JP2009115073A - Fuel cell-mounted type engine part 3 - Google Patents
Fuel cell-mounted type engine part 3 Download PDFInfo
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- JP2009115073A JP2009115073A JP2007322596A JP2007322596A JP2009115073A JP 2009115073 A JP2009115073 A JP 2009115073A JP 2007322596 A JP2007322596 A JP 2007322596A JP 2007322596 A JP2007322596 A JP 2007322596A JP 2009115073 A JP2009115073 A JP 2009115073A
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- engine
- ammonia
- hydrogen
- fuel cell
- naphtha
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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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
-
- 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
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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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
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- Fuel Cell (AREA)
Abstract
Description
燃料電池利用によるエンジンに関する省エネ技術分野Energy-saving technology related to engines using fuel cells
水素発生技術、炭化水素分解技術、省エネ技術Hydrogen generation technology, hydrocarbon decomposition technology, energy saving technology
燃料電池搭載型エンジンとして精製ナフサをエンジンの排熱を利用して脱水素環化反応を水素下で達成する特許(P2002−317188A)を発明し、かつ特許願(2005−175657)としてディーゼル用としてNH3から水素をとり出す発明をしてきたがエンジンの排熱の熱回収方法としてNH3を利用することが水素発生が容易であることが判明した。
循環水素ガスに代えて、アンモニア存在下で精製ナフサを水素下接触分解させる事によって、水素循環系の循環コンプレッサー等が不必要になり、運転が容易に達成される。Invented a patent (P2002-317188A) that achieves a dehydrocyclization reaction under hydrogen using exhaust heat of the engine as a fuel cell-mounted engine, and as a patent application (2005-175657) for diesel Although the invention of extracting hydrogen from NH 3 has been made, it has been found that it is easy to generate hydrogen by using NH 3 as a heat recovery method for exhaust heat of the engine.
Instead of circulating hydrogen gas, purified naphtha is catalytically cracked under hydrogen in the presence of ammonia, thereby eliminating the need for a circulating compressor or the like of the hydrogen circulation system and easily achieving operation.
精製ナフサから脱水素環化反応させるには水素の存在、触媒、吸熱反応を補完する熱源が必要となる。脱水素環化反応をすることにより精製ナフサはオクタン価の高い製品になり、それによりガソリンエンジンは稼動しやすくなるが通常のガソリンは精油所内で脱水素反応をされたものを市販店より購入し、運転しているが特許(P2002−317788A)の内容ではエンジンの排熱を利用して、燃料電池用の水素を精製ナフサからとり、同時に粗製ガソリンを発生させる仕組みについて言及している。この発明の欠点はひとつは脱水環化反応には高温と、水素下という条件が欠かせず、その水素をエンジンの一部を利用して、水素循環機として使用する煩雑さが組み込まれ、やや実現性に欠けるきらいがある。今ひとつは触媒に関して、充分な能力を発揮するものが発見されていないことがある。これらを解決する手段として、NH3を利用すると、アンモニアは低温で水素を窒素に分解するので、結果的に水素、窒素雰囲気で精製ナフサを脱水環化反応装置に挿入出来ることになる。
アンモニアは常温で約10kg/cmGの圧力があるので、その圧力を使えば系内の圧損をcoverしつつ、一緒に圧入した精製ナフサを反応器へと導びくことが出来、機械的な煩雑さを一部さける事ができる。一方、窒素は熱媒体として利用出来、触媒上及び下流の燃料電池とっても問題ないものとなる。即ち、循環水素用compressorの不必要なシステムを提供出来ることになる。In order to carry out the dehydrocyclization reaction from purified naphtha, the presence of hydrogen, a catalyst, and a heat source that complements the endothermic reaction are required. Purified naphtha becomes a product with a high octane number by dehydrocyclization reaction, which makes it easy to operate the gasoline engine, but purchase ordinary gasoline dehydrogenated in a refinery from a commercial store, Although it is operating, the content of the patent (P2002-317788A) refers to a mechanism that uses exhaust heat of the engine to take hydrogen for the fuel cell from purified naphtha and simultaneously generate crude gasoline. One of the disadvantages of this invention is that the dehydration cyclization reaction requires conditions of high temperature and under hydrogen, and the trouble of using the hydrogen as a hydrogen circulator using a part of the engine is incorporated. There is a lack of feasibility. The other thing is that no catalyst has been discovered that demonstrates sufficient capacity. As a means for solving these problems, when NH 3 is used, ammonia decomposes hydrogen into nitrogen at a low temperature. As a result, purified naphtha can be inserted into the dehydration cyclization reactor in a hydrogen and nitrogen atmosphere.
