CN105186022A - Alcohol-to-hydrogen electric pump - Google Patents

Alcohol-to-hydrogen electric pump Download PDF

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Publication number
CN105186022A
CN105186022A CN201510658423.7A CN201510658423A CN105186022A CN 105186022 A CN105186022 A CN 105186022A CN 201510658423 A CN201510658423 A CN 201510658423A CN 105186022 A CN105186022 A CN 105186022A
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hydrogen
gas
oxygen
reformer chamber
producer
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CN201510658423.7A
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Chinese (zh)
Inventor
向华
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Shanghai Hejide Dynamic Hydrogen Machine Co Ltd
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Shanghai Hejide Dynamic Hydrogen Machine Co Ltd
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Priority to CN201510658423.7A priority Critical patent/CN105186022A/en
Publication of CN105186022A publication Critical patent/CN105186022A/en
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    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
    • H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
    • H01M8/0612—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
    • H01M8/0618—Reforming processes, e.g. autothermal, partial oxidation or steam reforming
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/22—Fuel cells in which the fuel is based on materials comprising carbon or oxygen or hydrogen and other elements; Fuel cells in which the fuel is based on materials comprising only elements other than carbon, oxygen or hydrogen
    • 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
    • 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
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/10—Process efficiency
    • Y02P20/133—Renewable energy sources, e.g. sunlight
    • 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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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Sustainable Energy (AREA)
  • Sustainable Development (AREA)
  • Manufacturing & Machinery (AREA)
  • Electrochemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Fuel Cell (AREA)

Abstract

The invention discloses an alcohol-to-hydrogen electric pump which comprises a pump body, a methanol-to-hydrogen system, a hydrogen power generation system and a motor. The methanol-to-hydrogen system, the hydrogen power generation system, the motor and the pump body are sequentially connected; the methanol-to-hydrogen system prepares hydrogen through methanol steam reforming, the hydrogen passes through a membrane separation device with palladium-silver alloy to obtain high-purity hydrogen, the obtained hydrogen generates power through the hydrogen power generation system, and the generated power energy is supplied to operation of the motor to drive the pump body to work. According to the alcohol-to-hydrogen electric pump, methanol is utilized as the energy of the pump body, and the pump body can be applied to sites free of alternating currents.

Description

The electronic pump housing of a kind of alcohol hydrogen
Technical field
The invention belongs to electrical equipment technical field, relate to a kind of electric water pump, particularly relate to the electronic pump housing of a kind of alcohol hydrogen.
Background technology
Water pump is conveying liquid or the machinery making fluid pressurization.It sends the mechanical energy of prime mover or other external energies to liquid, liquid energy is increased, be mainly used to conveying liquid and comprise water, oil, acid & alkali liquid, emulsion, suspended emulsion and liquid metal etc., also can carry liquid, admixture of gas and the liquid containing suspended solids.
Existing water pump needs to plug alternating current and could work.And under many circumstances, people wish also can use water pump in the wild.Existing water pump cannot complete this work.
In view of this, nowadays in the urgent need to designing a kind of new water pump, to overcome the above-mentioned defect of existing water pump existence.
Summary of the invention
Technical problem to be solved by this invention is: provide a kind of alcohol hydrogen the electronic pump housing, hydrogen from methyl alcohol can be utilized to generate electricity as the energy of the pump housing, the pump housing can be used for the place not having alternating current.
For solving the problems of the technologies described above, the present invention adopts following technical scheme:
The electronic pump housing of a kind of alcohol hydrogen, the described electronic pump housing comprises: pump body, hydrogen production by methanol system, hydrogen gas generating system, motor, and hydrogen production by methanol system, hydrogen gas generating system, motor, pump body connect successively; Pump body comprises motor unit, pump unit, housing unit, cap unit; Motor unit comprises stator, rotor core and axle; Pump unit comprises inner rotator and external rotor, and inner rotator is attached to axle and inner rotator is formed with outer projection, and external rotor to be arranged on outside inner rotator and to have internal protrusion, and internal protrusion is formed as engaging with outer projection; Housing unit comprises motor shell and pump case, and pump case is connected to motor shell and is formed with pump accommodation section in pump case, is inserted with pump unit in pump accommodation section;
Described hydrogen production by methanol system comprises hydrogen manufacturing subsystem, air pressure adjustment subsystem, Collection utilization subsystem, and hydrogen manufacturing subsystem, air pressure adjustment subsystem, hydrogen gas generating system, Collection utilization subsystem connect successively;
Described hydrogen manufacturing subsystem utilizes methanol-water to prepare hydrogen, and described hydrogen manufacturing subsystem comprises solid hydrogen reservoir vessel, liquid container, raw material conveying device, device for rapidly starting, hydrogen producer, membrane separation device;
Described hydrogen producer comprises heat exchanger, vaporizer, reformer chamber; Membrane separation device is arranged in separation chamber, and separation chamber is arranged at the inside of reformer chamber; Described solid hydrogen reservoir vessel, liquid container are connected with hydrogen producer respectively; Liquid first alcohol and water is stored in liquid container;
Described device for rapidly starting provides the startup energy for hydrogen producer; Described device for rapidly starting comprises the first starting drive, the second starting drive; Described first starting drive comprises the first heating arrangements, the first gasification pipe, and the internal diameter of the first gasification pipe is 1 ~ 2mm, and the first gasification pipe is closely wound on the first heating arrangements; One end of described first gasification pipe connects liquid container, sends in the first gasification pipe by raw material conveying device by methyl alcohol; The other end of the first gasification pipe exports vaporized methyl alcohol, then by ignition mechanism ignition; Or the other end of the first gasification pipe exports vaporized methyl alcohol, and the methanol temperature exported reaches self-ignition point, directly spontaneous combustion after methyl alcohol exports from the first gasification pipe; Described second starting drive comprises the second gasification pipe, the main body of the second gasification pipe is arranged at described reformer chamber, first gasification pipe is or/and the methyl alcohol that the second gasification pipe exports is heat the second gasification pipe, by the methanol gasifying in the second gasification pipe while reformer chamber heats; Described reformer chamber inwall is provided with heating pipe line, is placed with catalyst in heating pipe line; Described device for rapidly starting is reformer chamber heating by the described heating pipe line of heating; After described hydrogen generating system starts, hydrogen generating system provides the energy needed for operation by the hydrogen that hydrogen producer obtains;
The initial start energy of described device for rapidly starting is that some solar energy starts module, and solar energy starts module and comprises the solar panel, solar energy-electric energy change-over circuit, the solar cell that connect successively; Solar energy starts module provides electric energy for the first heating arrangements; Or the initial start energy of described device for rapidly starting is manual generator, manual generator by the power storage that sends in battery;
