reduce the introduction of pollutants. The calcium chloride column can be manually replaced to filter out gaseous water in the moving gas.
[0017] S4: The pointing piece allows the passing gas to touch and intersect back and forth, increasing the contact area and the effective period, thereby ensuring efficient cooling. The pointing piece at the end can process the introduced gas to filter out and allow floating objects and gaseous water to fall into the holding chamber for collection and treatment.
[0018] The beneficial effects of the present invention are:
[0019] 1. The present invention allows the surrounding low-temperature gas to flow in from the inlet hole, and move toward the tail through the upper inside of the outer shell, carrying the high-temperature gas inside from the air inlet hole through the back side of the cooling assembly piece to be discharged upward. The reverse movement of gaseous water energy generated during the discharge period is gathered in the receiving chamber, discharged from the leakage hole and accumulated in the liquid storage shell, preventing the operation of the cooling blower and ensuring high cooling efficiency.
[0020] 2. The present invention utilizes equidistantly arranged calcium chloride columns that are slidably embedded in the front of the gas treatment shell at a 90-degree angle. The tail of the gas treatment shell is open and tilted, allowing the introduction of low-temperature gas from the surrounding side of the gas treatment shell. The tilted introduction hole structure reduces the introduction of pollutants. The calcium chloride columns can be manually replaced to filter out gaseous water in the moving gas, ensuring low humidity and preventing malfunction of the internal mechanism.
[0021] 3. The directional blades of the present invention are arranged in a pair of two. The two directional blades in a pair are arranged in a mirror-image curved structure. The directional blades can allow the passing gas to touch and intersect back and forth, so that the touch area and the effective period are increased, thereby ensuring efficient cooling. The directional blades at the end can process the introduced gas and filter it, allowing floating objects and gaseous water to fall into the holding chamber for collection and treatment, ensuring the long-term use of each device.
[0022] Other features and advantages of the present invention will be described in the following description, and in part will become apparent from the description, or will be understood by practicing the present invention. The purpose and other advantages of the present invention can be realized and obtained through the structures particularly pointed out in the description and the drawings. BRIEF DESCRIPTION OF THE DRAWINGS
[0023] The accompanying drawings are used to provide a further understanding of the present invention and constitute a part of the specification. Together with the embodiments of the present invention, they are used to explain the present invention and do not constitute a limitation of the present invention. In the accompanying drawings:
[0024] Figure 1 Schematic diagram of the structure of an embodiment of the present invention;
[0025] Figure 2 This is a schematic diagram of the outer shell structure of an embodiment of the present invention;
[0026] Figure 3 This is a schematic diagram of the structure inside the outer shell of an embodiment of the present invention;
[0027] Figure 4 This is a schematic diagram of the reverse structure of the outer shell of an embodiment of the present invention;
[0028] Figure 5 This is a schematic diagram of the back structure of the outer shell of an embodiment of the present invention;
[0029] Figure 6 This is a schematic diagram showing the structure of the interior of an embodiment of the present invention;
[0030] Figure 7 Schematic diagram of the inner separation structure of an embodiment of the present invention;
[0031] Figure numerals: 11, hydrogen storage tank; 111, methanol reforming reactor; 113, fuel cell; 12, supporting platform; 1212, liquid storage shell; 1213, unloading channel; 13, outer shell; 1312, access hole; 1313, air inlet hole; 1314, accommodating chamber; 1315, leakage hole; 14, gas treatment shell; 1412, calcium chloride column; 15, cooling air blower; 16, cooling assembly plate; 1612, pointing plate; 17, receiving shell; 18, shielding plate; 1812, supporting plate. DETAILED DESCRIPTION
[0032] In order to make the purpose, technical solution and advantages of the technical solution of the present invention clearer, the technical solution of the embodiment of the present invention will be clearly and completely described below in conjunction with the drawings of specific embodiments of the present invention. The same figure marks in the drawings represent the same components. It should be noted that the described embodiments are part of the embodiments of the present invention, not all of the embodiments. Based on the described embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.
