CN202026127U - Integrated fuel battery backup power supply system for on-site hydrogen production - Google Patents
Integrated fuel battery backup power supply system for on-site hydrogen production Download PDFInfo
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- CN202026127U CN202026127U CN201120063208XU CN201120063208U CN202026127U CN 202026127 U CN202026127 U CN 202026127U CN 201120063208X U CN201120063208X U CN 201120063208XU CN 201120063208 U CN201120063208 U CN 201120063208U CN 202026127 U CN202026127 U CN 202026127U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B10/00—Integration of renewable energy sources in buildings
- Y02B10/70—Hybrid systems, e.g. uninterruptible or back-up power supplies integrating renewable energies
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B70/00—Technologies for an efficient end-user side electric power management and consumption
- Y02B70/30—Systems integrating technologies related to power network operation and communication or information technologies for improving the carbon footprint of the management of residential or tertiary loads, i.e. smart grids as climate change mitigation technology in the buildings sector, including also the last stages of power distribution and the control, monitoring or operating management systems at local level
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B90/00—Enabling technologies or technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02B90/10—Applications of fuel cells in buildings
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/70—Wind energy
- Y02E10/76—Power conversion electric or electronic aspects
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y04—INFORMATION OR COMMUNICATION TECHNOLOGIES HAVING AN IMPACT ON OTHER TECHNOLOGY AREAS
- Y04S—SYSTEMS INTEGRATING TECHNOLOGIES RELATED TO POWER NETWORK OPERATION, COMMUNICATION OR INFORMATION TECHNOLOGIES FOR IMPROVING THE ELECTRICAL POWER GENERATION, TRANSMISSION, DISTRIBUTION, MANAGEMENT OR USAGE, i.e. SMART GRIDS
- Y04S20/00—Management or operation of end-user stationary applications or the last stages of power distribution; Controlling, monitoring or operating thereof
- Y04S20/20—End-user application control systems
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Abstract
The utility model provides an integrated fuel battery backup power supply system for on-site hydrogen production. The system includes an electrolytic bath, a hydrogen compressor, a hydrogen storage battle, a fuel battery and a plumbic acid battery. The electrolytic bath is connected with the hydrogen compressor which matches with the hydrogen production speed of the electrolytic bath. The hydrogen compressor is connected with the hydrogen storage battle and the fuel battery in turn. The fuel battery and the plumbic acid battery are connected in parallel, and then are connected with a load. Compared with the prior art, the integrated fuel battery backup power supply system for on-site hydrogen production has the advantages of practicality, simple craft, high stability, and the like.
Description
Technical field
The utility model relates to stand-by power supply, relates in particular to a kind of on-the-spot hydrogen manufacturing integrated fuel battery standby power system.
Background technology
Fuel cell can be used in bank as stand-by power supply, hospital, the airport, business premises etc. substitute lead-acid battery and the diesel engine generator widely applied at present, have environment friendly and pollution-free, noiselessness, light, be convenient to many advantages such as maintenance.
Stand-by power supply is as improving constantly along with people's quality of the life, the fast development of society's suitability for industrialized production, modern society and economy have reached indispensable degree to the dependence of electric power, and electric power has become the master switch of society and economical operation, do not had electricity, all just are absorbed in comprehensive paralysis rapidly.
On communication base station, in case grid power blackout, stand-by power supply normally plays the uninterrupted power supply important function for ensureing communication.
At present, good more important occasion, in communication, stand-by power supply mainly adopts lead accumulator and the combined mode of diesel generating set to carry out, the present situation of this stand-by power supply is increasing with the contradiction between the demand of current stand-by power supply, mainly show: a. lead accumulator finite capacity, it is 10 hours that the standby time generally is no more than, and does not satisfy great emergent dangerous situation demand at all.B. and lead accumulator exist weight big, in the life-span short (about general 3-5), pollute big, streaking one, life-span be cannot say for sure shortcoming .c. such as card in order to prolong the generating standby time, be equipped with a large amount of diesel generation oil locomotives, generally is that the base station about 10-20 is equipped with an oily locomotive of generating.Most of the time, oily locomotive seal up for safekeeping need not, often need not be bad to oily locomotive, need often to safeguard that regular maintenance is more frequent that workload is big.When running into large-area power-cuts or great dangerous situation, oily locomotive is not enough.
Fuel cell is as a kind of generating equipment of energy-conserving and environment-protective, and volume is little, and is in light weight, noiselessness, low price, safeguard low, but characteristics such as continuous operation are suitable for use in the stand-by power supply field very much.Compare with diesel engine generator with lead-acid battery, have zero and pollute, environmental protection, characteristics such as integrated cost is cheaper.
