JP2000226201A - Improver for fuel cell - Google Patents
Improver for fuel cellInfo
- Publication number
- JP2000226201A JP2000226201A JP11027679A JP2767999A JP2000226201A JP 2000226201 A JP2000226201 A JP 2000226201A JP 11027679 A JP11027679 A JP 11027679A JP 2767999 A JP2767999 A JP 2767999A JP 2000226201 A JP2000226201 A JP 2000226201A
- Authority
- JP
- Japan
- Prior art keywords
- fuel cell
- reformer
- catalyst
- holding
- metal pipe
- 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.)
- Granted
Links
- 239000000446 fuel Substances 0.000 title claims abstract description 33
- 239000003054 catalyst Substances 0.000 claims abstract description 42
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 38
- 239000001257 hydrogen Substances 0.000 claims abstract description 38
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 38
- 239000000463 material Substances 0.000 claims abstract description 30
- 239000012535 impurity Substances 0.000 claims abstract description 29
- 229910052751 metal Inorganic materials 0.000 claims abstract description 24
- 239000002184 metal Substances 0.000 claims abstract description 24
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims abstract description 19
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims abstract description 19
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000000460 chlorine Substances 0.000 claims abstract description 19
- 229910052801 chlorine Inorganic materials 0.000 claims abstract description 19
- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 19
- 239000011574 phosphorus Substances 0.000 claims abstract description 19
- 239000011593 sulfur Substances 0.000 claims abstract description 19
- 229910052717 sulfur Inorganic materials 0.000 claims abstract description 19
- 239000012784 inorganic fiber Substances 0.000 claims abstract description 12
- 150000002430 hydrocarbons Chemical class 0.000 claims description 8
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract description 10
- 239000000835 fiber Substances 0.000 abstract description 8
- 229910052878 cordierite Inorganic materials 0.000 abstract description 6
- JSKIRARMQDRGJZ-UHFFFAOYSA-N dimagnesium dioxido-bis[(1-oxido-3-oxo-2,4,6,8,9-pentaoxa-1,3-disila-5,7-dialuminabicyclo[3.3.1]nonan-7-yl)oxy]silane Chemical compound [Mg++].[Mg++].[O-][Si]([O-])(O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2)O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2 JSKIRARMQDRGJZ-UHFFFAOYSA-N 0.000 abstract description 6
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 abstract description 6
- 229910052697 platinum Inorganic materials 0.000 abstract description 3
- 238000005260 corrosion Methods 0.000 abstract description 2
- 230000007797 corrosion Effects 0.000 abstract description 2
- 229910001220 stainless steel Inorganic materials 0.000 abstract description 2
- 239000010935 stainless steel Substances 0.000 abstract description 2
- 238000007789 sealing Methods 0.000 abstract 4
- 230000014759 maintenance of location Effects 0.000 abstract 3
- 239000000126 substance Substances 0.000 abstract 1
- 239000003566 sealing material Substances 0.000 description 34
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 21
- 230000000052 comparative effect Effects 0.000 description 4
- 238000010248 power generation Methods 0.000 description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 229910052581 Si3N4 Inorganic materials 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 description 2
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 1
- 229910010271 silicon carbide Inorganic materials 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- 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
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Catalysts (AREA)
- Fuel Cell (AREA)
- Hydrogen, Water And Hydrids (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、例えば車両に搭載
される燃料電池用改質器に関するものである。The present invention relates to a reformer for a fuel cell mounted on a vehicle, for example.
【0002】[0002]
【従来の技術】従来、主として燃料電池用改質器は、触
媒保持体と、同保持体の外周を覆う金属製パイプと、両
者間に配置した保持シール材とを備えている。2. Description of the Related Art Conventionally, a reformer for a fuel cell mainly comprises a catalyst holder, a metal pipe for covering the outer periphery of the holder, and a holding seal material disposed between the two.