[0033] Reference Figure 1-7 The embodiment of the present invention provides an efficient methanol reforming hydrogen production power system, comprising a plurality of hydrogen storage tanks 11, the hydrogen storage tanks 11 are connected to the input end of a methanol reforming reactor 111 via a pipeline, the output end of the methanol reforming reactor 111 is connected to the input end of a hydrogen purification device via a pipeline, the output end of the hydrogen purification device is connected to a fuel cell 113, an outer shell 13 is arranged on the outside of the hydrogen purification device, the outer shell 13 is located on the support platform 12 and is fixedly connected to the support platform 12, a side wall of the outer shell 13 is fixedly connected to a gas processing shell 14 near the upper area, and one end of the gas processing shell 14 and the inner side of the outer shell 13 are mutually connected. The outer shell 13 is connected to the outer wall of the outer shell 13. The corner areas on the reverse side are fixedly connected with several cooling fans 15 at the same distance. The cooling assembly piece 16 is vertically fixedly connected to the inner wall of the outer shell 13 at the tail of the cooling fan 15. The front and reverse wall areas on the tail of the inner shell 13 are respectively fixedly connected to the receiving shell 17. The inner shell 13 is fixedly connected with a shielding piece 18 between the two receiving shells 17 on the front and reverse sides. Methanol and water are mixed and sent to the methanol reforming reactor 111 for reforming reaction. After purification by the hydrogen purification device, it is sent to the fuel cell 113 for power generation. Holes for pipelines to pass through can be reserved on the outer shell 13.
[0034] The supporting platform 12 includes a liquid storage shell 1212 and a discharge channel 1213. The square liquid storage shell 1212 is fixedly connected to the upper wall of the supporting platform 12. The tail area of the right wall of the liquid storage shell 1212 is fixedly connected to the discharge channel 1213 connected to the outside at a ninety-degree angle. The lower wall inside the liquid storage shell 1212 is installed in a slope, and the liquid formed by condensation when it is cold in the outer shell 13 can be gathered through the liquid storage shell 1212. The lower wall installed in a slope can actively discharge the liquid formed by condensation when it is cold to the outside to prevent the humidity inside the outer shell 13 from being too high.
[0035] The outer shell 13 includes an inlet hole 1312, an air inlet hole 1313, a receiving chamber 1314 and a leakage hole 1315. A square inlet hole 1312 is reserved on the right wall of the outer shell 13 and the area adapted to the gas processing shell 14. A square inlet hole 1313 is reserved in the area at the tail of the cooling assembly piece 16 inside the outer shell 13. A receiving chamber 1314 is reserved in the outer shell 13 on the opposite side of the air inlet hole 1313. The front wall of the receiving chamber 1314 is reserved on both sides for the liquid storage shell 12. Through the leakage hole 1315 inside the housing 12, the surrounding low-temperature gas flows in from the inlet hole 1312, moves toward the tail through the upper part of the inner side of the outer shell 13, and carries the high-temperature gas inside from the air inlet hole 1313 to pass through the reverse side of the cooling assembly piece 16 and discharge upward. The reverse-moving gaseous water energy generated during the discharge is gathered in the receiving chamber 1314 and discharged from the leakage hole 1315 to the liquid storage shell 1212 for accumulation, thereby preventing the cooling blower 15 from malfunctioning and ensuring efficient cooling.
[0036] The gas processing shell 14 includes calcium chloride columns 1412. The front of the gas processing shell 14 is slidably embedded with equidistantly installed calcium chloride columns 1412 at a 90-degree angle. The rear of the gas processing shell 14 is open and tilted to introduce low-temperature gas from the surrounding side of the gas processing shell 14. The tilted introduction hole structure can reduce the introduction of pollutants. The calcium chloride columns 1412 can be manually replaced to filter out gaseous water in the moving gas, ensure low humidity of the gas, and prevent malfunction of the internal mechanism.
[0037] The cooling assembly piece 16 includes a pointing piece 1612, and the cooling assembly piece 16 is fixedly connected to the vertically installed pointing piece 1612. The front end of the pointing piece 1612 is placed inside the outer shell 13, and the back end of the pointing piece 1612 is in contact with the back side of the outer shell 13. The pointing pieces 1612 are in a pair, and the two pointing pieces 1612 in a pair are in a curved structure that is mirror-mounted. The pointing pieces 1612 can allow the passing gas to touch and intersect back and forth, thereby increasing the touch area and the effective period, thereby ensuring high efficiency of cooling, and the pointing piece 1612 at the end can process the introduced gas to filter out, allowing floating objects and gaseous water to fall into the holding chamber 1314 for collection and treatment, thereby ensuring the long-term use of each component.
[0038] The two receiving shells 17 on the front and back sides both have a triangular prism structure with a ninety-degree angle. The slopes of the two receiving shells 17 are opposite to each other, which can ensure that floating objects and gaseous water fall into the liquid storage shell 1212 and gather.
[0039] The shielding piece 18 includes a supporting piece 1812. The shielding piece 18 has a curved structure that protrudes upward. The protruding central area of the shielding piece 18 is fixed to the supporting piece 1812 at a 90-degree angle toward the tail. The two sides of the supporting piece 1812 are fixed to the two sides inside the outer shell 13, which can prevent the floating objects and gaseous water contained therein from moving upward, ensuring that the humidity of the operating conditions of various components in the outer shell 13 is low.