Described catalyst comprises oxide, the oxide of Pd, the oxide of Cu, the oxide of Fe, the oxide of Zn, rare-earth oxide, the transition metal oxide of Pt; Wherein, precious metals pt content accounts for 0.6% ~ 1.8% of catalyst gross mass, Pd content accounts for 1.1% ~ 4% of catalyst gross mass, the oxide of Cu accounts for 6% ~ 12% of catalyst gross mass, the oxide of Fe accounts for 3% ~ 8% of catalyst gross mass, the oxide of Zn accounts for 8% ~ 20% of catalyst gross mass, and rare-earth oxide accounts for 6% ~ 40% of catalyst gross mass, and all the other are transition metal oxide;
Or described catalyst is copper-based catalysts, comprise material and mass fraction is: the CuO of 3-17 part, the ZrO of the ZnO of 3-18 part, 0.5-3 part, the Al of 55-80 part 2o 3, the CeO of 1-3 part 2, the La of 1-3 part 2o 3;
Store solid hydrogen in described solid hydrogen reservoir vessel, when hydrogen generating system starts, by gasification module, solid hydrogen is converted to gaseous hydrogen, gaseous hydrogen passes through combustion heat release, for hydrogen producer provides startup heat energy, as the startup energy of hydrogen producer;
First alcohol and water in described liquid container is delivered to heat exchanger heat exchange by raw material conveying device, enters vaporizer gasification after heat exchange; Methanol vapor after gasification and steam enter reformer chamber, and reformer chamber is provided with catalyst, and reformer chamber bottom and middle portion temperature are 300 DEG C ~ 420 DEG C; The temperature on described reformer chamber top is 400 DEG C ~ 570 DEG C; Reformer chamber is connected by connecting line with separation chamber, all or part of top being arranged at reformer chamber of connecting line, and the high temperature by reformer chamber top continues the gas that heating exports from reformer chamber; Described connecting line, as the buffering between reformer chamber and separation chamber, makes the temperature of the gas exported from reformer chamber identical with the temperature of separation chamber or close; Temperature in described separation chamber is set as 350 DEG C ~ 570 DEG C; Be provided with membrane separator in separation chamber, obtain hydrogen from the aerogenesis end of membrane separator;
Described raw material conveying device provides power, by the feedstock transportation in liquid container to hydrogen producer; Described raw material conveying device provides the pressure of 0.15 ~ 5MPa to raw material, and the hydrogen that hydrogen producer is obtained has enough pressure;
After described hydrogen producer starts hydrogen manufacturing, the hydrogen partial that hydrogen producer is obtained is or/and residual air is run by burning maintenance hydrogen producer;
The hydrogen that described hydrogen producer obtains is delivered to membrane separation device and is separated, and is more than or equal to 0.7MPa for separating of the difference of pressure inside and outside the membrane separation device of hydrogen; Described membrane separation device is the membrane separation device at porous ceramic surface Vacuum Deposition palladium-silver, and film plating layer is palladium-silver, and the mass percent palladium of palladium-silver accounts for 75% ~ 78%, and silver accounts for 22% ~ 25%;
Obtained hydrogen is passed through transfer conduit real-time Transmission to hydrogen gas generating system by described hydrogen manufacturing subsystem; Described transfer conduit is provided with air pressure adjustment subsystem, for adjusting the air pressure in transfer conduit; The hydrogen gas generation that described hydrogen gas generating system utilizes hydrogen manufacturing subsystem obtained;
Described air pressure adjustment subsystem comprises microprocessor, gas pressure sensor, valve positioner, air outlet valve, outlet pipe; Described gas pressure sensor is arranged in transfer conduit, in order to respond to the barometric information in transfer conduit, and the barometric information of induction is sent to microprocessor; This barometric information received from gas pressure sensor and setting threshold interval are compared by described microprocessor; When the pressure data received is higher than the maximum in setting threshold interval, Microprocessor S3C44B0X valve positioner opens air outlet valve setting-up time, air pressure in transfer conduit is made to be in setting range, one end of outlet pipe connects air outlet valve simultaneously, the other end connects described hydrogen manufacturing subsystem, and the firing equipment that needs being hydrogen manufacturing subsystem by burning heats; When the pressure data received is lower than the minimum value in setting threshold interval, hydrogen manufacturing subsystem described in Microprocessor S3C44B0X accelerates the transporting velocity of raw material;
Described Collection utilization subsystem connects the Vent passageway of hydrogen gas generating system, hydrogen, oxygen, water is collected respectively from the gas of discharging, utilize collect hydrogen, oxygen for hydrogen manufacturing subsystem or/and hydrogen gas generating system, the water collected as the raw material of hydrogen manufacturing subsystem, thus recycles;
Described Collection utilization subsystem comprises hydrogen/oxygen separator, hydrogen separator, hydrogen check-valves, oxygen separator, oxygen check valve, by hydrogen and oxygen separation, is then separated with water by hydrogen respectively, oxygen is separated with water;
Described hydrogen producer also comprises electric energy estimation block, hydrogen prepares detection module, power storage module; Whether described electric energy estimation block can meet reformation in order to the electric energy estimated hydrogen gas generation device and send in real time, the electric energy of needs consumption when being separated; If met, then close device for rapidly starting;
Whether hydrogen is prepared detection module and is used for detecting the hydrogen prepared in real time of hydrogen producer and stablizes; If hydrogen prepared by hydrogen producer is unstable, then controls device for rapidly starting and again start, and the electric energy part obtained is stored in power storage module, use when electric energy is not enough to the consumption providing hydrogen producer;
Described hydrogen gas generating system is fuel cell system, and fuel cell system comprises: gas supply device, pile; Described gas supply device utilizes the gas of compression as power, and automatic transport is in pile; Described pile comprises some sub-fuel cell modules, and each sub-fuel cell module comprises at least one super capacitor;
Described fuel cell system also comprises air intake conduit, outlet pipe; The gas of described compression is mainly oxygen; Air enters pile with oxygen after mixer mixes;
Described fuel cell system also comprises gas regulating system; Described gas regulating system comprises valve regulated control device, and oxygen content transducer is or/and Compressed Gas compression ratio transducer;
The data sensed in order to respond to the content of oxygen in the air and oxygen that mix in mixer, and are sent to valve regulated control device by described oxygen content transducer;
The data sensed in order to the compression ratio of induced compression oxygen, and are sent to valve regulated control device by described Compressed Gas compression ratio transducer;
Described valve regulated control device or/and the induction result of Compressed Gas compression ratio transducer regulates oxygen infusion valve, air entrainment valve door, controls the conveying ratio of compressed oxygen, air according to oxygen content transducer; Mist is pushed to pile reaction by the power that compressed oxygen produces after entering mixer;
Described fuel cell system also comprises humidification system, and humidification system comprises humidity exchanging container, humidity exchanges pipeline, and it is a part for air intake conduit that humidity exchanges pipeline; After described reaction, gas outlet pipe is delivered to humidity exchanging container,
The material that described humidity exchanges pipeline is only permeable airtight, makes to react rear gas and natural air carries out humidity exchange, and cannot circulate between gas.
The electronic pump housing of a kind of alcohol hydrogen, the described electronic pump housing comprises: pump body, hydrogen production by methanol system, hydrogen gas generating system, motor, and hydrogen production by methanol system, hydrogen gas generating system, motor, pump body connect successively;
Described hydrogen production by methanol system utilizes preparing hydrogen by reforming methanol-water steam, hydrogen obtains highly purified hydrogen by the membrane separation device being coated with palladium-silver, the hydrogen obtained is generated electricity by hydrogen gas generating system, and the electric energy power supply machine sent runs, thus drives this body running of pump.