Since ammonia has a pressure of about 10 kg / cmG at room temperature, using that pressure can cover the pressure loss in the system and lead the purified naphtha injected together to the reactor. Can be avoided. On the other hand, nitrogen can be used as a heat medium, and there is no problem with the fuel cell on the catalyst and downstream. That is, an unnecessary system for circulating hydrogen compressor can be provided.
この方法を使用するとガソリンの消費量は半減以下になる。
燃料電池系の運転保持が改善される。If this method is used, the consumption of gasoline will be halved or less.
Operational maintenance of the fuel cell system is improved.
エンジンの排熱の一部をBypassさせて、脱水素用の反応熱を確保し、精製ナフサはアンモニアと混合され、排ガス中ある熱交換器群によって順次、昇温され、反応塔に入る。この時の温度は600℃以上が望ましいが排ガスの温度は600〜900℃なので充分達成できる。アンモニアは液弁タンクに封入してあるのでその圧力10kg/cm2G内外を利用してOne throughの流れを作る。図−1参照A part of the exhaust heat of the engine is bypassed to secure reaction heat for dehydrogenation, and the purified naphtha is mixed with ammonia, and the temperature is sequentially raised by a group of heat exchangers in the exhaust gas and enters the reaction tower. The temperature at this time is preferably 600 ° C. or higher, but the exhaust gas temperature is 600 to 900 ° C., which can be sufficiently achieved. Since ammonia is sealed in the liquid valve tank, the flow of One through is made using the inside and outside of the pressure 10 kg / cm 2 G. See Fig-1.
極めて高い、地球温暖化対策としてのCo2削減、省エネにかなう。Extremely high, Co 2 reduction of as global warming, come true to energy saving.
A.エンジン H1,H2,H3 熱交器
B.エンジン排気ガス a.空気
C.ターボ.チャージャー b,アンモニア
R.反応器 n,ナフサ
M.メンブラン,セパレーター h,水素リッチガス及び窒素ガス
F,燃料電池
D1,アンモニアタンク
D2,ナフサタンク
D3,粗成ガソリン
D4,水タンク
P,精密filterA. Engine H 1 , H 2 , H 3 heat exchanger B. Engine exhaust gas a. Air C.I. turbo. Charger b, ammonia R. Reactor n, naphtha M. Membrane, separator h, hydrogen rich gas and nitrogen gas F, fuel cell D 1 , ammonia tank D 2 , naphtha tank D 3 , crude gasoline D 4 , water tank P, precision filter
Claims (13)
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JP2007322596A JP2009115073A (en) | 2007-11-06 | 2007-11-06 | Fuel cell-mounted type engine part 3 |
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JP2007322596A JP2009115073A (en) | 2007-11-06 | 2007-11-06 | Fuel cell-mounted type engine part 3 |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104675515A (en) * | 2015-02-13 | 2015-06-03 | 王海斌 | Gasoline and ammonia double-fuel supply device for automobile engine |
CN109520822A (en) * | 2018-12-17 | 2019-03-26 | 陕西化建工程有限责任公司 | A kind of DCC device ultra-large volume reactor gas pressure test system and method |
CN109520852A (en) * | 2018-12-17 | 2019-03-26 | 陕西化建工程有限责任公司 | A kind of DCC device ultra-large volume regenerator gas pressure test system and method |
CN113294801A (en) * | 2021-05-26 | 2021-08-24 | 华中科技大学 | Combustion device capable of realizing high-efficiency clean combustion of pure ammonia and control method thereof |
CN114876632A (en) * | 2022-05-27 | 2022-08-09 | 北京工业大学 | Ammonia fuel-based internal combustion engine-fuel cell hybrid power generation device and control method thereof |
-
2007
- 2007-11-06 JP JP2007322596A patent/JP2009115073A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104675515A (en) * | 2015-02-13 | 2015-06-03 | 王海斌 | Gasoline and ammonia double-fuel supply device for automobile engine |
CN109520822A (en) * | 2018-12-17 | 2019-03-26 | 陕西化建工程有限责任公司 | A kind of DCC device ultra-large volume reactor gas pressure test system and method |
CN109520852A (en) * | 2018-12-17 | 2019-03-26 | 陕西化建工程有限责任公司 | A kind of DCC device ultra-large volume regenerator gas pressure test system and method |
CN113294801A (en) * | 2021-05-26 | 2021-08-24 | 华中科技大学 | Combustion device capable of realizing high-efficiency clean combustion of pure ammonia and control method thereof |
CN114876632A (en) * | 2022-05-27 | 2022-08-09 | 北京工业大学 | Ammonia fuel-based internal combustion engine-fuel cell hybrid power generation device and control method thereof |
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