【0003】触媒保持体には白金等の触媒が担持されて
いる。触媒保持体としては、例えばハニカム状に成形し
たコージェライト担体が用いられている。この触媒保持
体は、メタノール等の炭化水素化合物を通過させること
により水素を発生させる。A catalyst such as platinum is supported on a catalyst holder. As the catalyst holder, for example, a cordierite carrier formed in a honeycomb shape is used. The catalyst holder generates hydrogen by passing a hydrocarbon compound such as methanol.
【0004】また、保持シール材としては、通常、セラ
ミックファイバー等の無機繊維のみからなるものが用い
られている。この保持シール材は、自動車の走行中等に
おいて触媒保持体が金属製パイプと当接した際の破損を
防ぐため、また金属製シェルと触媒保持体との間から炭
化水素化合物がリークすることを防ぐために用いられて
いる。[0004] As the holding sealing material, one made of only inorganic fibers such as ceramic fibers is usually used. This holding sealing material is used to prevent the catalyst holding body from being damaged when the catalyst holding body comes into contact with the metal pipe during driving of an automobile or the like, and also to prevent hydrocarbon compounds from leaking from between the metal shell and the catalyst holding body. Used for
【0005】[0005]
【発明が解決しようとする課題】ところで、一般的な保
持シール材には、塩素、リン、硫黄などの不純物が、2
〜3wt%以上の濃度で含有されていることが発明者に
よって確認されている。By the way, impurities such as chlorine, phosphorus, and sulfur are contained in a general holding sealing material.
It has been confirmed by the inventor that it is contained at a concentration of 以上 3 wt% or more.
【0006】また、NBRやSBR等の有機バインダを
1〜10wt%程度含浸させた保持シール材については不
純物濃度がさらに高くなっている。しかしながら、不純
物を多量に含む保持シール材を用いると、改質器によっ
て生成される水素に、塩素、リン、硫黄などが混入して
しまい、水素の純度が低下してしまう。そして、このよ
うに水素の純度が低下すると、燃料電池の発電効率が低
下する、装置の寿命が短くなるなどの不都合を生じるこ
とが予想される。[0006] Further, the holding seal material impregnated with an organic binder such as NBR or SBR at about 1 to 10 wt% has a higher impurity concentration. However, when a holding sealing material containing a large amount of impurities is used, chlorine, phosphorus, sulfur, and the like are mixed into hydrogen generated by the reformer, and the purity of hydrogen is reduced. When the purity of hydrogen is reduced in this way, it is expected that inconveniences such as a decrease in power generation efficiency of the fuel cell and a shortened life of the device will occur.
【0007】本発明はこうした実情に鑑みてなされたも
のであり、その目的は、純度の高い水素を生成させるこ
とのできる燃料電池用改質器を提供することにある。The present invention has been made in view of such circumstances, and an object of the present invention is to provide a reformer for a fuel cell capable of producing high-purity hydrogen.
【0008】[0008]
【課題を解決するための手段】上記の課題を解決するた
めに、請求項1に記載の発明では、炭化水素化合物と反
応して水素を生成させる触媒を保持する触媒保持体と、
同触媒保持体を収容する金属製パイプと、前記触媒保持
体及び前記金属製パイプの間に配置されて前記触媒保持
体を保持する保持シール材とを備える燃料電池用改質器
において、前記保持シール材は、低不純物濃度の無機繊
維材料からなり、かつ樹脂未含浸のマット状物であるこ
とを要旨とする。In order to solve the above-mentioned problems, according to the first aspect of the present invention, there is provided a catalyst holder for holding a catalyst for producing hydrogen by reacting with a hydrocarbon compound;
A fuel cell reformer, comprising: a metal pipe for accommodating the catalyst holder; and a holding sealer disposed between the catalyst holder and the metal pipe for holding the catalyst holder. The gist is that the sealing material is made of an inorganic fiber material having a low impurity concentration and is a resin-impregnated mat-like material.