As a preferred embodiment of the present invention, described hydrogen production by methanol system comprises hydrogen manufacturing subsystem, air pressure adjustment subsystem, Collection utilization subsystem, and hydrogen manufacturing subsystem, air pressure adjustment subsystem, hydrogen gas generating system, Collection utilization subsystem connect successively;
Described hydrogen manufacturing subsystem utilizes methanol-water to prepare hydrogen, and described hydrogen manufacturing subsystem comprises solid hydrogen reservoir vessel, liquid container, raw material conveying device, device for rapidly starting, hydrogen producer, membrane separation device;
Described hydrogen producer comprises heat exchanger, vaporizer, reformer chamber; Membrane separation device is arranged in separation chamber, and separation chamber is arranged at the inside of reformer chamber; Described solid hydrogen reservoir vessel, liquid container are connected with hydrogen producer respectively; Liquid first alcohol and water is stored in liquid container;
Described device for rapidly starting provides the startup energy for hydrogen producer; Described device for rapidly starting comprises the first starting drive, the second starting drive; Described first starting drive comprises the first heating arrangements, the first gasification pipe, and the internal diameter of the first gasification pipe is 1 ~ 2mm, and the first gasification pipe is closely wound on the first heating arrangements; One end of described first gasification pipe connects liquid container, sends in the first gasification pipe by raw material conveying device by methyl alcohol; The other end of the first gasification pipe exports vaporized methyl alcohol, then by ignition mechanism ignition; Or the other end of the first gasification pipe exports vaporized methyl alcohol, and the methanol temperature exported reaches self-ignition point, directly spontaneous combustion after methyl alcohol exports from the first gasification pipe; Described second starting drive comprises the second gasification pipe, the main body of the second gasification pipe is arranged at described reformer chamber, first gasification pipe is or/and the methyl alcohol that the second gasification pipe exports is heat the second gasification pipe, by the methanol gasifying in the second gasification pipe while reformer chamber heats; Described reformer chamber inwall is provided with heating pipe line, is placed with catalyst in heating pipe line; Described device for rapidly starting is reformer chamber heating by the described heating pipe line of heating; After described hydrogen generating system starts, hydrogen generating system provides the energy needed for operation by the hydrogen that hydrogen producer obtains;
Store solid hydrogen in described solid hydrogen reservoir vessel, when hydrogen generating system starts, by gasification module, solid hydrogen is converted to gaseous hydrogen, gaseous hydrogen passes through combustion heat release, for hydrogen producer provides startup heat energy, as the startup energy of hydrogen producer;
First alcohol and water in described liquid container is delivered to heat exchanger heat exchange by raw material conveying device, enters vaporizer gasification after heat exchange; Methanol vapor after gasification and steam enter reformer chamber, and reformer chamber is provided with catalyst, and reformer chamber bottom and middle portion temperature are 300 DEG C ~ 420 DEG C; The temperature on described reformer chamber top is 400 DEG C ~ 570 DEG C; Reformer chamber is connected by connecting line with separation chamber, all or part of top being arranged at reformer chamber of connecting line, and the high temperature by reformer chamber top continues the gas that heating exports from reformer chamber; Described connecting line, as the buffering between reformer chamber and separation chamber, makes the temperature of the gas exported from reformer chamber identical with the temperature of separation chamber or close; Temperature in described separation chamber is set as 350 DEG C ~ 570 DEG C; Be provided with membrane separator in separation chamber, obtain hydrogen from the aerogenesis end of membrane separator;
Described raw material conveying device provides power, by the feedstock transportation in liquid container to hydrogen producer; Described raw material conveying device provides the pressure of 0.15 ~ 5MPa to raw material, and the hydrogen that hydrogen producer is obtained has enough pressure;
After described hydrogen producer starts hydrogen manufacturing, the hydrogen partial that hydrogen producer is obtained is or/and residual air is run by burning maintenance hydrogen producer;
The hydrogen that described hydrogen producer obtains is delivered to membrane separation device and is separated, and is more than or equal to 0.7MPa for separating of the difference of pressure inside and outside the membrane separation device of hydrogen; Described membrane separation device is the membrane separation device at porous ceramic surface Vacuum Deposition palladium-silver, and film plating layer is palladium-silver, and the mass percent palladium of palladium-silver accounts for 75% ~ 78%, and silver accounts for 22% ~ 25%;
Obtained hydrogen is passed through transfer conduit real-time Transmission to hydrogen gas generating system by described hydrogen manufacturing subsystem; Described transfer conduit is provided with air pressure adjustment subsystem, for adjusting the air pressure in transfer conduit; The hydrogen gas generation that described hydrogen gas generating system utilizes hydrogen manufacturing subsystem obtained;
Described air pressure adjustment subsystem comprises microprocessor, gas pressure sensor, valve positioner, air outlet valve, outlet pipe; Described gas pressure sensor is arranged in transfer conduit, in order to respond to the barometric information in transfer conduit, and the barometric information of induction is sent to microprocessor; This barometric information received from gas pressure sensor and setting threshold interval are compared by described microprocessor; When the pressure data received is higher than the maximum in setting threshold interval, Microprocessor S3C44B0X valve positioner opens air outlet valve setting-up time, air pressure in transfer conduit is made to be in setting range, one end of outlet pipe connects air outlet valve simultaneously, the other end connects described hydrogen manufacturing subsystem, and the firing equipment that needs being hydrogen manufacturing subsystem by burning heats; When the pressure data received is lower than the minimum value in setting threshold interval, hydrogen manufacturing subsystem described in Microprocessor S3C44B0X accelerates the transporting velocity of raw material;
Described Collection utilization subsystem connects the Vent passageway of hydrogen gas generating system, hydrogen, oxygen, water is collected respectively from the gas of discharging, utilize collect hydrogen, oxygen for hydrogen manufacturing subsystem or/and hydrogen gas generating system, the water collected as the raw material of hydrogen manufacturing subsystem, thus recycles;
Described Collection utilization subsystem comprises hydrogen/oxygen separator, hydrogen separator, hydrogen check-valves, oxygen separator, oxygen check valve, by hydrogen and oxygen separation, is then separated with water by hydrogen respectively, oxygen is separated with water.
As a preferred embodiment of the present invention, the initial start energy of described device for rapidly starting is that some solar energy starts module, and solar energy starts module and comprises the solar panel, solar energy-electric energy change-over circuit, the solar cell that connect successively; Solar energy starts module provides electric energy for the first heating arrangements; Or the initial start energy of described device for rapidly starting is manual generator, manual generator by the power storage that sends in battery.
As a preferred embodiment of the present invention, described catalyst comprises oxide, the oxide of Pd, the oxide of Cu, the oxide of Fe, the oxide of Zn, rare-earth oxide, the transition metal oxide of Pt;
Wherein, precious metals pt content accounts for 0.6% ~ 1.8% of catalyst gross mass, Pd content accounts for 1.1% ~ 4% of catalyst gross mass, the oxide of Cu accounts for 6% ~ 12% of catalyst gross mass, the oxide of Fe accounts for 3% ~ 8% of catalyst gross mass, the oxide of Zn accounts for 8% ~ 20% of catalyst gross mass, and rare-earth oxide accounts for 6% ~ 40% of catalyst gross mass, and all the other are transition metal oxide.
As a preferred embodiment of the present invention, described catalyst is copper-based catalysts, comprises material and mass fraction is: the CuO of 2-20 part, the ZrO of the ZnO of 2-20 part, 0.1-5 part, the Al of 45-95 part 2o 3, the CeO of 0-5 part 2, the La of 0-5 part 2o 3.
As a preferred embodiment of the present invention, described hydrogen gas generating system comprises fuel cell, and fuel cell comprises some sub-fuel cell modules, and each sub-fuel cell module comprises at least one super capacitor.
As a preferred embodiment of the present invention, described hydrogen gas generating system is fuel cell system, and fuel cell system comprises: gas supply device, pile; Described gas supply device utilizes the gas of compression as power, and automatic transport is in pile; Described pile comprises some sub-fuel cell modules, and each sub-fuel cell module comprises at least one super capacitor;
Described fuel cell system also comprises air intake conduit, outlet pipe; The gas of described compression is mainly oxygen; Air enters pile with oxygen after mixer mixes.