Fuel cell can provide the non-firm power of ultra-long time as stand-by power supply, and increases with low costly, and this is the advantage place that fuel cell has cost competitiveness very much.
Need hydrogen during fuel cell operation, fuel cell wants for a long time operation continuously that a large amount of hydrogen of deposit must be arranged at the operation scene.The mode that obtains standby hydrogen has a variety of, and for example the mode of dispensing is dispensed into on-the-spot mode of installing then with hydrogen from hydrogen manufacturing factory.Because hydrogen manufacturing factory quantity is less relatively, the use hydrogen of Fen Saning especially relatively is not occasion very easily in traffic, and it is very uneconomical that this mode becomes, and its commercial operation difficulty is bigger, is difficult to find appropriate provider either.So this scheme has directly influenced the commercialization process of hydrogen reserve battery.In addition, hydrogen can in situ preparation, the mode of storage.The mode of on-the-spot hydrogen manufacturing is many.Such as preparing hydrogen by reforming methanol, methane reforming hydrogen manufacturing.This mode will obtain the high hydrogen system complexity of comparison purity, and the start-up time of generation hydrogen is long, and system complex is not for very suitable as the system of this response of will powering fast of stand-by power supply.The mode that also has a kind of on-the-spot hydrogen manufacturing in addition is the mode of brine electrolysis, and this mode need expend certain electric power.Reserve battery (lead-acid battery) generally is connected in parallel in the electric power system as auxiliary power, generally, has civil power in the system, so reserve battery does not provide electric power to load.When civil power cuts off the power supply, be connected in parallel on reserve battery in the system and start working and provide electric power for power consumption equipment.When civil power came, civil power provided reserve battery (lead-acid battery) charging power on the one hand by behind the AC/DC, provides electric power to load on the one hand.
If on-the-spot electrolytic hydrogen production is adopted in the hydrogen of fuel cell source, will consume certain electric weight like this.Will consume excessive electric power if the electrolytic cell outfit is unreasonable, so we need also further be equipped with AC/DC or overall electric distribution power consumption to original system.This scheme of electric power for original whole system can change bigger, drops into greatlyyer, in conditional this scheme of occasion of some power supply ability difficulty is passed through.System power dissipation can most of (even all) substitute lead-acid battery for electric power supply system of fuel cell, can reduce the AC/DC Switching Power Supply power in the original system behind the original system installation electric power supply system of fuel cell.If our reasonable disposition electrolytic cell, with being not more than of being equipped with of electrolytic cell or near in original whole system to the power of lead-acid battery charging, the whole system distribution will no longer increase power consumption, need not increase original distribution configuration, need not increase original electrical network burden, realize of the butt joint of a kind of gapless with original scene.Though hydrogen energy conversion efficiency in the whole process of preparation generating is lower than lead-acid battery, but fuel cell is as a non-firm power system, the running time of non-firm power is shorter, therefore the consumption rate of hydrogen is less, under most of state, hydrogen fuel cell is different from lead-acid battery, do not need floating current, do not need standby energy consumption, generally speaking, in whole hydrogen production-storage-power generation process, with needing the floating charge lead-acid battery to compare for a long time, energy consumption does not increase generally speaking, just can not improve the energy consumption of whole system.But fuel cell is as a kind of electricity generation system that non-firm power can be provided for a long time, and its marginal capacity is very strong.
The utility model content
The purpose of this utility model is exactly in order to provide the on-the-spot hydrogen manufacturing integrated fuel battery standby power system that a kind of cost is low, have industrialization prospect.
In order to achieve the above object, the utility model has adopted following technical scheme: a kind of on-the-spot hydrogen manufacturing integrated fuel battery standby power system, it is characterized in that, comprise electrolytic cell, hydrogen gas compressor, storage hydrogen bottle, fuel cell and lead-acid battery, described electrolytic cell connects the hydrogen gas compressor that is complementary with its product hydrogen speed, this hydrogen gas compressor connects storage hydrogen bottle and fuel cell successively, is connected load and electrolytic cell after fuel cell and the lead-acid battery parallel connection.
The electric supply installation of described electrolytic cell comprises solar cell, wind power generation plant, hydroelectric installation or civil power.
Described electric supply installation directly connects load and lead-acid battery.
Described hydrogen gas compressor is membrane pump compressor or plunger displacement pump compressor.
Electrolytic hydrogen production is a kind of low power electrolytic hydrogen production equipment, hydrogen manufacturing speed is relatively slow, and with producing the hydrogen gas compressor that hydrogen speed is complementary, the low pressure hydrogen that electrolysis is generated is compressed to high pressure during the hydrogen compression, be stored in the hydrogen cylinder guarantee fuel when doing operation of fuel cells.
