JPS6379707A - Burner of reformer for fuel cell - Google Patents
Burner of reformer for fuel cellInfo
- Publication number
- JPS6379707A JPS6379707A JP61224877A JP22487786A JPS6379707A JP S6379707 A JPS6379707 A JP S6379707A JP 61224877 A JP61224877 A JP 61224877A JP 22487786 A JP22487786 A JP 22487786A JP S6379707 A JPS6379707 A JP S6379707A
- Authority
- JP
- Japan
- Prior art keywords
- fuel
- liq
- catalyst
- ignition
- combustion
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000000446 fuel Substances 0.000 title claims abstract description 82
- 238000002485 combustion reaction Methods 0.000 claims abstract description 39
- 239000003054 catalyst Substances 0.000 claims abstract description 33
- 239000007788 liquid Substances 0.000 claims description 25
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 abstract description 12
- 238000006243 chemical reaction Methods 0.000 abstract description 6
- 238000011109 contamination Methods 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 8
- 210000004027 cell Anatomy 0.000 description 7
- 238000005265 energy consumption Methods 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 150000002431 hydrogen Chemical class 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 210000005056 cell body Anatomy 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 241000209140 Triticum Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 239000010425 asbestos Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000002828 fuel tank Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910001120 nichrome Inorganic materials 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 229910052895 riebeckite Inorganic materials 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- 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
- H01M8/0625—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 in a modular combined reactor/fuel cell structure
- H01M8/0631—Reactor construction specially adapted for combination reactor/fuel cell
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01B—BOILING; BOILING APPARATUS ; EVAPORATION; EVAPORATION APPARATUS
- B01B1/00—Boiling; Boiling apparatus for physical or chemical purposes ; Evaporation in general
- B01B1/005—Evaporation for physical or chemical purposes; Evaporation apparatus therefor, e.g. evaporation of liquids for gas phase reactions
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Fuel Cell (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の技術分野〕
本発明は、燃料電池用改質装置の加熱源として設ける燃
焼装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a combustion device provided as a heat source for a fuel cell reformer.
燃料電池の構成は、主として燃料を水素主体の改質ガス
に変化させる改質装置と、この改質装置から発生した改
質ガスの水素を空気(酸素)と反応させて水と電気エネ
ルギに変える燃料電池本体とからなっている。改質装置
ではメタノール等の液体燃料を気化するためと、気化し
た燃料を触媒層′で反応させて改質ガスにするための熱
源が必要であり、その熱源として燃焼器(バーナ)が使
用されるのが一般的である。A fuel cell mainly consists of a reformer that changes fuel into a reformed gas consisting mainly of hydrogen, and a system that reacts the hydrogen in the reformed gas generated by this reformer with air (oxygen) to convert it into water and electrical energy. It consists of a fuel cell body. A reformer requires a heat source to vaporize liquid fuel such as methanol and to react the vaporized fuel in the catalyst layer to form reformed gas, and a combustor (burner) is used as the heat source. It is common to
ところで、上記燃焼器の燃料として液体燃料を使用する
場合は、その液体燃料が気体燃料に比べて貯溜容積が小
さいため装置をコンパトにできるという利点があり、特
に可搬型の燃料電池には極めて有利である。しかし、そ
の反面、液体燃料は初期着火性が悪いため、その着火の
ためにヒータ等で予熱する必要があり、電力などのエネ
ルギ消費量がかなり大きくなるという欠点があった。ま
た、着火前に燃焼部から吐出された燃料が下方へ垂れ流
され、それが汚れを起こし、かつ燃料を無駄にするとい
う欠点があった。By the way, when liquid fuel is used as the fuel for the combustor, it has the advantage that the storage capacity of the liquid fuel is smaller than that of gaseous fuel, so the device can be made more compact, which is particularly advantageous for portable fuel cells. It is. However, on the other hand, since liquid fuel has poor initial ignition properties, it is necessary to preheat it with a heater or the like in order to ignite it, which has the disadvantage that energy consumption such as electric power is considerably large. Furthermore, the fuel discharged from the combustion section before ignition drips downward, causing contamination and wasting the fuel.
本発明の目的は、装置のコンパクト化に有利な液体燃料
を使用するに当たり、着火のためのエネルギ消費を少な
くし、かつ燃料の無駄な垂れ流しや燃焼部の汚れを防止
することができる燃料電池用改質装置の燃焼装置を提供
することにある。An object of the present invention is to reduce the energy consumption for ignition when using liquid fuel, which is advantageous for making the device more compact, and to prevent wasteful dripping of fuel and fouling of the combustion section. An object of the present invention is to provide a combustion device for a reformer.
