• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The invention called "compression-assisted hydrogen storage system by compressive residual heat", consists of the efficient compression of hydrogen at high pressure (900-1000 bar) where the heat developed by the multi-stage compression process with cooling intermediate of hydrogen, is used to be converted into mechanical and/or electrical energy and used to partially supply the demand for compression energy, significantly increasing the efficiency of the overall compression process. (Machine-translation by Google Translate, not legally binding)
    公开号:ES2618294A1
    申请号:ES201500912
    申请日:2015-12-18
    公开日:2017-06-21
    发明作者:Ramón FERREIRO GARCÍA
    申请人:Universidade da Coruna；
    IPC主号:
    专利说明:

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    DESCRIPTION
    Hydrogen storage system by compression assisted by residual compression heat.
    Technical field of the invention
    The present invention pertains to the technical field of high pressure storage of hydrogen intended for fuel supply to thermal machines operating with hydrogen as fuels.
    Objective of the invention
    The objective of the present invention called "HYDROGEN STORAGE SYSTEM BY COMPRESSION ASSISTED BY RESIDUAL HEAT OF COMPRESSION", consists in the efficient compression of hydrogen at high pressure (900-1000 bar) where the heat developed by the multi compression process -step or polyphasic with intermediate hydrogen cooling, is used to be converted into mechanical and / or electrical energy and used to partially supply the demand for compression energy, significantly reducing the net compression work or significantly increasing the overall process efficiency of compression.
    Background of the invention
    The currently known hydrogen storage procedures are based on the following technologies:
    Physical storage comprising,
    - gaseous compression of hydrogen above 700 bar
    - cryogenic compression between 10 and 350 bar
    - hydrogen liquefaction between 1 and 10 bar stored in cryogenic tanks Solid hydrogen storage comprising procedures based on
    - Hydrides or hydrogen compounds with other metallic, chemical, or organic elements such as
    - adsorption based on activated carbon,
    - adsorption based on zeolites or very porous natural solid rock or,
    - adsorption based on metal-organic compounds MOF (metal-organic frameworks).
    The hydrogen storage technique proposed in this invention belongs to the hydrogen gas compression group above 700 bar in which the residual hydrogen compression energy is used, whose heat is converted into mechanical and / or electrical energy to be recovered and feed the hydrogen compression process both optionally mechanically or electrically.
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    Brief Description of the Invention
    The invention called "HYDROGEN STORAGE SYSTEM FOR COMPRESSION ASSISTED BY RESIDUAL COMPRESSION HEAT" is to take advantage of the residual thermal energy generated during the hydrogen compression process, and convert it to mechanical and / or electrical energy to complement the demand for mechanical energy or electric used by the hydrogen compression system. The system is based on the fact that the cooling heat of the low, medium and high pressure compressors is used to drive an alternative actuator cylinder, which drives a hydrogen compressor cylinder that helps increase the hydrogen pressure at the compressor inlet of hydrogen from the first phase, reducing the net compression work and increasing the thermal efficiency of the plant.
    Description of the figures
    In this section, the components constituting the invention called "HYDROGEN STORAGE SYSTEM BY COMPRESSION ASSISTED BY RESIDUAL COMPRESSION HEAT" are described in an illustrative and non-limiting manner, to facilitate the understanding of the invention where reference is made to the following figures :
    Figure 1 shows the scheme of the fundamental configuration of the invention called "HYDROGEN STORAGE SYSTEM BY COMPRESSION ASSISTED BY RESIDUAL HEAT OF COMPRESSION", which shows the following components:
    1 low pressure hydrogen supply line
    2 by-pass valve
    3 hydrogen cooler at room temperature
    4 first phase hydrogen compressor
    5 first phase hydrogen cooler
    6 second phase hydrogen compressor
    7 second phase hydrogen cooler
    8 third phase hydrogen compressor
    9 third stage hydrogen cooler
    10 high pressure hydrogen discharge duct
    11 circulation pump of thermal working fluid
    12 actuator cylinder
    13 cylinder hydrogen compressor
    14 valve 2p-3v (two positions-three vlas) of heat supply to the actuator cylinder
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    15 valve 2p-3v heat return actuator cylinder
    16 2p-3v fry supply valve to the actuator cylinder
    17 2p-3v return valve for actuator cylinder
    18 2p-3v hydrogen supply valve to the compressor cylinder
    19 valve 2p-3v hydrogen discharge compressor cylinder
    20 regeneration valve by mixing in the actuator cylinder Detailed description of the invention