As a preferred embodiment of the present invention, described fuel cell system also comprises gas regulating system; Described gas regulating system comprises valve regulated control device, and oxygen content transducer is or/and Compressed Gas compression ratio transducer;
The data sensed in order to respond to the content of oxygen in the air and oxygen that mix in mixer, and are sent to valve regulated control device by described oxygen content transducer;
The data sensed in order to the compression ratio of induced compression oxygen, and are sent to valve regulated control device by described Compressed Gas compression ratio transducer;
Described valve regulated control device or/and the induction result of Compressed Gas compression ratio transducer regulates oxygen infusion valve, air entrainment valve door, controls the conveying ratio of compressed oxygen, air according to oxygen content transducer; Mist is pushed to pile reaction by the power that compressed oxygen produces after entering mixer.
As a preferred embodiment of the present invention, described fuel cell system also comprises humidification system, and humidification system comprises humidity exchanging container, humidity exchanges pipeline, and it is a part for air intake conduit that humidity exchanges pipeline; After described reaction, gas outlet pipe is delivered to humidity exchanging container,
The material that described humidity exchanges pipeline is only permeable airtight, makes to react rear gas and natural air carries out humidity exchange, and cannot circulate between gas.
Beneficial effect of the present invention is: the electronic pump housing of alcohol hydrogen that the present invention proposes, and hydrogen from methyl alcohol can be utilized to generate electricity as the energy of the pump housing, the pump housing can be used for the place not having alternating current.
Accompanying drawing explanation
Fig. 1 is the composition schematic diagram of the electronic pump housing of alcohol hydrogen of the present invention.
Fig. 2 is the composition schematic diagram of hydrogen production by methanol system in present system.
Fig. 3 is the structural representation of device for rapidly starting in hydrogen producer
Fig. 4 is the structural representation of hydrogen producer and heating pipe line thereof.
Fig. 5 is the composition schematic diagram of the hydrogen producer being provided with safety valve.
Fig. 6 is the schematic diagram under the another kind of state of the hydrogen producer being provided with safety valve.
Fig. 7 is the composition schematic diagram of fuel cell system in present system.
Embodiment
The preferred embodiments of the present invention are described in detail below in conjunction with accompanying drawing.
Embodiment one
Refer to Fig. 1, present invention is disclosed the electronic pump housing of a kind of alcohol hydrogen, the described electronic pump housing comprises: pump body, hydrogen production by methanol system, hydrogen gas generating system, motor; Hydrogen production by methanol system, hydrogen gas generating system, motor connect successively.Described hydrogen production by methanol system utilizes preparing hydrogen by reforming methanol-water steam, hydrogen obtains highly purified hydrogen by the membrane separation device being coated with palladium-silver, the hydrogen obtained is generated electricity by hydrogen gas generating system, and the electric energy power supply machine sent runs, thus drives this body running of pump.Preferably, the water that hydrogen gas generating system generates also is delivered to the water output port of pump body.
In the present embodiment, refer to Fig. 2, hydrogen production by methanol system is small portable hydrogen producer, comprising: liquid container 10, raw material conveying device 50, device for rapidly starting 40, device for producing hydrogen 20, membrane separation device 30, hydrogen delivery tube road 60.
As shown in Figure 3, described device for rapidly starting 40 comprises housing 41, heating arrangements 42, gasification pipe 43, and the internal diameter of gasification pipe 43 is 1 ~ 2mm, and gasification pipe 43 is wound on heating arrangements 42; Described heating arrangements can be electrically heated rod, utilizes alternating current or storage battery, dry cell.
One end of described gasification pipe 43 connects liquid container 10, is sent into by methyl alcohol in gasification pipe 43; The other end of gasification pipe 43 exports vaporized methyl alcohol, then by ignition mechanism ignition; Or the other end of gasification pipe 43 exports vaporized methyl alcohol, and the methanol temperature exported reaches self-ignition point, and methyl alcohol exports rear direct spontaneous combustion from gasification pipe 43; Described device for rapidly starting 40 provides the startup energy for device for producing hydrogen (in other words whole hydrogen producer).
Referring to Fig. 4, in order to improve the firing rate of device for producing hydrogen, being provided with heating pipe line 21 at the reformer chamber inwall of described device for producing hydrogen 20, in heating pipe line 21, be placed with catalyst (as can by heating and temperature control at 380 DEG C ~ 480 DEG C); Described device for rapidly starting 40 is reformer chamber heating by the described heating pipe line 21 of heating, can improve the efficiency of heating surface.
As shown in Figure 2, device for producing hydrogen 20 can also arrange the second starting drive 70, described second starting drive 70 comprises the second gasification pipe, and the main body of the second gasification pipe is arranged at reformer chamber, and the second gasification pipe is reformer chamber heating (can also be the heating of other unit of hydrogen producer).First gasification pipe is or/and the methyl alcohol that the second gasification pipe exports is heat the second gasification pipe, by the methanol gasifying in the second gasification pipe while reformer chamber heats.Setting-up time after the second starting drive can continue the methyl alcohol of obtained gasification, can close above-mentioned device for rapidly starting, thus reduces the dependence to extra powers such as electric energy further.
In addition, described device for producing hydrogen 20 comprises heat exchanger, vaporizer, reformer chamber; Membrane separation device is arranged in separation chamber, and separation chamber is arranged at the top of reformer chamber.Described liquid container is connected with device for producing hydrogen; Liquid first alcohol and water is stored in liquid container.
First alcohol and water in described liquid container is delivered to heat exchanger heat exchange by raw material conveying device, enters vaporizer gasification after heat exchange; Methanol vapor after gasification and steam enter reformer chamber, and reformer chamber is provided with catalyst, and reformer chamber bottom and middle portion temperature are 300 DEG C ~ 420 DEG C.The temperature on described reformer chamber top is 400 DEG C ~ 570 DEG C; Reformer chamber is connected by connecting line with separation chamber, all or part of top being arranged at reformer chamber of connecting line, and the high temperature by reformer chamber top continues the gas that heating exports from reformer chamber; Described connecting line, as the buffering between reformer chamber and separation chamber, makes the temperature of the gas exported from reformer chamber identical with the temperature of separation chamber or close.Temperature in described separation chamber is set as 350 DEG C ~ 570 DEG C; Be provided with membrane separator in separation chamber, obtain hydrogen from the aerogenesis end of membrane separator.By above-mentioned improvement, the low temperature requirements of reformer chamber catalyst can be ensured respectively, and the high temperature requirement of separation chamber, and then improve hydrogen preparation efficiency; Meanwhile, preheating method of the present invention (separation chamber being arranged at the top of reformer chamber) is very convenient.
Described catalyst comprises oxide, the oxide of Pd, the oxide of Cu, the oxide of Fe, the oxide of Zn, rare-earth oxide, the transition metal oxide of Pt; Wherein, precious metals pt content accounts for 0.6% ~ 1.8% of catalyst gross mass, Pd content accounts for 1.1% ~ 4% of catalyst gross mass, the oxide of Cu accounts for 6% ~ 12% of catalyst gross mass, the oxide of Fe accounts for 3% ~ 8% of catalyst gross mass, the oxide of Zn accounts for 8% ~ 20% of catalyst gross mass, and rare-earth oxide accounts for 6% ~ 40% of catalyst gross mass, and all the other are transition metal oxide;
Or described catalyst is copper-based catalysts, comprise material and mass fraction is: the CuO of 3-17 part, the ZrO of the ZnO of 3-18 part, 0.5-3 part, the Al of 55-80 part 2o 3, the CeO of 1-3 part 2, the La of 1-3 part 2o 3.