上記目的を達成する本発明は、燃焼器により燃料蒸発器
を加熱し、この燃料蒸発器で気化した燃料を触媒層で改
質ガスに変える燃料電池用改質装置において、前記燃焼
器を液体燃料で燃焼させ、その燃焼部の火炎発生部下部
側に点火用触媒を配置したことを特徴とするものである
。To achieve the above object, the present invention provides a fuel cell reformer in which a fuel evaporator is heated by a combustor, and the fuel vaporized by the fuel evaporator is converted into reformed gas by a catalyst layer. It is characterized by having an ignition catalyst disposed below the flame generating part of the combustion part.
第1〜3図は本発明の実施例による燃焼装置を示し、第
4図は同燃焼装置が使用される燃料電池用改質′、麦装
の一例を示すものである。1 to 3 show a combustion apparatus according to an embodiment of the present invention, and FIG. 4 shows an example of a fuel cell reforming system and a wheat dressing in which the combustion apparatus is used.
第4図において、1は環状に形成された燃料蒸発器で、
その周囲に燃料供給ノズル2、−。In FIG. 4, 1 is an annularly formed fuel evaporator;
Around it a fuel supply nozzle 2,-.
2が複数個所に取り付けられ、メタノールと水との混合
液体燃料が供給されるようになっている。この燃料蒸発
器1の下方に、詳細を後述する燃焼器3が設置され、こ
の燃焼器3による加熱によって液体燃料を気化させるよ
うになっている。2 are attached to multiple locations to supply a liquid fuel mixture of methanol and water. A combustor 3, the details of which will be described later, is installed below the fuel evaporator 1, and the liquid fuel is vaporized by heating by the combustor 3.
燃料蒸発器1の上面には複数の反応管4.・・・・、4
が接続され、その各反応管4の内側には触媒が充填され
て触媒層5が形成されている。この触媒層5では、燃料
蒸発器1で気化された燃料が水素主体の改質ガスに変化
する反応を行い、それが上部の集合室6に集められ、さ
らに図示しない燃料電池本体へ送り出されるようになっ
ている。On the upper surface of the fuel evaporator 1, there are a plurality of reaction tubes 4. ..., 4
are connected, and the inside of each reaction tube 4 is filled with a catalyst to form a catalyst layer 5. In this catalyst layer 5, the fuel vaporized in the fuel evaporator 1 undergoes a reaction to change into reformed gas consisting mainly of hydrogen, which is collected in an upper collecting chamber 6 and further sent to the fuel cell main body (not shown). It has become.
また、複数本の反応管4.−、 4の周囲は断熱壁7に
よって囲まれ、燃焼器3から上昇する加熱ガスによる加
熱空間を形成している。断熱壁7の上部には多数の排気
孔8、−、 8が設けられ、加熱空間内の加熱ガスを外
側へ排出させるようになっている。In addition, a plurality of reaction tubes 4. -, 4 are surrounded by a heat insulating wall 7, forming a space heated by the heated gas rising from the combustor 3. A large number of exhaust holes 8, -, 8 are provided in the upper part of the heat insulating wall 7, and the heated gas in the heating space is discharged to the outside.
第1〜3図に示す燃焼器3において、18は燃料電池本
体で空気(酸素)と反応しないまま排出された余剰の水
素が、気体燃料として供給される気体燃料供給管である
。この気体燃料供給管18は環状の燃焼管19に接続さ
れ、かつその燃焼管19の円周方向にそって穿たれた多
数の小孔20.・−220から気体燃料が流出して燃焼
するようになっている。In the combustor 3 shown in FIGS. 1 to 3, 18 is a gaseous fuel supply pipe through which surplus hydrogen discharged without reacting with air (oxygen) in the fuel cell body is supplied as gaseous fuel. This gaseous fuel supply pipe 18 is connected to an annular combustion pipe 19, and a large number of small holes 20 are bored along the circumferential direction of the combustion pipe 19. - Gaseous fuel flows out from the -220 and burns.
一方、10は液体燃料供給管であり、送液量(回転数)
を調節制御できるポンプ11が接続され、図示しない燃
料タンクからメタノール等の液体燃料を供給するように
なっている。この液体燃料供給管10は、分配管12に
接続され、さらにその分配管12には円周方向にそって
多数の燃焼管13.−・−913が接続されている。On the other hand, 10 is a liquid fuel supply pipe, and the amount of liquid fed (rotation speed)
A pump 11 is connected to the pump 11 and supplies liquid fuel such as methanol from a fuel tank (not shown). This liquid fuel supply pipe 10 is connected to a distribution pipe 12, and the distribution pipe 12 further includes a large number of combustion pipes 13. -.-913 is connected.
各燃焼管13は上端がループ状に丸められて二股状にな
り、その両脚が環状の分配管12に接続されるように形
成され、かつ内部には石綿。The upper end of each combustion tube 13 is rounded into a loop shape to form a bifurcated shape, both legs of which are connected to the annular distribution pipe 12, and the inside is filled with asbestos.