【0009】請求項2に記載の発明では、請求項1に記
載の燃料電池用改質器において、前記マット状物中にお
ける不純物濃度は、1%未満であることを要旨とする。
請求項3に記載の発明では、請求項1または請求項2に
記載の燃料電池用改質器において、前記マット状物中に
おける塩素、硫黄及びリンの濃度は、300ppm以下で
あることを要旨とする。According to a second aspect of the present invention, in the fuel cell reformer according to the first aspect, an impurity concentration in the mat-like material is less than 1%.
According to a third aspect of the present invention, in the fuel cell reformer according to the first or second aspect, the concentration of chlorine, sulfur, and phosphorus in the mat-like material is 300 ppm or less. I do.
【0010】以下、本発明の「作用」について説明す
る。請求項1に記載の発明によると、低不純物濃度の無
機繊維材料からなり、かつ樹脂未含浸のマット状物を保
持シール材として用いている。すなわち、もともと不純
物の含有量が少ないため、生成される水素に混入する不
純物も少なくなる。したがって、生成される水素を高純
度に維持することができる。その結果、水素純度の低下
に起因する燃料電池の発電効率の低下等を確実に防止す
ることができる。Hereinafter, the "action" of the present invention will be described. According to the first aspect of the invention, a mat-like material made of an inorganic fiber material having a low impurity concentration and not impregnated with a resin is used as a holding sealing material. That is, since the content of impurities is originally small, the amount of impurities mixed into the generated hydrogen is also reduced. Therefore, the generated hydrogen can be maintained at a high purity. As a result, it is possible to reliably prevent a decrease in the power generation efficiency of the fuel cell due to a decrease in the hydrogen purity.
【0011】請求項2に記載の発明によると、保持シー
ル材に含有される不純物濃度を1%未満とすることによ
り、生成される水素を確実に高純度に維持することがで
きる。According to the second aspect of the present invention, by setting the concentration of impurities contained in the holding sealing material to less than 1%, the generated hydrogen can be reliably maintained at a high purity.
【0012】請求項3に記載の発明によると、保持シー
ル材に含有される塩素、硫黄及びリンの濃度を300pp
m以下とすることにより、生成される水素をさらに確実
に高純度に維持することができる。According to the third aspect of the present invention, the concentration of chlorine, sulfur and phosphorus contained in the holding sealing material is set to 300 pp.
By setting it to m or less, the generated hydrogen can be more reliably maintained at a high purity.
【0013】[0013]
【発明の実施の形態】以下、本発明を具体化した一実施
形態を図1及び図2に基づき詳細に説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described below in detail with reference to FIGS.
【0014】図1に示すように、燃料電池1には改質器
2が接続されている。本実施形態において、この燃料電
池1及び改質器2は車両等に搭載され、同燃料電池1に
は、車両の走行や車両電装品の駆動などに用いられるモ
ータ3が接続されている。As shown in FIG. 1, a fuel cell 1 is connected to a reformer 2. In the present embodiment, the fuel cell 1 and the reformer 2 are mounted on a vehicle or the like, and the fuel cell 1 is connected to a motor 3 used for running the vehicle, driving vehicle electric components, and the like.
【0015】改質器2は、図2に示すように、本体13
とその本体13を収容する金属パイプ14とから構成さ
れている。本体13は、円柱状をなす触媒保持体11
と、同保持体11の外周面に巻き付けられた保持シール
材12とから構成されている。[0015] As shown in FIG.
And a metal pipe 14 for accommodating the main body 13 thereof. The main body 13 has a cylindrical catalyst holder 11.
And a holding sealing material 12 wound around the outer peripheral surface of the holding body 11.