[0040] During operation, the surrounding low-temperature gas flows in from the inlet hole 1312, moves toward the tail through the upper inside of the outer shell 13, and carries the high-temperature gas inside from the air inlet hole 1313 through the back of the cooling assembly piece 16 to be discharged upward. The reverse-moving gaseous water energy generated during the discharge process will gather in the receiving chamber 1314, and be discharged from the leakage hole 1315 to the liquid storage shell 1212 to accumulate together, preventing the operation of the cooling blower 15 from being affected, ensuring efficient cooling. The tail of the gas processing shell 14 is installed at an angle, which can introduce low-temperature gas from the side of the gas processing shell 14. The tilted introduction hole structure can reduce the introduction of pollutants. The calcium chloride column 1412 can be replaced manually to filter out the gaseous water in the moving gas, ensure low humidity of the gas, and prevent malfunction of the internal mechanism. The pointing pieces 1612 are in a pair of two, and the two pointing pieces 1612 in a pair are in a curved structure installed in a mirror image. The pointing piece 161 2 It allows the passing gas to touch and intersect back and forth, so that the touch area and the effective period are increased, thereby ensuring efficient cooling, and the pointing piece 1612 at the end can handle the introduced gas screening, allowing floating objects and gaseous water to fall into the storage chamber 1314 for collection and treatment, ensuring the long-term use of various components, the lower wall inside the liquid storage shell 1212 is installed in a slope, which can collect the liquid formed by condensation when it is cold in the outer shell 13 through the liquid storage shell 1212, and the lower wall installed in a slope can actively discharge the liquid formed by condensation when it is cold to the outside, preventing the humidity in the outer shell 13 from being too high, the shielding piece 18 is a curved structure protruding upward, and the protruding central area of the shielding piece 18 is fixedly connected to the supporting piece 1812 at 90 degrees toward the tail, and the two sides of the supporting piece 1812 are fixedly connected to the two sides inside the outer shell 13, which can prevent the contained floating objects and gaseous water from moving upward, ensuring that the humidity of the operating conditions of various components in the outer shell 13 is low.
[0041] A high-efficiency methanol reforming hydrogen production method comprises the following steps:
[0042] S1: The methanol in the hydrogen storage tank 11 is sent to the methanol reforming reactor 111 through a pipeline for reforming reaction, and then sent to the hydrogen purification device through a pipeline for purification and then sent to the fuel cell 113 for power generation.
[0043] S2: During normal operation of the hydrogen purification device, low-temperature ambient gas flows in through the inlet hole 1312, moves toward the rear through the upper inside of the outer shell 13, and carries the high-temperature gas inside out through the air inlet hole 1313, through the back side of the cooling assembly plate 16, and is discharged upward. During the discharge, the reverse movement of gaseous water energy gathers in the receiving chamber 1314, is discharged through the leakage hole 1315, and is accumulated in the liquid storage shell 1212.
[0044] S3: The tail of the gas processing shell 14 is tilted to introduce low-temperature gas from the side of the gas processing shell 14. The tilted introduction hole structure can reduce the introduction of pollutants. The calcium chloride column 1412 can be manually replaced to filter out gaseous water in the moving gas.
[0045] S4: The pointing piece 1612 allows the passing gas to touch and intersect back and forth, thereby increasing the touching area and the effective period, thereby ensuring efficient cooling. The pointing piece 1612 at the end can process the introduced gas to filter out and allow floating objects and gaseous water to fall into the receiving chamber 1314 for collection and treatment.
[0046] The basic principles, main features, and advantages of the present invention are shown and described above. Those skilled in the art should understand that the present invention is not limited to the above embodiments. The above embodiments and descriptions are merely illustrative of the principles of the present invention. Various changes and modifications may be made to the present invention without departing from the spirit and scope of the present invention. Such changes and modifications are intended to fall within the scope of the present invention. The scope of protection claimed in the present invention is defined by the appended claims and their equivalents.