ガラス繊維等からなる溶存14が挿入されている。また
、各燃焼管13のループ部13aの内周側には1個又は
複数個の小孔15.−・−・、15が穿たれ、その小孔
15を介して内部の溶存14が外気へ臨み、そこから液
体燃料が蒸発して燃焼するようになっている。A melt 14 made of glass fiber or the like is inserted. Furthermore, one or more small holes 15. -..., 15 are bored, and the dissolved fuel 14 inside faces the outside air through the small holes 15, from which the liquid fuel evaporates and burns.
多数本の燃焼管13.−・−・、13の上端部付近には
、これら全体に跨るように横渡し部材16が固定され、
各燃焼管13を振動させないように安定させている。ま
た、この横渡し部材16と気体燃料の燃焼管19との間
にはマット状の点火用触媒17が保持され、燃焼管13
.19の火炎発生部である小孔15.20よりは下部に
位置している。また、この点火用触媒17の中にはニク
ロム線等のヒータ21が環状に埋設され(第3図参照)
、リード線22.22からの通電によって発熱し、点火
用触媒17を活性化させるようにしている。Multiple combustion tubes 13. -..., 13, a horizontal member 16 is fixed near the upper end thereof so as to straddle the entirety thereof,
Each combustion tube 13 is stabilized so as not to vibrate. Further, a mat-like ignition catalyst 17 is held between the horizontal member 16 and the gaseous fuel combustion pipe 19, and the combustion pipe 13
.. It is located below the small hole 15.20 which is the flame generating part of No. 19. Furthermore, a heater 21 such as a nichrome wire is buried in the ignition catalyst 17 in an annular shape (see Fig. 3).
, the ignition catalyst 17 is activated by generating heat by applying electricity from the lead wires 22 and 22.
また、この点火用触媒17の外周には、適当な間隔で複
数個所にノズル23.−・・、23が配設され、液体燃
料が点火用触媒に向けて噴射されるようになっている。Further, on the outer periphery of this ignition catalyst 17, nozzles 23. -..., 23 are arranged so that liquid fuel is injected toward the ignition catalyst.
このノズル23からは点火時にのみ液体燃料を噴射する
ため、上記液体燃料供給管10とは別系統の燃料供給系
が設けられ、点火用液体燃料供給管24から分配管25
を介して供給されるようにしである。また、燃焼用の燃
料ではないので、このノズル23には溶存は内挿されて
いない。Since the liquid fuel is injected from this nozzle 23 only at the time of ignition, a fuel supply system separate from the liquid fuel supply pipe 10 is provided, and from the ignition liquid fuel supply pipe 24 to the distribution pipe 25.
It is to be supplied via. Further, since the fuel is not for combustion, no dissolved gas is inserted into this nozzle 23.
上述した燃焼装置によると、液体燃料用の燃焼管13に
対し点火用触媒17が取り付けであるため、従来のよう
に大電力によって予熱しなくても初期着火することがで
きる。しかも、点火用触媒17は燃焼管13の火炎発生
部(小孔15)より下方に配置されているため、着火後
において火炎に常時曝されることがなく、触媒寿命を延
長することができる。According to the above-mentioned combustion device, since the ignition catalyst 17 is attached to the combustion pipe 13 for liquid fuel, initial ignition can be performed without preheating with large electric power as in the conventional case. Moreover, since the ignition catalyst 17 is arranged below the flame generating part (small hole 15) of the combustion tube 13, it is not constantly exposed to flame after ignition, and the life of the catalyst can be extended.
また、燃焼管13の小孔15から点火前に液体燃料が漏
出しても、下方の点火用触媒17に捕捉されるため、そ
のまま下方へ滴下することがない。そして、着火と同時
に燃焼消失するため、燃料を無駄にすることがなく、か
つ燃焼部を汚すこともない。Further, even if liquid fuel leaks from the small hole 15 of the combustion tube 13 before ignition, it will be captured by the ignition catalyst 17 below, so it will not drip downward. Since the fuel is burned and extinguished at the same time as ignition, fuel is not wasted and the combustion section is not contaminated.
また、点火時に、上記実施例のように点火用触媒17に
対しノズル23から積極的に液体燃料を噴射するように
すれば、着火時間を短縮することができる。さらに、実
施例のようにヒータ21を併用して触媒を活性化するよ
うにすれば、−層着火時間の短縮を図ることができる。Further, when igniting, if liquid fuel is actively injected from the nozzle 23 to the ignition catalyst 17 as in the above embodiment, the ignition time can be shortened. Furthermore, if the heater 21 is used in combination to activate the catalyst as in the embodiment, it is possible to shorten the -layer ignition time.