Described electrolytic hydrogen production part, electrolytic cell power source can be solar cells, wind power generation, the primary energy such as small water conservancy generating (from the net application scenario) or the direct energy from civil power.Small-power is the power that provides with respect to whole stand-by power supply, and the electrolytic cell consumed power is lower, and its electrolysis power is generally 1/2-30 for fuel cell generation provides power 1/1-200.
The hydrogen compression device is a kind of small power hydrogen air compressor, and its hydrogen compression flank speed is approaching with electrolytic hydrogen production speed, and compress mode can be a membrane pump, and plunger displacement pump compression device, power are generally electrolysis installation power 1/3-30.The 1/3-300 of fuel cell generation power output, by the Hydrogen Vapor Pressure after the hydrogen compression device compression generally between 2-100MPa.
Like this, whole system with regard to become the long-time electrolytic hydrogen production of a kind of low-power and stored and high power relatively the generating of short time a system of non-firm power is provided.
Compared with prior art, adopt small-sized electrolytic hydrogen production and compressed hydrogen equipment in the utility model the utility model, with low cost, the cost of whole system is increased fewer, so the overall fuel cell standby power system is compared with traditional lead-acid battery+diesel engine generator and is had competitive advantage.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Embodiment
As shown in Figure 1, a kind of on-the-spot hydrogen manufacturing integrated fuel battery standby power system, comprise electrolytic cell 1, hydrogen gas compressor 2, storage hydrogen bottle 3, fuel cell 4 and lead-acid battery 5, described electrolytic cell 1 connects the hydrogen gas compressor 2 that is complementary with its product hydrogen speed, this hydrogen gas compressor 2 connects storage hydrogen bottle 3 and fuel cell 4 successively, is connected load 6 and electrolytic cell 1 after fuel cell 4 and lead-acid battery 5 parallel connections.
Wherein, fuel cell 4 can provide the electric power of 2KW.Under the usual condition, as standby power system, fuel cell is not worked, be in holding state, because the 220V electric main is arranged under the usual condition, the electric power of load this moment 6 usefulness comes from civil power, does not comprise electrolytic cell 1, hydrogen gas compressor 2, storage hydrogen bottle 3, fuel cell 4 parts among this embodiment in the common standby power system.Electric main offers on the one hand load after by AC/DC, offers lead-acid battery on the one hand, and AC/DC has born the required electric power of load and plumbic acid energy-storage battery.If this moment mains failure, (48V 500AH) provides load required battery as energy-storage battery to lead-acid battery 5, if in the occasion of the long-time power backup of needs, lead-acid battery needs Capacity Ratio bigger, thereby volume, and weight ratio is bigger.
Increased electrolytic cell 1, hydrogen gas compressor 2, storage hydrogen bottle 3, fuel cell 4 in the utility model, the capacity of lead-acid battery 5 can reduce (can adopt the 40AH lead-acid battery) significantly simultaneously.In the utility model, under the usual condition, the required 2KW electric power of load 6 is from civil power, during the civil power outage, lead-acid battery 5 (being 40AH this moment) provides the load required electric power, because lead-acid battery capacity is smaller, provide the time ratio of electric power shorter, being in the fuel cell of holding state this moment starts working, hydrogen in the storage hydrogen bottle 3 enters fuel cell, the operating time of fuel cell is relevant with the capacity of storage hydrogen bottle 3, as long as the hydrogen amount in the storage hydrogen bottle is enough, fuel cell is continuous output power just.When civil power comes, fuel cell.
Because operation of fuel cells needs hydrogen in said process, but for whole system is in stand-by state, the hydrogen in the storage hydrogen bottle should keep certain amount, timely hydrogen make-up when the hydrogen reserves are not enough.Electrolytic cell 1 among the embodiment, hydrogen gas compressor 2, storage hydrogen bottle 3 just plays such function.When civil power came, because amounts of hydrogen reduces in the storage hydrogen bottle of just having worked, electrolytic cell was started working, and the mesolow hydrogen (0.2-3Mpa) of generation is compressed paramount pressure (3-80Mpa) and is stored in the hydrogen cylinder standby.Electrolytic cell power in the present embodiment is 800W, the flow of hydrogen is 1.5L/min (a mark attitude), hydrogen compressor is 100W, whole electrolysis compression device energy consuming ratio is lower, so in whole process, compared with prior art, the AC/DC of the utility model system electromotive power output does not generally increase, but reduces.
Enforcement by this programme, can under the situation that does not change original distribution system, original energy storage lead-acid battery be carried out most replacement, the time of using the hydrogen energy storing and electricity generating can improve non-firm power, improve marginal capacity, solve this difficult problem of hydrogen availability, be convenient to commercial application.