Claims
1. A high-efficiency methanol reforming hydrogen production power system, comprising a plurality of hydrogen storage tanks (11), characterized in that: The hydrogen storage tank (11) is connected to the input end of the methanol reforming reactor (111) via a pipeline, the output end of the methanol reforming reactor (111) is connected to the input end of the hydrogen purification device via a pipeline, the output end of the hydrogen purification device is connected to the fuel cell (113), an outer shell (13) is arranged on the outside of the hydrogen purification device, the outer shell (13) is located on the support platform (12) and is fixedly connected to the support platform (12), a side wall of the outer shell (13) is fixedly connected to the gas processing shell (14) near the upper area, one end of the gas processing shell (14) and the inside of the outer shell (13) are connected to each other, and the reverse corner area of the upper wall of the outer shell (13) is fixedly connected to a plurality of fuel cells at the same distance. A warm air blower (15), a cooling assembly piece (16) is vertically fixed to the inner wall of the outer shell (13) at the tail of the cooling air blower (15), the wall areas on the front and back sides of the tail inside the outer shell (13) are respectively fixed to a receiving shell (17), a shielding piece (18) is fixed to the inside of the outer shell (13) between the two receiving shells (17) on the front and back sides, the cooling assembly piece (16) includes a pointing piece (1612), a vertically installed pointing piece (1612) is fixed to the cooling assembly piece (16), the front end of the pointing piece (1612) is placed inside the outer shell (13), and the back end of the pointing piece (1612) is in contact with the back side of the outer shell (13).
2. The high-efficiency methanol reforming hydrogen production power system according to claim 1, characterized in that: The supporting platform (12) includes a liquid storage shell (1212) and a discharge channel (1213). The square liquid storage shell (1212) is fixedly connected to the upper wall of the supporting platform (12). The tail area of the right wall of the liquid storage shell (1212) is fixedly connected to the discharge channel (1213) connected to the outside at a 90-degree angle. The lower wall inside the liquid storage shell (1212) is arranged in a slope.
3. The high-efficiency methanol reforming hydrogen production power system according to claim 1, characterized in that: The outer shell (13) includes an inlet hole (1312), an air inlet hole (1313), a receiving chamber (1314) and a leakage hole (1315). A square inlet hole (1312) is reserved in the area on the right wall of the outer shell (13) and adapted to the gas processing shell (14). A square inlet hole (1313) is reserved in the area at the tail of the cooling assembly piece (16) inside the outer shell (13). A receiving chamber (1314) is reserved in the outer shell (13) on the opposite side of the air inlet hole (1313). Leakage holes (1315) that penetrate the liquid storage shell (1212) are reserved on both sides of the front wall of the receiving chamber (1314).
4. The high-efficiency methanol reforming hydrogen production power system according to claim 1, characterized in that: The gas processing shell (14) includes calcium chloride columns (1412). The front of the gas processing shell (14) is slidably embedded with the calcium chloride columns (1412) arranged at equal distances at a 90-degree angle. The tail of the gas processing shell (14) is open and arranged. The tail of the gas processing shell (14) is skewed.
5. The high-efficiency methanol reforming hydrogen production power system according to claim 1, characterized in that: The two pointing pieces (1612) form a pair, and the two pointing pieces (1612) in a pair are arranged in a mirror-image curved structure.
6. The high-efficiency methanol reforming hydrogen production power system according to claim 1, characterized in that: The two receiving shells (17) on the front and back sides both have a triangular prism structure with an angle of ninety degrees, and the slopes of the two receiving shells (17) are opposite to each other.
7. The high-efficiency methanol reforming hydrogen production power system according to claim 1, characterized in that: The shielding piece (18) includes a supporting piece (1812), and the shielding piece (18) is a curved structure protruding upward. The protruding central area in the shielding piece (18) is fixedly connected to the supporting piece (1812) at a 90-degree angle toward the tail, and the two sides of the supporting piece (1812) are fixedly connected to the two inner sides of the outer shell (13).
8. A high-efficiency methanol reforming hydrogen production method, characterized by: The device according to any one of claims 1 to 7 further comprises the following steps: S1: The methanol in the hydrogen storage tank (11) is sent to the methanol reforming reactor (111) through a pipeline for reforming reaction, and then sent to the hydrogen purification device through a pipeline for purification and then sent to the fuel cell (113) for power generation S2: During normal operation of the hydrogen purification device, the surrounding low-temperature gas flows in from the inlet hole (1312), moves toward the rear through the upper part of the outer shell (13), and carries the high-temperature gas inside from the air inlet hole (1313) through the reverse side of the cooling assembly piece (16) and is discharged upward. The reverse movement of gaseous water energy generated during the discharge process is gathered in the receiving chamber (1314), discharged from the leakage hole (1315) and accumulated in the liquid storage shell (1212); S3: The tail of the gas treatment shell (14) is tilted and can introduce low-temperature gas from the side of the gas treatment shell (14). The tilted introduction hole structure can reduce the introduction of pollutants. The calcium chloride column (1412) can be manually replaced to filter out gaseous water in the moving gas; S4: The pointing piece (1612) can allow the passing gas to touch and intersect back and forth, thereby increasing the touch area and the effective period, thereby ensuring efficient cooling, and the pointing piece (1612) at the end can process the introduced gas to filter out, allowing floating objects and gaseous water to fall into the receiving chamber (1314) for collection and treatment.