JP6449860B2 - 分配された水素を補給するカスケード式の方法およびシステム - Google Patents
分配された水素を補給するカスケード式の方法およびシステム Download PDFInfo
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- JP6449860B2 JP6449860B2 JP2016517057A JP2016517057A JP6449860B2 JP 6449860 B2 JP6449860 B2 JP 6449860B2 JP 2016517057 A JP2016517057 A JP 2016517057A JP 2016517057 A JP2016517057 A JP 2016517057A JP 6449860 B2 JP6449860 B2 JP 6449860B2
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- Prior art keywords
- fuel
- compressed fuel
- compressed
- compressor
- fuel storage
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- 239000001257 hydrogen Substances 0.000 title claims description 45
- 229910052739 hydrogen Inorganic materials 0.000 title claims description 45
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims description 40
- 238000000034 method Methods 0.000 title claims description 29
- 239000000446 fuel Substances 0.000 claims description 351
- 238000003860 storage Methods 0.000 claims description 144
- 238000009826 distribution Methods 0.000 claims description 92
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 12
- 230000002000 scavenging effect Effects 0.000 claims description 9
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 8
- 230000006835 compression Effects 0.000 claims description 7
- 238000007906 compression Methods 0.000 claims description 7
- 150000002431 hydrogen Chemical class 0.000 claims description 6
- 239000003345 natural gas Substances 0.000 claims description 6
- 238000007599 discharging Methods 0.000 claims description 4
- 239000001294 propane Substances 0.000 claims description 4
- 239000007789 gas Substances 0.000 description 8
- 238000010586 diagram Methods 0.000 description 7
- 230000003466 anti-cipated effect Effects 0.000 description 5
- 238000005868 electrolysis reaction Methods 0.000 description 5
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 239000003792 electrolyte Substances 0.000 description 3
- 239000012528 membrane Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 2
- 239000002608 ionic liquid Substances 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000012913 prioritisation Methods 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 239000002001 electrolyte material Substances 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- -1 hydrogen ions Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000007726 management method Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 238000013341 scale-up Methods 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
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- F17C5/00—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures
- F17C5/06—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures for filling with compressed gases
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