【0016】触媒保持体11には白金等の触媒が担持さ
れている。この触媒保持体11としては、例えばハニカ
ム状に成形したコージェライトやアルミナ等の多孔質体
が用いられている。なお、本実施形態において触媒保持
体11は、略真円状の断面形状を有している。また、触
媒保持体11中における不純物濃度、すなわち塩素、硫
黄、リンの含有濃度も極めて小さくなっている。The catalyst holder 11 carries a catalyst such as platinum. As the catalyst holder 11, a porous body made of, for example, cordierite or alumina formed into a honeycomb shape is used. In this embodiment, the catalyst holder 11 has a substantially perfect circular cross section. Further, the impurity concentration in the catalyst holder 11, that is, the concentration of chlorine, sulfur, and phosphorus is extremely low.
【0017】保持シール材12はマット状物である。同
保持シール材12の一端には凸部12aが形成され、他
端には凸部12aと対応する凹部12bが形成されてい
る。また、この保持シール材12は、結晶質アルミナ繊
維やシリカ−アルミナ繊維等の無機繊維材料から構成さ
れ、塩素、硫黄及びリンの不純物の含有濃度が、それぞ
れ100ppm以下に設定されている。なお、保持シール
材12にNBRやSBR等の有機バインダは含浸されて
いない。すなわち、保持シール材12は、低不純物濃度
の無機繊維材料である。The holding sealing material 12 is a mat-like material. At one end of the holding sealing material 12, a convex portion 12a is formed, and at the other end, a concave portion 12b corresponding to the convex portion 12a is formed. The holding sealing material 12 is made of an inorganic fiber material such as a crystalline alumina fiber or a silica-alumina fiber, and the concentrations of impurities of chlorine, sulfur and phosphorus are set to 100 ppm or less, respectively. The holding sealing material 12 is not impregnated with an organic binder such as NBR or SBR. That is, the holding sealing material 12 is an inorganic fiber material having a low impurity concentration.
【0018】金属製パイプ14は円筒形状をなし、例え
ばステンレススチールなどの耐食性に優れた材料を用い
て形成されている。また、この金属製パイプ14の内径
L2は、本体13の直径L1よりも数mm〜十数mm程度大
きく設定されている。The metal pipe 14 has a cylindrical shape and is formed of a material having excellent corrosion resistance, such as stainless steel. The inner diameter L2 of the metal pipe 14 is set to be several mm to several tens mm larger than the diameter L1 of the main body 13.
【0019】次に、このように構成された改質器2の組
付方法を簡単に説明する。まず、保持シール材12を触
媒保持体11に巻き付けた後、凸部12aと凹部12b
とを合わせた状態で両端をテープ15で固定する。Next, a method of assembling the reformer 2 configured as described above will be briefly described. First, after the holding sealing material 12 is wound around the catalyst holding body 11, the convex portions 12a and the concave portions 12b are formed.
Are fixed with tape 15 at both ends.
【0020】続いて、図2に矢印で示すように、本体1
3を金属製パイプ14内に圧入する。これにより、本体
13は、金属製パイプ14との間に隙間なく挿着される
こととなる。このため、後記するメタノールが保持シー
ル材12と金属製パイプ14との間から流出してしまう
ことが防止される。Subsequently, as shown by an arrow in FIG.
3 is pressed into a metal pipe 14. As a result, the main body 13 is inserted into the metal pipe 14 without any gap. Therefore, it is possible to prevent the later-described methanol from flowing out between the holding sealing material 12 and the metal pipe 14.
【0021】そして、金属製パイプ14の一端側をメタ
ノールの貯蔵タンク(図示略)に接続し、他端側を前記
燃料電池1に接続する。次に、このように構成された燃
料電池1及び改質器2の動作を説明する。Then, one end of the metal pipe 14 is connected to a methanol storage tank (not shown), and the other end is connected to the fuel cell 1. Next, the operation of the fuel cell 1 and the reformer 2 configured as described above will be described.