このヒータ21は、触媒を活性化するだけのものである
ので、従来装置の燃料予熱用ヒータのように大電力を消
費することはなく、エネルギ消費量を極めて少ないもの
にすることができる。Since this heater 21 only activates the catalyst, it does not consume a large amount of electric power unlike the fuel preheating heater of the conventional device, and the amount of energy consumption can be extremely reduced.
上述したように本発明は、液体燃料で燃焼を行うように
した燃焼部に点火用触媒を使用するようにしたので、従
来装置のヒータで予熱するものに比べて着火のためのエ
ネルギ消費を少なくすることができる。しかも、上記点
火用触媒を燃焼部の火炎発生部下部側に配置するので、
点火用触媒が着火後においても火炎に曝されることがな
く、点火用触媒の寿命を延長することができる。As mentioned above, the present invention uses an ignition catalyst in the combustion section that burns liquid fuel, so the energy consumption for ignition is reduced compared to the conventional device that preheats with a heater. can do. Moreover, since the above-mentioned ignition catalyst is placed on the lower side of the flame generation part of the combustion part,
Even after ignition, the ignition catalyst is not exposed to flame, and the life of the ignition catalyst can be extended.
また、着火前に燃焼部から液体燃料が漏出しても、下方
の点火用触媒によって捕捉されるため着火と同時に燃焼
消失し、燃焼部を汚したり、また燃料を無駄にすること
がない。Furthermore, even if liquid fuel leaks from the combustion section before ignition, it is captured by the ignition catalyst below, so it burns and disappears at the same time as ignition, thereby preventing contamination of the combustion section and waste of fuel.
第1図は本発明の実施例による燃焼装置を示す側面図、
第2図は同平面図、第3図は第1図のm−m矢視図、第
4図は同燃焼装置を使用する燃料電池用改質装置の一例
を示す縦断面図である。
1・・・燃料蒸発器、 3・・・燃焼器、 4・・・反
応管、 5・・・触媒層、 lO・・・液体燃料供給管
、12・・・分配管、 13・・・燃焼管、 14・・
・溶存、15・・・小孔(火炎発生部)、 17・・・
点火用触媒、 23・・・ノズル、 24・・・点火用
液体燃料供給管、 25・・・分配管。
第4図FIG. 1 is a side view showing a combustion device according to an embodiment of the present invention;
2 is a plan view of the same, FIG. 3 is a view taken along the line mm in FIG. 1, and FIG. 4 is a longitudinal cross-sectional view showing an example of a fuel cell reformer using the same combustion apparatus. DESCRIPTION OF SYMBOLS 1...Fuel evaporator, 3...Combustor, 4...Reaction tube, 5...Catalyst layer, 1O...Liquid fuel supply pipe, 12...Distribution pipe, 13...Combustion Tube, 14...
・Dissolved, 15... Small hole (flame generation part), 17...
Catalyst for ignition, 23... Nozzle, 24... Liquid fuel supply pipe for ignition, 25... Distribution pipe. Figure 4
Claims (3)
器で気化した燃料を触媒層で改質ガスに変える燃料電池
用改質装置において、前記燃焼器を液体燃料で燃焼させ
、その燃焼部の火炎発生部下部側に点火用触媒を配置し
たことを特徴とする燃料電池用改質装置の燃焼装置。(1) In a fuel cell reformer that heats a fuel evaporator with a combustor and converts the vaporized fuel in the fuel evaporator into reformed gas in a catalyst layer, the combustor is combusted with liquid fuel, and the combustion A combustion device for a fuel cell reformer, characterized in that an ignition catalyst is disposed on the lower side of a flame generating section.
1項記載の燃料電池用改質装置の燃焼装置。(2) A combustion device for a fuel cell reformer according to claim 1, wherein the combustion section comprises a wick combustion mechanism.
媒に対し液体燃料を噴射する点火用燃料系を設けた特許
請求の範囲第2項記載の燃料電池用改質装置の燃焼装置
。(3) A combustion device for a fuel cell reformer according to claim 2, further comprising an ignition fuel system for injecting liquid fuel to an ignition catalyst, in addition to a combustion fuel system for the combustion section.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61224877A JPS6379707A (en) | 1986-09-25 | 1986-09-25 | Burner of reformer for fuel cell |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61224877A JPS6379707A (en) | 1986-09-25 | 1986-09-25 | Burner of reformer for fuel cell |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6379707A true JPS6379707A (en) | 1988-04-09 |
Family
ID=16820570
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61224877A Pending JPS6379707A (en) | 1986-09-25 | 1986-09-25 | Burner of reformer for fuel cell |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6379707A (en) |
-
1986
- 1986-09-25 JP JP61224877A patent/JPS6379707A/en active Pending
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