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- F17C2205/0323—Valves
- F17C2205/0329—Valves manually actuated
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- F17C2205/035—Flow reducers
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- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
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- F17C2223/0153—Liquefied gas, e.g. LPG, GPL
- F17C2223/0161—Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
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- F17C2260/00—Purposes of gas storage and gas handling
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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
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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
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- Y02P90/45—Hydrogen technologies in production processes
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
- Fuel Cell (AREA)
- Hydrogen, Water And Hydrids (AREA)
Description
[発明の態様]
[1]
燃料源を圧縮するように設計された圧縮機;
複数の燃料分配ユニット;
燃料圧縮機と複数の燃料分配ユニットとに流体連結された、少なくとも1つの低圧の圧縮燃料貯蔵容器;ならびに
複数の高圧の圧縮燃料貯蔵容器
を含む圧縮燃料分配ステーションであって、各高圧の圧縮燃料貯蔵容器は、燃料圧縮機と少なくとも1つの燃料分配ユニットとに流体連結されている、上記圧縮燃料分配ステーション。
[2]
前記燃料圧縮機と前記複数の燃料分配ユニットとに流体連結された、少なくとも1つの中圧の圧縮燃料貯蔵容器をさらに含む、パラグラフ1に記載の燃料分配ステーション。
[3]
前記少なくとも1つの低圧の圧縮燃料貯蔵容器と前記少なくとも1つの中圧の圧縮燃料貯蔵容器とに流体連結された、少なくとも1つの圧縮機をさらに含み、ここで該圧縮機は、前記低圧の圧縮燃料貯蔵容器から燃料を掃気し、燃料を圧縮して、該中圧の圧縮燃料貯蔵容器に排出するように設計されている、パラグラフ2に記載の燃料分配ステーション。
[4]
前記少なくとも1つの低圧の圧縮燃料貯蔵容器と前記少なくとも1つの高圧の圧縮燃料貯蔵容器とに流体連結された、少なくとも1つの圧縮機をさらに含み、ここで該圧縮機は、前記低圧の圧縮燃料貯蔵容器から燃料を掃気し、燃料を圧縮して、前記高圧の圧縮燃料貯蔵容器に排出するように設計されている、パラグラフ2に記載の燃料分配ステーション。
[5]
前記少なくとも1つの中圧の圧縮燃料貯蔵容器と前記少なくとも1つの高圧の圧縮燃料貯蔵容器とに流体連結された、少なくとも1つの圧縮機をさらに含み、ここで該圧縮機は、前記中圧の圧縮燃料貯蔵容器から燃料を掃気し、燃料を圧縮して、前記高圧の圧縮燃料貯蔵容器に排出するように設計されている、パラグラフ1に記載の燃料分配ステーション。
[6]
前記圧縮燃料貯蔵容器の1つから燃料を掃気し、燃料を圧縮して、より高い圧力の圧縮燃料貯蔵容器の1つに排出するように設計された少なくとも1つの圧縮機をさらに含む、パラグラフ1に記載の燃料分配ステーション。
[7]
前記圧縮機が、電気化学的圧縮機である、パラグラフ6に記載の燃料分配ステーション。
[8]
前記燃料源が、水素、天然ガス、およびプロパンの少なくとも1つを包含する、パラグラフ1に記載の燃料分配ステーション。
[9]
前記圧縮機が、電気化学的水素圧縮機である、パラグラフ1に記載の燃料分配ステーション。
[10]
各高圧の圧縮燃料貯蔵容器が、前記低圧の圧縮燃料貯蔵容器より少ない容積容量を有する、パラグラフ1に記載の燃料分配ステーション。
[11]
分配ステーションから圧縮燃料を分配する方法であって、
燃料源を圧縮する工程;
圧縮された燃料源を、少なくとも1つの低圧の圧縮燃料貯蔵容器と複数の高圧の圧縮燃料貯蔵容器とに分配する工程;
該複数の高圧の圧縮燃料貯蔵容器の1つと関連付けられた燃料分配ユニットに、低圧、次いで高圧で燃料を供給する工程を含む、上記方法。
[12]
前記圧縮された燃料源を、少なくとも1つの中圧の圧縮燃料貯蔵容器に分配する工程をさらに含む、パラグラフ11に記載の分配ステーションから圧縮燃料を分配する方法。
[13]
前記圧縮燃料貯蔵容器の1つから燃料を掃気する工程;
圧縮機を使用して燃料を圧縮する工程;および
より高い圧力の圧縮燃料貯蔵容器の1つに燃料を排出する工程
をさらに含む、パラグラフ11に記載の分配ステーションから圧縮燃料を分配する方法。
[14]
車両に、低圧燃料を放出し、次いでより高い圧力で燃料を放出し、フル充填が達成されるまで高圧燃料を放出し、そして均一化することによって、車両に燃料をフル充填レベルまで供給する工程
をさらに含む、パラグラフ11に記載の分配ステーションから圧縮燃料を分配する方法。
[15]
前記燃料源が、優先順位および燃料分配ユニットの利用率に基づき該高圧の圧縮燃料貯蔵容器に分配される、パラグラフ11に記載の分配ステーションから圧縮燃料を分配する方法。
110 燃料源
120 圧縮機
130 燃料分配ユニット
140 低圧の圧縮燃料貯蔵容器(LPCFR)
150 中圧の圧縮燃料貯蔵容器(MPCFR)