    The "HYDROGEN STORAGE SYSTEM FOR COMPRESSION ASSISTED BY RESIDUAL HEAT OF COMPRESSION", consisting of the following components:
    - low pressure hydrogen supply line (1) from the hydrogen generating plant
    - by-pass valve (2) designed to facilitate the entry of hydrogen directly from the hydrogen generating plant to the hydrogen compressor of the first phase during the plant start-up operation phase
    - hydrogen cooler at room temperature (3)
    - first phase hydrogen compressor (4)
    - First phase hydrogen cooler (5) operating as heat recovery of the first phase compressor
    - hydrogen compressor of the second phase (6)
    - Hydrogen cooler of the second phase (7) that operates as heat recovery of the second phase compressor
    - third phase hydrogen compressor (8)
    - third stage hydrogen cooler (9) operating as heat recovery of the third phase compressor
    10 high pressure hydrogen discharge duct (10) to the storage cylinder-bottles
    - circulation pump of the thermal working fluid (11) which operates in a closed circuit
    - actuator cylinder (12) which, by virtue of the heat supplied, moves in the opposite direction to that of heat application and in the same direction of application of fried
    - hydrogen compressor cylinder (13) which is driven by the actuator cylinder (12)
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    - 2p-3v valve (two positions-three vlas) of heat supply to the actuator cylinder (14) by means of a thermal working fluid that can be a thermal oil or a gaseous thermal fluid such as hydrogen or helium
    - 2p-3v heat return valve of the actuator cylinder (15) by means of a thermal working fluid
    - 2p-3v cold fluid supply valve to the actuator cylinder (16) consisting of a thermal cooling fluid such as fresh water
    - 2p-3v cold fluid return valve of the actuator cylinder (17)
    - 2p-3v hydrogen supply valve to the compressor cylinder (18) through the suction zone of the alternative compressor (13)
    - 2p-3v hydrogen discharge valve from the compressor cylinder (19) to the hydrogen cooler (3)
    - regeneration valve by mixing in the actuator cylinder (20) intended to intercommunicate the two zones of the cylinder (12) in order to contribute to regenerate by mixing both zones of the actuator cylinder alternately.
    The mentioned set of elements is characterized by operating so that the heat generated by the compressors (4), (6) and (8) is used to partially supply the compression system, by means of the alternative compressor (13) driven by the actuator cylinder (12), according to the following sequence:
    The hydrogen to be compressed is supplied by the low pressure hydrogen supply line (1) and conducted through the by-pass valve (2) and the cooler (3) to the first phase hydrogen compressor. It is then cooled by the working thermal fluid in the cooler (5), it is compressed again in the hydrogen compressor of the second phase, it is cooled in the hydrogen cooler of the second phase (7), repeating the process of compression and cooling in the third phase hydrogen compressor (8) and cooled by the third phase hydrogen cooler (9), being stored in bottles or cylinders at high pressure (800-1000) bar. When the actuator cylinder (12) that drives the alternative compressor (13) has enough heat to operate, the bypass valve (2) is closed, forcing the hydrogen present in the hydrogen supply line (1) to pass to the compressor (13) that compresses it and transfers it through a cooler (3) to be compressed by means of the hydrogen compressor (4) and the successive phases until the exit through the high pressure hydrogen discharge duct (10), around at 800-1000 bar.
    Where the actuator cylinder (12) operates in such a way that the thermal fluid working at high temperature driven by the circulation pump (11) passes to the heater located in the left zone of the actuator cylinder (12) through the 2p-3v valve (14), and returning by the valve 2p-3v (15) at low temperature, whereby the left zone of the cylinder (12) is active and the piston of the actuator cylinder (12) moves to the right, while the Working coolant enters the right area of the actuator cylinder through the 2p-3v valve (16) and exits through the 2p-3v valve (17). When the actuator cylinder has reached the right end of stroke, the valves 2p-3v (14), (15), (16) and (17) are closed, the regeneration valve (20) is opened until the pressures between both zones of the actuator cylinder (12). In this state, the 2p-3v valve (17) is closed and the cycle is repeated with the role of the 2p-3v (14), (15), (16) and (17) valves changed to make the area active
    right of the actuator cylinder (12) causing its piston or piston to move to the left.
    Preferred Embodiment of the Invention
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    The preferred embodiment of the HYDROGEN STORAGE SYSTEM FOR COMPRESSION ASSISTED THROUGH RESIDUAL COMPRESSION HEAT corresponds to the scheme shown in Figure 1 in accordance with the description given in the preceding section relative to the detailed description of the invention.