【0022】図1に示すように、まず、炭化水素化合物
の一種であるメタノールが気化された状態で改質器2に
送り込まれる。そして、改質器2は、このメタノールを
触媒保持体11内の触媒に反応させて水素を生成し、そ
の水素を燃料電池1側に送り出す。燃料電池1は、生成
された水素と酸素とを反応させ、その反応により得たエ
ネルギーを電力に変換する。モータ3は、この電力によ
って駆動される。なお、水素と酸素との反応によって生
成された水は車外に排出される。As shown in FIG. 1, first, methanol, which is a kind of hydrocarbon compound, is sent to the reformer 2 in a vaporized state. Then, the reformer 2 reacts the methanol with the catalyst in the catalyst holder 11 to generate hydrogen, and sends the hydrogen to the fuel cell 1 side. The fuel cell 1 reacts generated hydrogen with oxygen, and converts energy obtained by the reaction into electric power. The motor 3 is driven by this electric power. Note that water generated by the reaction between hydrogen and oxygen is discharged outside the vehicle.
【0023】[0023]
【実施例及び比較例】本実施形態においては、保持シー
ル材12に含有される不純物濃度に応じて、以下の表1
に示すように、改質器2によって生成される水素の純度
が変化した。EXAMPLES AND COMPARATIVE EXAMPLES In the present embodiment, the following Table 1 is used according to the impurity concentration contained in the holding sealing material 12.
As shown in FIG. 7, the purity of hydrogen generated by the reformer 2 changed.
【0024】なお、本実施形態においては、改質器2と
して以下のものを用いた。 ・ 触媒保持体11…外径130mm、長さ100mmのコ
ージェライトモノリス。In the present embodiment, the following is used as the reformer 2. -Catalyst holder 11: Cordierite monolith having an outer diameter of 130 mm and a length of 100 mm.
【0025】・ 保持シール材12…厚み25mmの結晶
質アルミナ繊維のマット状物。 ・ 金属製パイプ14…外径φ141mm、板厚1.5mm
のSUS304製。 また、改質器2の流入側には約500℃の気化したメタ
ノールを所定の流量約0.05(m3/min)で通じるこ
とにした。そして、改質器2の流出側から排出される水
素ガスをサンプリングし、常法に従って不純物濃度を測
定し、その平均値を求めた。Holding sealing material 12: A mat-like material of crystalline alumina fiber having a thickness of 25 mm.・ Metal pipe 14: Outside diameter φ141mm, thickness 1.5mm
Made of SUS304. Further, the vaporized methanol at about 500 ° C. is passed through the inflow side of the reformer 2 at a predetermined flow rate of about 0.05 (m 3 / min). Then, hydrogen gas discharged from the outlet side of the reformer 2 was sampled, the impurity concentration was measured according to a conventional method, and the average value was obtained.
【0026】[0026]
【表1】 表1に示すように、「実施例1」においては、不純物と
しての塩素、硫黄及びリンをいずれも50ppm含有する
保持シール材12を用いて水素純度を測定した。すなわ
ち、この「実施例1」においては、不純物を合計で15
0ppm含有する保持シール材12を用いた。その結果、
生成された水素の純度は99.8%となった。[Table 1] As shown in Table 1, in "Example 1," the purity of hydrogen was measured using the holding sealing material 12 containing 50 ppm of chlorine, sulfur, and phosphorus as impurities. That is, in the “Example 1”, the impurities were
The holding sealing material 12 containing 0 ppm was used. as a result,
The purity of the generated hydrogen was 99.8%.
【0027】「実施例2」においては、塩素を135pp
m、硫黄を50ppm、リンを100ppm含有する保持シー
ル材12を用いて水素純度を測定した。すなわち、この
「実施例2」においては、不純物を合計で285ppm含
有する保持シール材12を用いた。その結果、生成され
た水素の純度は98.7%となった。In "Example 2," 135 ppm of chlorine was added.
The hydrogen purity was measured using a holding sealing material 12 containing m, 50 ppm of sulfur and 100 ppm of phosphorus. That is, in the “Example 2”, the holding sealing material 12 containing a total of 285 ppm of impurities was used. As a result, the purity of the generated hydrogen became 98.7%.