160 高圧の圧縮燃料貯蔵容器(HPCFR)
170 弁
200 CFDS
210 燃料源
220 圧縮機
230 燃料分配ユニット
240 低圧の圧縮燃料貯蔵容器(LPCFR)
250 中圧の圧縮燃料貯蔵容器(MPCFR)
260 高圧の圧縮燃料貯蔵容器(HPCFR)
270 弁
300 CFDS
310 燃料源
320 圧縮機
330 燃料分配ユニット
340 低圧の圧縮燃料貯蔵容器(LPCFR)
350 中圧の圧縮燃料貯蔵容器(MPCFR)
360 高圧の圧縮燃料貯蔵容器(HPCFR)
370 弁
381 第一のEHC
382 第二のEHC
Claims (14)
- 燃料源を圧縮するように設計された圧縮機;
複数の燃料分配ユニット;
燃料圧縮機に流体連結された、少なくとも1つの低圧の圧縮燃料貯蔵容器;
前記燃料圧縮機に流体連結された、少なくとも1つの中圧の圧縮燃料貯蔵容器;ならびに
前記圧縮機から圧縮燃料を受け入れように設計された複数の高圧の圧縮燃料貯蔵容器
を含む圧縮燃料分配ステーションであって、
前記少なくとも1つの低圧の圧縮燃料貯蔵容器および前記少なくとも1つの中圧の圧縮燃料貯蔵容器の各個は、圧縮燃料を複数の燃料分配ユニットに供給するように流体的に設計されおり、そして
前記複数の燃料分配ユニットの各個は、前記複数の高圧の圧縮燃料貯蔵容器のうちの前記各個の燃料分配ユニットに対応した1つから、圧縮燃料を受け入れるように流体的に設計されている、上記圧縮燃料分配ステーション。 - 前記少なくとも1つの低圧の圧縮燃料貯蔵容器と前記少なくとも1つの中圧の圧縮燃料貯蔵容器とに流体連結された、少なくとも1つの圧縮機をさらに含み、ここで該圧縮機は、前記少なくとも1つの低圧の圧縮燃料貯蔵容器から燃料を掃気し、燃料を圧縮して、前記少なくとも1つの中圧の圧縮燃料貯蔵容器に排出するように設計されている、請求項1に記載の圧縮燃料分配ステーション。
- 前記少なくとも1つの低圧の圧縮燃料貯蔵容器と前記複数の高圧の圧縮燃料貯蔵容器とに流体連結された、少なくとも1つの圧縮機をさらに含み、ここで該圧縮機は、前記少なくとも1つの低圧の圧縮燃料貯蔵容器から燃料を掃気し、燃料を圧縮して、前記複数の高圧の圧縮燃料貯蔵容器に排出するように設計されている、請求項1に記載の圧縮燃料分配ステーション。
- 前記少なくとも1つの中圧の圧縮燃料貯蔵容器と前記複数の高圧の圧縮燃料貯蔵容器とに流体連結された、少なくとも1つの圧縮機をさらに含み、ここで該圧縮機は、前記少なくとも1つの中圧の圧縮燃料貯蔵容器から燃料を掃気し、燃料を圧縮して、前記複数の高圧の圧縮燃料貯蔵容器に排出するように設計されている、請求項1に記載の圧縮燃料分配ステーション。
- 前記圧縮燃料貯蔵容器の1つから燃料を掃気し、燃料を圧縮して、より高い圧力の圧縮燃料貯蔵容器の1つに排出するように設計された少なくとも1つの圧縮機をさらに含む、請求項1に記載の圧縮燃料分配ステーション。
- 前記少なくとも1つの圧縮機が、電気化学的圧縮機である、請求項2〜5のいずれかに記載の圧縮燃料分配ステーション。
- 前記燃料源が、水素、天然ガス、およびプロパンの少なくとも1つを包含する、請求項1に記載の圧縮燃料分配ステーション。
- 前記圧縮機が、電気化学的水素圧縮機である、請求項1に記載の圧縮燃料分配ステーション。
- 前記複数の高圧の圧縮燃料貯蔵容器の各個が、前記低圧の圧縮燃料貯蔵容器の各個より少ない容積容量を有する、請求項1に記載の圧縮燃料分配ステーション。
- 分配ステーションから圧縮燃料を分配する方法であって、
燃料源を圧縮する工程;
圧縮された燃料源を、少なくとも1つの低圧の圧縮燃料貯蔵容器と少なくとも1つの中圧の圧縮燃料貯蔵容器と複数の高圧の圧縮燃料貯蔵容器とに分配する工程;
複数の燃料分配ユニットに、低圧、次いで中圧で燃料を供給する工程;
前記複数の高圧の圧縮燃料貯蔵容器のうちの1つから前記複数の燃料分配ユニットのうちの1つへ高圧で燃料を供給する工程を含み、
前記複数の燃料分配ユニットの各個は、前記複数の高圧の圧縮燃料貯蔵容器のうちの前記各個の燃料分配ユニットに対応した1つから圧縮燃料を受け入れるように流体的に設計されている、
上記方法。 - 前記少なくとも1つの低圧の圧縮燃料貯蔵容器の1つ、および/または前記少なくとも1つの中圧の圧縮燃料貯蔵容器の1つから燃料を掃気する工程;
圧縮機を使用して燃料を圧縮する工程;および
より高い圧力の圧縮燃料貯蔵容器の1つに燃料を排出する工程
をさらに含む、請求項10に記載の分配ステーションから圧縮燃料を分配する方法。 - 前記高圧の圧縮燃料貯蔵容器と車両との間の圧力を均一化する工程
をさらに含む、請求項10に記載の分配ステーションから圧縮燃料を分配する方法。 - 前記燃料源が、圧縮燃料を最も必要とする高圧の圧縮燃料貯蔵容器に分配される、請求項10に記載の分配ステーションから圧縮燃料を分配する方法。
- 前記圧縮機が、圧縮燃料を最も必要とする高圧の圧縮燃料貯蔵容器に圧縮燃料を供給する、請求項1に記載の圧縮燃料分配ステーション。
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2014
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CA2912650A1 (en) | 2014-12-04 |
US20180363851A1 (en) | 2018-12-20 |
JP2016526136A (ja) | 2016-09-01 |
WO2014194248A3 (en) | 2015-04-23 |
WO2014194248A2 (en) | 2014-12-04 |
KR20160014044A (ko) | 2016-02-05 |
ES2734553T3 (es) | 2019-12-10 |
EP3004721A2 (en) | 2016-04-13 |
US10077871B2 (en) | 2018-09-18 |
AU2014273940B2 (en) | 2018-09-13 |
US20140352840A1 (en) | 2014-12-04 |
EP3004721B1 (en) | 2019-06-26 |
AU2014273940A1 (en) | 2015-12-03 |
US10295122B2 (en) | 2019-05-21 |
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