In addition, described raw material conveying device provides power, by the feedstock transportation in liquid container to device for producing hydrogen; Described raw material conveying device provides the pressure of 0.15 ~ 5MPa to raw material, and the hydrogen that device for producing hydrogen is obtained has enough pressure.The hydrogen that described device for producing hydrogen obtains is delivered to membrane separation device and is separated, 0.7MPa (temperature in membrane separation device is set as 300 ~ 500 DEG C, and pressure is less than 5Mpa differential pressure and is no more than 15 kilograms) is more than or equal to for separating of the difference of pressure inside and outside the membrane separation device of hydrogen.By this improvement, the hydrogen that device for producing hydrogen is obtained has enough pressure, can improve the purity of hydrogen production efficiency and obtained hydrogen.
After described hydrogen producer starts, hydrogen producer provides the energy needed for operation by the hydrogen that device for producing hydrogen obtains; Now, device for rapidly starting can be closed.The hydrogen partial obtained due to device for producing hydrogen or/and residual air maintains hydrogen producer operation by burning, thus can reduce the dependence to extra power, and adaptive ability is strong.
In addition, refer to Fig. 5, Fig. 6, described hydrogen delivery tube road 60 is provided with spring safety valve 61, and spring safety valve 61 comprises valve body, spring mechanism, end of upspringing; Described raw material conveying device 50 comprises delivery pump, and the switch-linear hybrid (certain raw material conveying device 50 also can be other power set) of end near delivery pump of upspringing, can disconnect the switch of raw material conveying device when end of upspringing is upspring.By arranging mechanical safety valve on hydrogen delivery tube road, when air pressure reaches set point, mechanical safety valve is opened, and can control raw material conveying device stopping transferring raw material.Thus the fail safe of equipment operation can be improved, prevent hydrogen leak and blast.
Particularly, in the present embodiment, the switch of described delivery pump comprises contact-segment 62 and three ports, and three ports are respectively the first port 63, second port 64, the 3rd port 65.One end of described contact-segment 62 is rotatably arranged at the first port 63, first port 63 and connects delivery pump; The other end of contact-segment 62 can contact the second port 64 or the 3rd port 65.
Described second port 64 connects power supply, when the first port 63 connects the second port 64, can control delivery pump work.Described 3rd port 65 connects alarm transmitting device, when the first port connects the 3rd port 65, can control conveying air pump inoperative, alarm transmitting device sends warning message (mode as by note) to corresponding server or client simultaneously, can notify corresponding personnel.
Described hydrogen gas generation device connects hydrogen producer, and the Partial DC electricity sent is delivered to hydrogen producer; Hydrogen producer drives electromagnetic heater to be reformer chamber, separation chamber's heating by oneself obtained direct current; Meanwhile, also the direct current sent is delivered to the deep sea water extracting device of system, seawater purifying plant, oxygen delivery devices, water generation equipment, runs for these equipment, go back hydrogen supply gas electric generating apparatus self-operating simultaneously.
Described hydrogen producer comprises electromagnetic heater; Electromagnetic heater comprises the reformation cylinder body forming reformer chamber, the separation cylinder body forming separation chamber, be arranged at the first heater coil outside reformation cylinder body, the second heater coil that splitter cylinder is external, reformation cylinder body, temperature sensor, the pressure sensor be separated in cylinder body, and electromagnetic controller; Data Control first heater coil that electromagnetic controller senses according to temperature sensor, pressure sensor, the electric current of the second heater coil, can make reformer chamber, separation chamber reaches design temperature instantaneously.
Described hydrogen producer also comprises electric energy estimation block, hydrogen prepares detection module, power storage module; Whether described electric energy estimation block can meet reformation in order to the electric energy estimated hydrogen gas generation device and send in real time, the electric energy of needs consumption when being separated; If met, then close device for rapidly starting.
Whether hydrogen is prepared detection module and is used for detecting the hydrogen prepared in real time of hydrogen producer and stablizes; If hydrogen prepared by hydrogen producer is unstable, then controls device for rapidly starting and again start, and the electric energy part obtained is stored in power storage module, use when electric energy is not enough to the consumption providing hydrogen producer.
Refer to Fig. 7, in the present embodiment, described hydrogen gas generation device 200 is fuel cell system, and fuel cell system comprises: gas supply device, pile 201; Described gas supply device utilizes the gas of compression as power, and automatic transport is in pile 201.
In the present embodiment, gas supply device is Compressed Gas feedway 202, and described Compressed Gas enters pile 201 after being delivered to a mixer 203, and one end of mixer 203 connects air; Natural air in the reaction of setting ratio inspiration pile, is regulated oxygen content by the power that Compressed Gas produces after entering mixer 203.
Described fuel cell system also comprises air intake conduit, outlet pipe, and air intake conduit, outlet pipe are all through humidification system 204.The gas of described compression is mainly oxygen (also can be air); Natural air and compressed oxygen enter pile 201 after mixer mixes.
Described fuel cell system also comprises gas regulating system, and gas regulating system is arranged in mixer 203; Described gas regulating system comprises valve regulated control device, and oxygen content transducer is or/and Compressed Gas compression ratio transducer.
The data sensed in order to respond to the content of oxygen in the air and oxygen that mix in mixer, and are sent to valve regulated control device by described oxygen content transducer.
The data sensed in order to the compression ratio of induced compression oxygen, and are sent to valve regulated control device by described Compressed Gas compression ratio transducer.
Described valve regulated control device or/and the induction result of Compressed Gas compression ratio transducer regulates oxygen infusion valve, air entrainment valve door, controls the conveying ratio (if natural air ratio can be 0-70%) of compressed oxygen, natural air according to oxygen content transducer; Mist is pushed to pile reaction by the power that compressed oxygen produces after entering mixer, utilizes natural air to do dilution decompression.
Described humidification system 204 comprises humidity exchanging container, humidity exchanges pipeline, and it is a part for air intake conduit that humidity exchanges pipeline; After described reaction, gas outlet pipe is delivered to humidity exchanging container.
The material that described humidity exchanges pipeline is only permeable airtight, makes to react rear gas and natural air carries out humidity exchange, and cannot circulate between gas.Humidity exchanges pipeline spiral in humidity exchanging container and arranges, and fully can carry out humidity exchange.
Embodiment two
The difference of the present embodiment and embodiment one is, in the present embodiment, the electronic pump housing of described alcohol hydrogen also comprises air pressure adjustment subsystem, Collection utilization subsystem.
Described air pressure adjustment subsystem comprises microprocessor, gas pressure sensor, valve positioner, air outlet valve, outlet pipe; Described gas pressure sensor is arranged in transfer conduit, in order to respond to the barometric information in transfer conduit, and the barometric information of induction is sent to microprocessor; This barometric information received from gas pressure sensor and setting threshold interval are compared by described microprocessor; When the pressure data received is higher than the maximum in setting threshold interval, Microprocessor S3C44B0X valve positioner opens air outlet valve setting-up time, air pressure in transfer conduit is made to be in setting range, one end of outlet pipe connects air outlet valve simultaneously, the other end connects described hydrogen manufacturing subsystem, and the firing equipment that needs being hydrogen manufacturing subsystem by burning heats; When the pressure data received is lower than the minimum value in setting threshold interval, hydrogen manufacturing subsystem described in Microprocessor S3C44B0X accelerates the transporting velocity of raw material.
Described Collection utilization subsystem connects the Vent passageway of hydrogen gas generating system, hydrogen, oxygen, water is collected respectively from the gas of discharging, utilize collect hydrogen, oxygen for hydrogen manufacturing subsystem or/and hydrogen gas generating system, the water collected as the raw material of hydrogen manufacturing subsystem, thus recycles.Described Collection utilization subsystem comprises hydrogen/oxygen separator, hydrogen separator, hydrogen check-valves, oxygen separator, oxygen check valve, by hydrogen and oxygen separation, is then separated with water by hydrogen respectively, oxygen is separated with water.