【0028】ちなみに、「比較例」においては、塩素を
1.2%、硫黄を0.6%、リンを0.4%含有する保
持シール材12を用いて水素純度を測定した。すなわ
ち、この比較例における保持シール材12は、従来用い
られている保持シール材12であり、2200ppm
(2.2%)の不純物を含有したものである。その結
果、生成された水素の純度は80.3%となった。By the way, in "Comparative Example", hydrogen purity was measured using a holding sealing material 12 containing 1.2% of chlorine, 0.6% of sulfur and 0.4% of phosphorus. That is, the holding sealing material 12 in this comparative example is a holding sealing material 12 conventionally used, and is 2200 ppm.
(2.2%) impurities. As a result, the purity of the generated hydrogen was 80.3%.
【0029】これらの結果、前記「実施例1,2」にお
いては、保持シール材12として低不純物濃度の無機繊
維材料を用いることにより、生成される水素の純度が高
く維持されていることが判る。As a result, in Examples 1 and 2, it is found that the purity of generated hydrogen is kept high by using an inorganic fiber material having a low impurity concentration as the holding sealing material 12. .
【0030】特に、「実施例1」の結果から、塩素、硫
黄及びリンの含有濃度をそれぞれ100ppm以下とする
ことにより、ほぼ純粋な水素が生成されることが判る。
また、「実施例2」の結果から、塩素、硫黄及びリンの
含有濃度が合計で300ppm以下であっても、純粋度の
高い水素が生成されることが判る。In particular, from the results of "Example 1", it can be seen that almost pure hydrogen is produced by setting the concentration of chlorine, sulfur and phosphorus to 100 ppm or less, respectively.
Further, from the results of “Example 2”, it can be seen that even when the total concentration of chlorine, sulfur and phosphorus is 300 ppm or less, highly pure hydrogen is generated.
【0031】なお、「比較例」においては不純物濃度が
2.2%の保持シール材12が用いられ、これにより8
0.3%の純粋度の水素が生成されている。このため、
不純物濃度が1%未満の保持シール材12を用いれば、
90%以上の純粋度の水素を生成することができると推
測される。In the comparative example, the holding sealing material 12 having an impurity concentration of 2.2% was used.
0.3% pure hydrogen has been produced. For this reason,
If the holding sealing material 12 having an impurity concentration of less than 1% is used,
It is speculated that hydrogen with a purity of 90% or more can be produced.
【0032】したがって、本実施形態によれば以下のよ
うな効果を得ることができる。 (1)保持シール材12として、塩素、硫黄及びリンの
不純物の含有濃度が低い無機繊維材料を用いることによ
り、改質器2から生成される水素を高純度に維持するこ
とができる。したがって、燃料電池1の発電効率の低下
を確実に防止することができる。Therefore, according to the present embodiment, the following effects can be obtained. (1) By using an inorganic fiber material having a low concentration of impurities of chlorine, sulfur and phosphorus as the holding sealing material 12, hydrogen generated from the reformer 2 can be maintained at high purity. Therefore, a decrease in the power generation efficiency of the fuel cell 1 can be reliably prevented.
【0033】(2)保持シール材12に含有される塩
素、硫黄及びリンの不純物の含有濃度を、1%未満とす
ることにより、改質器2から生成される水素を確実に高
純度に維持することができる。(2) By setting the concentration of chlorine, sulfur and phosphorus impurities contained in the holding sealing material 12 to less than 1%, the hydrogen generated from the reformer 2 is maintained at a high purity. can do.