In the utility model, we can replace with lead-acid battery energy-storage batteries such as lithium battery, occasion in the civil power inconvenience, can adopt wind power generation, modes such as solar power generation provide conventional electric power, with unsettled unnecessary solar energy, or wind energy carries out further brine electrolysis, produces hydrogen and lays in.
Claims (4)
1. on-the-spot hydrogen manufacturing integrated fuel battery standby power system, it is characterized in that, comprise electrolytic cell, hydrogen gas compressor, storage hydrogen bottle, fuel cell and lead-acid battery, described electrolytic cell connects the hydrogen gas compressor that is complementary with its product hydrogen speed, this hydrogen gas compressor connects storage hydrogen bottle and fuel cell successively, is connected load after fuel cell and the lead-acid battery parallel connection.
2. on-the-spot hydrogen manufacturing integrated fuel battery standby power system according to claim 1 is characterized in that the electric supply installation of described electrolytic cell comprises solar cell, wind power generation plant, hydroelectric installation or civil power.
3. on-the-spot hydrogen manufacturing integrated fuel battery standby power system according to claim 2 is characterized in that described electric supply installation directly connects load and lead-acid battery.
4. on-the-spot hydrogen manufacturing integrated fuel battery standby power system according to claim 1 is characterized in that described hydrogen gas compressor is membrane pump compressor or plunger displacement pump compressor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120063208XU CN202026127U (en) | 2011-03-11 | 2011-03-11 | Integrated fuel battery backup power supply system for on-site hydrogen production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120063208XU CN202026127U (en) | 2011-03-11 | 2011-03-11 | Integrated fuel battery backup power supply system for on-site hydrogen production |
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| CN202026127U true CN202026127U (en) | 2011-11-02 |
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| CN201120063208XU Expired - Lifetime CN202026127U (en) | 2011-03-11 | 2011-03-11 | Integrated fuel battery backup power supply system for on-site hydrogen production |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105244519A (en) * | 2015-11-10 | 2016-01-13 | 北京有色金属研究总院 | Metal hydride hydrogen storage and fuel cell combination system |
| CN105378042A (en) * | 2013-06-28 | 2016-03-02 | Jx日矿日石能源株式会社 | Compressor oil, method for producing compressor oil, method for compressing hydrogen, method for generating electric power, and method for supplying hydrogen |
| CN105826582A (en) * | 2016-05-20 | 2016-08-03 | 厦门大学 | Electrochemistry type gas compression device and compression method |
| CN109411787A (en) * | 2018-10-31 | 2019-03-01 | 中广核研究院有限公司 | A kind of energy comprehensive utilization system and its design method |
| CN109915352A (en) * | 2019-04-30 | 2019-06-21 | 天津锦美碳材科技发展有限公司 | A kind of tracking regulator control system of variable-flow hydrogen gas compressor operating condition |
| CN110939868A (en) * | 2018-09-25 | 2020-03-31 | 国家能源投资集团有限责任公司 | Supply station and method capable of simultaneously or independently charging and hydrogenating |
-
2011
- 2011-03-11 CN CN201120063208XU patent/CN202026127U/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105378042A (en) * | 2013-06-28 | 2016-03-02 | Jx日矿日石能源株式会社 | Compressor oil, method for producing compressor oil, method for compressing hydrogen, method for generating electric power, and method for supplying hydrogen |
| CN105244519A (en) * | 2015-11-10 | 2016-01-13 | 北京有色金属研究总院 | Metal hydride hydrogen storage and fuel cell combination system |
| CN105826582A (en) * | 2016-05-20 | 2016-08-03 | 厦门大学 | Electrochemistry type gas compression device and compression method |
| CN105826582B (en) * | 2016-05-20 | 2019-07-09 | 厦门大学 | A kind of gas compressing apparatus and compression method of electric chemical formula |
| CN110939868A (en) * | 2018-09-25 | 2020-03-31 | 国家能源投资集团有限责任公司 | Supply station and method capable of simultaneously or independently charging and hydrogenating |
| CN110939868B (en) * | 2018-09-25 | 2021-08-17 | 国家能源投资集团有限责任公司 | Supply station and method capable of simultaneously or independently charging and hydrogenating |
| CN109411787A (en) * | 2018-10-31 | 2019-03-01 | 中广核研究院有限公司 | A kind of energy comprehensive utilization system and its design method |
| CN109915352A (en) * | 2019-04-30 | 2019-06-21 | 天津锦美碳材科技发展有限公司 | A kind of tracking regulator control system of variable-flow hydrogen gas compressor operating condition |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
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Granted publication date: 20111102 |
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| CX01 | Expiry of patent term |