Embodiment three
Present invention is disclosed the electronic pump housing of a kind of alcohol hydrogen, the described electronic pump housing comprises: pump body, hydrogen production by methanol system, hydrogen gas generating system, motor; Hydrogen production by methanol system, hydrogen gas generating system, motor connect successively.Described hydrogen production by methanol system utilizes preparing hydrogen by reforming methanol-water steam, hydrogen obtains highly purified hydrogen by the membrane separation device being coated with palladium-silver, the hydrogen obtained is generated electricity by hydrogen gas generating system, and the electric energy power supply machine sent runs, thus drives this body running of pump.
In sum, the electronic pump housing of alcohol hydrogen that the present invention proposes, can utilize hydrogen from methyl alcohol to generate electricity as the energy of the pump housing, the pump housing can be used for the place not having alternating current.
Here description of the invention and application is illustrative, not wants by scope restriction of the present invention in the above-described embodiments.Distortion and the change of embodiment disclosed are here possible, are known for the replacement of embodiment those those of ordinary skill in the art and the various parts of equivalence.Those skilled in the art are noted that when not departing from spirit of the present invention or substantive characteristics, the present invention can in other forms, structure, layout, ratio, and to realize with other assembly, material and parts.When not departing from the scope of the invention and spirit, can other distortion be carried out here to disclosed embodiment and change.

Claims (10)

1. the electronic pump housing of alcohol hydrogen, is characterized in that, the described electronic pump housing comprises: pump body, hydrogen production by methanol system, hydrogen gas generating system, motor, and hydrogen production by methanol system, hydrogen gas generating system, motor, pump body connect successively; Pump body comprises motor unit, pump unit, housing unit, cap unit; Motor unit comprises stator, rotor core and axle; Pump unit comprises inner rotator and external rotor, and inner rotator is attached to axle and inner rotator is formed with outer projection, and external rotor to be arranged on outside inner rotator and to have internal protrusion, and internal protrusion is formed as engaging with outer projection; Housing unit comprises motor shell and pump case, and pump case is connected to motor shell and is formed with pump accommodation section in pump case, is inserted with pump unit in pump accommodation section;
Described hydrogen production by methanol system comprises hydrogen manufacturing subsystem, air pressure adjustment subsystem, Collection utilization subsystem, and hydrogen manufacturing subsystem, air pressure adjustment subsystem, hydrogen gas generating system, Collection utilization subsystem connect successively;
Described hydrogen manufacturing subsystem utilizes methanol-water to prepare hydrogen, and described hydrogen manufacturing subsystem comprises solid hydrogen reservoir vessel, liquid container, raw material conveying device, device for rapidly starting, hydrogen producer, membrane separation device;
Described hydrogen producer comprises heat exchanger, vaporizer, reformer chamber; Membrane separation device is arranged in separation chamber, and separation chamber is arranged at the inside of reformer chamber; Described solid hydrogen reservoir vessel, liquid container are connected with hydrogen producer respectively; Liquid first alcohol and water is stored in liquid container;
Described device for rapidly starting provides the startup energy for hydrogen producer; Described device for rapidly starting comprises the first starting drive, the second starting drive; Described first starting drive comprises the first heating arrangements, the first gasification pipe, and the internal diameter of the first gasification pipe is 1 ~ 2mm, and the first gasification pipe is closely wound on the first heating arrangements; One end of described first gasification pipe connects liquid container, sends in the first gasification pipe by raw material conveying device by methyl alcohol; The other end of the first gasification pipe exports vaporized methyl alcohol, then by ignition mechanism ignition; Or the other end of the first gasification pipe exports vaporized methyl alcohol, and the methanol temperature exported reaches self-ignition point, directly spontaneous combustion after methyl alcohol exports from the first gasification pipe; Described second starting drive comprises the second gasification pipe, the main body of the second gasification pipe is arranged at described reformer chamber, first gasification pipe is or/and the methyl alcohol that the second gasification pipe exports is heat the second gasification pipe, by the methanol gasifying in the second gasification pipe while reformer chamber heats; Described reformer chamber inwall is provided with heating pipe line, is placed with catalyst in heating pipe line; Described device for rapidly starting is reformer chamber heating by the described heating pipe line of heating; After described hydrogen generating system starts, hydrogen generating system provides the energy needed for operation by the hydrogen that hydrogen producer obtains;
The initial start energy of described device for rapidly starting is that some solar energy starts module, and solar energy starts module and comprises the solar panel, solar energy-electric energy change-over circuit, the solar cell that connect successively; Solar energy starts module provides electric energy for the first heating arrangements; Or the initial start energy of described device for rapidly starting is manual generator, manual generator by the power storage that sends in battery;
Described catalyst comprises oxide, the oxide of Pd, the oxide of Cu, the oxide of Fe, the oxide of Zn, rare-earth oxide, the transition metal oxide of Pt; Wherein, precious metals pt content accounts for 0.6% ~ 1.8% of catalyst gross mass, Pd content accounts for 1.1% ~ 4% of catalyst gross mass, the oxide of Cu accounts for 6% ~ 12% of catalyst gross mass, the oxide of Fe accounts for 3% ~ 8% of catalyst gross mass, the oxide of Zn accounts for 8% ~ 20% of catalyst gross mass, and rare-earth oxide accounts for 6% ~ 40% of catalyst gross mass, and all the other are transition metal oxide;
Or described catalyst is copper-based catalysts, comprise material and mass fraction is: the CuO of 3-17 part, the ZrO of the ZnO of 3-18 part, 0.5-3 part, the Al of 55-80 part 2o 3, the CeO of 1-3 part 2, the La of 1-3 part 2o 3;
Store solid hydrogen in described solid hydrogen reservoir vessel, when hydrogen generating system starts, by gasification module, solid hydrogen is converted to gaseous hydrogen, gaseous hydrogen passes through combustion heat release, for hydrogen producer provides startup heat energy, as the startup energy of hydrogen producer;
First alcohol and water in described liquid container is delivered to heat exchanger heat exchange by raw material conveying device, enters vaporizer gasification after heat exchange; Methanol vapor after gasification and steam enter reformer chamber, and reformer chamber is provided with catalyst, and reformer chamber bottom and middle portion temperature are 300 DEG C ~ 420 DEG C; The temperature on described reformer chamber top is 400 DEG C ~ 570 DEG C; Reformer chamber is connected by connecting line with separation chamber, all or part of top being arranged at reformer chamber of connecting line, and the high temperature by reformer chamber top continues the gas that heating exports from reformer chamber; Described connecting line, as the buffering between reformer chamber and separation chamber, makes the temperature of the gas exported from reformer chamber identical with the temperature of separation chamber or close; Temperature in described separation chamber is set as 350 DEG C ~ 570 DEG C; Be provided with membrane separator in separation chamber, obtain hydrogen from the aerogenesis end of membrane separator;
Described raw material conveying device provides power, by the feedstock transportation in liquid container to hydrogen producer; Described raw material conveying device provides the pressure of 0.15 ~ 5MPa to raw material, and the hydrogen that hydrogen producer is obtained has enough pressure;
After described hydrogen producer starts hydrogen manufacturing, the hydrogen partial that hydrogen producer is obtained is or/and residual air is run by burning maintenance hydrogen producer;
The hydrogen that described hydrogen producer obtains is delivered to membrane separation device and is separated, and is more than or equal to 0.7MPa for separating of the difference of pressure inside and outside the membrane separation device of hydrogen; Described membrane separation device is the membrane separation device at porous ceramic surface Vacuum Deposition palladium-silver, and film plating layer is palladium-silver, and the mass percent palladium of palladium-silver accounts for 75% ~ 78%, and silver accounts for 22% ~ 25%;