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    权利要求:
    Claims (2)
    [1]
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    1. Hydrogen storage system by compression assisted by residual compression heat, which consists of the following components:
    - low pressure hydrogen supply line (1) from the hydrogen generating plant
    - by-pass valve (2) designed to facilitate the entry of hydrogen directly from the hydrogen generating plant to the hydrogen compressor of the first phase during the plant start-up operation phase
    - hydrogen cooler at room temperature (3)
    - first phase hydrogen compressor (4)
    - First phase hydrogen cooler (5) operating as heat recovery of the first phase compressor
    - hydrogen compressor of the second phase (6)
    - Hydrogen cooler of the second phase (7) that operates as heat recovery of the second phase compressor
    - third phase hydrogen compressor (8)
    - third stage hydrogen cooler (9) operating as heat recovery of the third phase compressor
    10 high pressure hydrogen discharge duct (10) to the storage cylinder-bottles
    - circulation pump of the thermal working fluid (11) which operates in a closed circuit
    - actuator cylinder (12) which, by virtue of the heat supplied, moves in the opposite direction to that of heat application and in the same direction of application of fried
    - hydrogen compressor cylinder (13) which is driven by the actuator cylinder (12)
    - 2p-3v valve (two positions-three vlas) of heat supply to the actuator cylinder (14) by means of a thermal working fluid that can be a thermal oil or a gaseous thermal fluid such as hydrogen or helium
    - 2p-3v heat return valve of the actuator cylinder (15) by means of a thermal working fluid
    - 2p-3v cold fluid supply valve to the actuator cylinder (16) consisting of a thermal cooling fluid such as fresh water
    - 2p-3v cold fluid return valve of the actuator cylinder (17)
    - 2p-3v hydrogen supply valve to the compressor cylinder (18) through the aspiration zone of the alternative compressor (13)
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    - 2p-3v hydrogen discharge valve from the compressor cylinder (19) to the hydrogen cooler (3)
    - regeneration valve by mixing in the actuator cylinder (20) intended to intercommunicate the two zones of the cylinder (12) in order to contribute to regenerate by mixing both zones of the actuator cylinder alternately,
    It is characterized by operating so that the heat generated by the compressors (4), (6) and (8) is used to partially supply the compression system, by means of the alternative compressor (13) driven by the actuator cylinder (12) .
    [2]
    2. Hydrogen storage system by compression assisted by residual compression heat according to revindication 1a characterized by the operation procedure according to which, the hydrogen to be compressed is supplied by the low pressure hydrogen supply conduit (1) and conducted to through the bypass valve (2) and the cooler (3) to the hydrogen compressor of the first phase. It is then cooled by the working thermal fluid in the cooler (5), it is compressed again in the hydrogen compressor of the second phase, it is cooled in the hydrogen cooler of the second phase (7), repeating the process of compression and cooling in the third phase hydrogen compressor (8) and cooled by the third phase hydrogen cooler (9), being stored in bottles or cylinders at high pressure (800-1000) bar. When the actuator cylinder (12) that drives the alternative compressor (13) has enough heat to operate, the bypass valve (2) is closed, forcing the hydrogen present in the hydrogen supply line (1) to pass to the compressor (13) that compresses it and transfers it through a cooler (3) to be compressed by means of the hydrogen compressor (4) and the successive phases until the exit through the high pressure hydrogen discharge duct (10), around at 800-1000 bar.
    Where the actuator cylinder (12) operates in such a way that the thermal fluid working at high temperature driven by the circulation pump (11) passes to the heater located in the left zone of the actuator cylinder (12) through the 2p-3v valve (14), and returning by the valve 2p-3v (15) at low temperature, whereby the left zone of the cylinder (12) is active and the piston of the actuator cylinder (12) moves to the right, while the Working coolant enters the right area of the actuator cylinder through the 2p-3v valve (16) and exits through the 2p-3v valve (17). When the actuator cylinder has reached the right end of stroke, the valves 2p-3v (14), (15), (16) and (17) are closed, the regeneration valve (20) is opened until the pressures between both zones of the actuator cylinder (12). In this state, the 2p-3v valve (17) is closed and the cycle is repeated with the role of the 2p-3v (14), (15), (16) and (17) valves changed to activate the right area of the actuator cylinder (12) causing its piston or piston to move to the left.
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    同族专利:
    公开号 | 公开日
    ES2618294B2|2017-11-28|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    FR402589A|1909-04-30|1909-10-12|Laurent Pierre Guedon|Process for using or recovering the heat generated in air compressors|
    DE3134844A1|1980-12-09|1982-07-08|Veb Kombinat Pumpen Und Verdichter, Ddr 4020 Halle|Method for the energy optimisation of a compression process|
    法律状态:
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