Obtained hydrogen is passed through transfer conduit real-time Transmission to hydrogen gas generating system by described hydrogen manufacturing subsystem; Described transfer conduit is provided with air pressure adjustment subsystem, for adjusting the air pressure in transfer conduit; The hydrogen gas generation that described hydrogen gas generating system utilizes hydrogen manufacturing subsystem obtained;
Described air pressure adjustment subsystem comprises microprocessor, gas pressure sensor, valve positioner, air outlet valve, outlet pipe; Described gas pressure sensor is arranged in transfer conduit, in order to respond to the barometric information in transfer conduit, and the barometric information of induction is sent to microprocessor; This barometric information received from gas pressure sensor and setting threshold interval are compared by described microprocessor; When the pressure data received is higher than the maximum in setting threshold interval, Microprocessor S3C44B0X valve positioner opens air outlet valve setting-up time, air pressure in transfer conduit is made to be in setting range, one end of outlet pipe connects air outlet valve simultaneously, the other end connects described hydrogen manufacturing subsystem, and the firing equipment that needs being hydrogen manufacturing subsystem by burning heats; When the pressure data received is lower than the minimum value in setting threshold interval, hydrogen manufacturing subsystem described in Microprocessor S3C44B0X accelerates the transporting velocity of raw material;
Described Collection utilization subsystem connects the Vent passageway of hydrogen gas generating system, hydrogen, oxygen, water is collected respectively from the gas of discharging, utilize collect hydrogen, oxygen for hydrogen manufacturing subsystem or/and hydrogen gas generating system, the water collected as the raw material of hydrogen manufacturing subsystem, thus recycles;
Described Collection utilization subsystem comprises hydrogen/oxygen separator, hydrogen separator, hydrogen check-valves, oxygen separator, oxygen check valve, by hydrogen and oxygen separation, is then separated with water by hydrogen respectively, oxygen is separated with water;
Described hydrogen producer also comprises electric energy estimation block, hydrogen prepares detection module, power storage module; Whether described electric energy estimation block can meet reformation in order to the electric energy estimated hydrogen gas generation device and send in real time, the electric energy of needs consumption when being separated; If met, then close device for rapidly starting;
Whether hydrogen is prepared detection module and is used for detecting the hydrogen prepared in real time of hydrogen producer and stablizes; If hydrogen prepared by hydrogen producer is unstable, then controls device for rapidly starting and again start, and the electric energy part obtained is stored in power storage module, use when electric energy is not enough to the consumption providing hydrogen producer;
Described hydrogen gas generating system is fuel cell system, and fuel cell system comprises: gas supply device, pile; Described gas supply device utilizes the gas of compression as power, and automatic transport is in pile; Described pile comprises some sub-fuel cell modules, and each sub-fuel cell module comprises at least one super capacitor;
Described fuel cell system also comprises air intake conduit, outlet pipe; The gas of described compression is mainly oxygen; Air enters pile with oxygen after mixer mixes;
Described fuel cell system also comprises gas regulating system; Described gas regulating system comprises valve regulated control device, and oxygen content transducer is or/and Compressed Gas compression ratio transducer;
The data sensed in order to respond to the content of oxygen in the air and oxygen that mix in mixer, and are sent to valve regulated control device by described oxygen content transducer;
The data sensed in order to the compression ratio of induced compression oxygen, and are sent to valve regulated control device by described Compressed Gas compression ratio transducer;
Described valve regulated control device or/and the induction result of Compressed Gas compression ratio transducer regulates oxygen infusion valve, air entrainment valve door, controls the conveying ratio of compressed oxygen, air according to oxygen content transducer; Mist is pushed to pile reaction by the power that compressed oxygen produces after entering mixer;
Described fuel cell system also comprises humidification system, and humidification system comprises humidity exchanging container, humidity exchanges pipeline, and it is a part for air intake conduit that humidity exchanges pipeline; After described reaction, gas outlet pipe is delivered to humidity exchanging container,
The material that described humidity exchanges pipeline is only permeable airtight, makes to react rear gas and natural air carries out humidity exchange, and cannot circulate between gas.
2. the electronic pump housing of alcohol hydrogen, is characterized in that, the described electronic pump housing comprises: pump body, hydrogen production by methanol system, hydrogen gas generating system, motor, and hydrogen production by methanol system, hydrogen gas generating system, motor, pump body connect successively;
Described hydrogen production by methanol system utilizes preparing hydrogen by reforming methanol-water steam, hydrogen obtains highly purified hydrogen by the membrane separation device being coated with palladium-silver, the hydrogen obtained is generated electricity by hydrogen gas generating system, and the electric energy power supply machine sent runs, thus drives this body running of pump.
3. the electronic pump housing of alcohol hydrogen according to claim 2, is characterized in that:
Described hydrogen production by methanol system comprises hydrogen manufacturing subsystem, air pressure adjustment subsystem, Collection utilization subsystem, and hydrogen manufacturing subsystem, air pressure adjustment subsystem, hydrogen gas generating system, Collection utilization subsystem connect successively;
Described hydrogen manufacturing subsystem utilizes methanol-water to prepare hydrogen, and described hydrogen manufacturing subsystem comprises solid hydrogen reservoir vessel, liquid container, raw material conveying device, device for rapidly starting, hydrogen producer, membrane separation device;
Described hydrogen producer comprises heat exchanger, vaporizer, reformer chamber; Membrane separation device is arranged in separation chamber, and separation chamber is arranged at the inside of reformer chamber; Described solid hydrogen reservoir vessel, liquid container are connected with hydrogen producer respectively; Liquid first alcohol and water is stored in liquid container;
Described device for rapidly starting provides the startup energy for hydrogen producer; Described device for rapidly starting comprises the first starting drive, the second starting drive; Described first starting drive comprises the first heating arrangements, the first gasification pipe, and the internal diameter of the first gasification pipe is 1 ~ 2mm, and the first gasification pipe is closely wound on the first heating arrangements; One end of described first gasification pipe connects liquid container, sends in the first gasification pipe by raw material conveying device by methyl alcohol; The other end of the first gasification pipe exports vaporized methyl alcohol, then by ignition mechanism ignition; Or the other end of the first gasification pipe exports vaporized methyl alcohol, and the methanol temperature exported reaches self-ignition point, directly spontaneous combustion after methyl alcohol exports from the first gasification pipe; Described second starting drive comprises the second gasification pipe, the main body of the second gasification pipe is arranged at described reformer chamber, first gasification pipe is or/and the methyl alcohol that the second gasification pipe exports is heat the second gasification pipe, by the methanol gasifying in the second gasification pipe while reformer chamber heats; Described reformer chamber inwall is provided with heating pipe line, is placed with catalyst in heating pipe line; Described device for rapidly starting is reformer chamber heating by the described heating pipe line of heating; After described hydrogen generating system starts, hydrogen generating system provides the energy needed for operation by the hydrogen that hydrogen producer obtains;
Store solid hydrogen in described solid hydrogen reservoir vessel, when hydrogen generating system starts, by gasification module, solid hydrogen is converted to gaseous hydrogen, gaseous hydrogen passes through combustion heat release, for hydrogen producer provides startup heat energy, as the startup energy of hydrogen producer;
First alcohol and water in described liquid container is delivered to heat exchanger heat exchange by raw material conveying device, enters vaporizer gasification after heat exchange; Methanol vapor after gasification and steam enter reformer chamber, and reformer chamber is provided with catalyst, and reformer chamber bottom and middle portion temperature are 300 DEG C ~ 420 DEG C; The temperature on described reformer chamber top is 400 DEG C ~ 570 DEG C; Reformer chamber is connected by connecting line with separation chamber, all or part of top being arranged at reformer chamber of connecting line, and the high temperature by reformer chamber top continues the gas that heating exports from reformer chamber; Described connecting line, as the buffering between reformer chamber and separation chamber, makes the temperature of the gas exported from reformer chamber identical with the temperature of separation chamber or close; Temperature in described separation chamber is set as 350 DEG C ~ 570 DEG C; Be provided with membrane separator in separation chamber, obtain hydrogen from the aerogenesis end of membrane separator;
Described raw material conveying device provides power, by the feedstock transportation in liquid container to hydrogen producer; Described raw material conveying device provides the pressure of 0.15 ~ 5MPa to raw material, and the hydrogen that hydrogen producer is obtained has enough pressure;
After described hydrogen producer starts hydrogen manufacturing, the hydrogen partial that hydrogen producer is obtained is or/and residual air is run by burning maintenance hydrogen producer;
The hydrogen that described hydrogen producer obtains is delivered to membrane separation device and is separated, and is more than or equal to 0.7MPa for separating of the difference of pressure inside and outside the membrane separation device of hydrogen; Described membrane separation device is the membrane separation device at porous ceramic surface Vacuum Deposition palladium-silver, and film plating layer is palladium-silver, and the mass percent palladium of palladium-silver accounts for 75% ~ 78%, and silver accounts for 22% ~ 25%;
Obtained hydrogen is passed through transfer conduit real-time Transmission to hydrogen gas generating system by described hydrogen manufacturing subsystem; Described transfer conduit is provided with air pressure adjustment subsystem, for adjusting the air pressure in transfer conduit; The hydrogen gas generation that described hydrogen gas generating system utilizes hydrogen manufacturing subsystem obtained;
Described air pressure adjustment subsystem comprises microprocessor, gas pressure sensor, valve positioner, air outlet valve, outlet pipe; Described gas pressure sensor is arranged in transfer conduit, in order to respond to the barometric information in transfer conduit, and the barometric information of induction is sent to microprocessor; This barometric information received from gas pressure sensor and setting threshold interval are compared by described microprocessor; When the pressure data received is higher than the maximum in setting threshold interval, Microprocessor S3C44B0X valve positioner opens air outlet valve setting-up time, air pressure in transfer conduit is made to be in setting range, one end of outlet pipe connects air outlet valve simultaneously, the other end connects described hydrogen manufacturing subsystem, and the firing equipment that needs being hydrogen manufacturing subsystem by burning heats; When the pressure data received is lower than the minimum value in setting threshold interval, hydrogen manufacturing subsystem described in Microprocessor S3C44B0X accelerates the transporting velocity of raw material;
Described Collection utilization subsystem connects the Vent passageway of hydrogen gas generating system, hydrogen, oxygen, water is collected respectively from the gas of discharging, utilize collect hydrogen, oxygen for hydrogen manufacturing subsystem or/and hydrogen gas generating system, the water collected as the raw material of hydrogen manufacturing subsystem, thus recycles;
Described Collection utilization subsystem comprises hydrogen/oxygen separator, hydrogen separator, hydrogen check-valves, oxygen separator, oxygen check valve, by hydrogen and oxygen separation, is then separated with water by hydrogen respectively, oxygen is separated with water.
4. the electronic pump housing of alcohol hydrogen according to claim 3, is characterized in that:
The initial start energy of described device for rapidly starting is that some solar energy starts module, and solar energy starts module and comprises the solar panel, solar energy-electric energy change-over circuit, the solar cell that connect successively; Solar energy starts module provides electric energy for the first heating arrangements; Or the initial start energy of described device for rapidly starting is manual generator, manual generator by the power storage that sends in battery.
5. the electronic pump housing of alcohol hydrogen according to claim 3, is characterized in that:
Described catalyst comprises oxide, the oxide of Pd, the oxide of Cu, the oxide of Fe, the oxide of Zn, rare-earth oxide, the transition metal oxide of Pt;
Wherein, precious metals pt content accounts for 0.6% ~ 1.8% of catalyst gross mass, Pd content accounts for 1.1% ~ 4% of catalyst gross mass, the oxide of Cu accounts for 6% ~ 12% of catalyst gross mass, the oxide of Fe accounts for 3% ~ 8% of catalyst gross mass, the oxide of Zn accounts for 8% ~ 20% of catalyst gross mass, and rare-earth oxide accounts for 6% ~ 40% of catalyst gross mass, and all the other are transition metal oxide;
Or described catalyst is copper-based catalysts, comprise material and mass fraction is: the CuO of 2-20 part, the ZrO of the ZnO of 2-20 part, 0.1-5 part, the Al of 45-95 part 2o 3, the CeO of 0-5 part 2, the La of 0-5 part 2o 3.
6. the electronic pump housing of alcohol hydrogen according to claim 2, is characterized in that:
Described pump body comprises motor unit, pump unit, housing unit, cap unit; Motor unit comprises stator, rotor core and axle; Pump unit comprises inner rotator and external rotor, and inner rotator is attached to axle and inner rotator is formed with outer projection, and external rotor to be arranged on outside inner rotator and to have internal protrusion, and internal protrusion is formed as engaging with outer projection; Housing unit comprises motor shell and pump case, and pump case is connected to motor shell and is formed with pump accommodation section in pump case, is inserted with pump unit in pump accommodation section.
7. the electronic pump housing of alcohol hydrogen according to claim 2, is characterized in that:
Described hydrogen gas generating system comprises fuel cell, and fuel cell comprises some sub-fuel cell modules, and each sub-fuel cell module comprises at least one super capacitor.
8. the electronic pump housing of alcohol hydrogen according to claim 2, is characterized in that:
Described hydrogen gas generating system is fuel cell system, and fuel cell system comprises: gas supply device, pile; Described gas supply device utilizes the gas of compression as power, and automatic transport is in pile; Described pile comprises some sub-fuel cell modules, and each sub-fuel cell module comprises at least one super capacitor;
Described fuel cell system also comprises air intake conduit, outlet pipe; The gas of described compression is mainly oxygen; Air enters pile with oxygen after mixer mixes.
9. the electronic pump housing of alcohol hydrogen according to claim 8, is characterized in that:
Described fuel cell system also comprises gas regulating system; Described gas regulating system comprises valve regulated control device, and oxygen content transducer is or/and Compressed Gas compression ratio transducer;
The data sensed in order to respond to the content of oxygen in the air and oxygen that mix in mixer, and are sent to valve regulated control device by described oxygen content transducer;
The data sensed in order to the compression ratio of induced compression oxygen, and are sent to valve regulated control device by described Compressed Gas compression ratio transducer;
Described valve regulated control device or/and the induction result of Compressed Gas compression ratio transducer regulates oxygen infusion valve, air entrainment valve door, controls the conveying ratio of compressed oxygen, air according to oxygen content transducer; Mist is pushed to pile reaction by the power that compressed oxygen produces after entering mixer.
10. the electronic pump housing of alcohol hydrogen according to claim 2, is characterized in that:
Described fuel cell system also comprises humidification system, and humidification system comprises humidity exchanging container, humidity exchanges pipeline, and it is a part for air intake conduit that humidity exchanges pipeline; After described reaction, gas outlet pipe is delivered to humidity exchanging container;
The material that described humidity exchanges pipeline is only permeable airtight, makes to react rear gas and natural air carries out humidity exchange, and cannot circulate between gas.
CN201510658423.7A 2015-10-12 2015-10-12 Alcohol-to-hydrogen electric pump Pending CN105186022A (en)

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Citations (5)

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