【0034】(3)保持シール材12に含有される塩
素、硫黄及びリンの不純物の含有濃度を、それぞれ10
0ppm以下とすることにより、改質器2から生成される
水素をさらに確実に高純度に維持することができる。ま
た、前記不純物の含有濃度を、合計で300ppm以下と
することによっても、同様の効果を得ることができる。(3) The concentration of chlorine, sulfur and phosphorus impurities contained in the holding sealing material 12 is set to 10
By setting the content to 0 ppm or less, the hydrogen generated from the reformer 2 can be more reliably maintained at a high purity. Similar effects can be obtained by setting the concentration of the impurities to 300 ppm or less in total.
【0035】なお、本発明の実施形態は以下のように変
更してもよい。 ・ 炭化水素化合物は、メタノールに限定されるもので
はない。すなわち、エタノール、プロパノール、ブタノ
ール、メタン、エタン、プロパン、ブタン等のように、
その分子構造中に、塩素等のハロゲン、硫黄、リン等を
含まない各種炭化水素化合物であってもよい。The embodiment of the present invention may be modified as follows. -The hydrocarbon compound is not limited to methanol. That is, like ethanol, propanol, butanol, methane, ethane, propane, butane, etc.
Various hydrocarbon compounds which do not contain halogen such as chlorine, sulfur, phosphorus and the like in the molecular structure may be used.
【0036】・ 触媒保持体11は、コージェライト、
アルミナに限定されるものではない。すなわち、炭化珪
素や窒化珪素等でも適用可能である。 ・ 触媒保持体11はハニカム状に限定されるものでは
なく、多孔質であればよい。The catalyst support 11 is made of cordierite,
It is not limited to alumina. That is, silicon carbide, silicon nitride, and the like are also applicable. The catalyst support 11 is not limited to a honeycomb shape, but may be porous.
【0037】・ 金属製パイプ14は、単一の部材から
なる筒に限定されるものではない。すなわち、複数の部
材からなるもの、すなわち二分割されたシェル状のパイ
プ片を組み合わせて形成してもよい。また、この金属製
パイプ14の断面形状は、前記実施形態のような真円形
状に限定されず、例えば楕円形状や多角形状であっても
よい。勿論この金属パイプの形状に合わせて触媒保持体
11の外形状を変更してもよい。The metal pipe 14 is not limited to a cylinder made of a single member. That is, it may be formed by combining a plurality of members, that is, two-piece shell-shaped pipe pieces. Further, the cross-sectional shape of the metal pipe 14 is not limited to a perfect circular shape as in the above embodiment, and may be, for example, an elliptical shape or a polygonal shape. Of course, the outer shape of the catalyst holder 11 may be changed according to the shape of the metal pipe.
【0038】・ 前記実施形態では、塩素、硫黄及びリ
ンの濃度がそれぞれ100ppm以下となるように設定し
ているが、これらは合計で300ppm以下であってもよ
い。次に、特許請求の範囲に記載された技術的思想のほ
かに、前述した実施形態によって把握される技術的思想
を以下に列挙する。In the above embodiment, the concentrations of chlorine, sulfur and phosphorus are set to be 100 ppm or less, respectively. However, these may be 300 ppm or less in total. Next, in addition to the technical ideas described in the claims, technical ideas grasped by the above-described embodiments will be listed below.
【0039】(1) 請求項1または請求項2に記載の
燃料電池用改質器において、前記マット状物中における
塩素、硫黄及びリンの濃度は、それぞれ100ppm以下
であることを特徴とする燃料電池用改質器。(1) The fuel cell reformer according to claim 1 or 2, wherein the concentrations of chlorine, sulfur and phosphorus in the mat-like material are each 100 ppm or less. Battery reformer.
【0040】この技術的思想(1)に記載の発明によれ
ば、改質器から生成される水素の純度をさらに高く確実
に維持することができる。 (2) 請求項1〜3、技術的思想(1)のいずれか1
項に記載の燃料電池用改質器において、前記マット状物
は、結晶質アルミナ繊維及びシリカ−アルミナ繊維から
選び出される少なくとも1種類の無機繊維材料であるこ
とを特徴とする燃料電池用改質器。According to the invention described in the technical concept (1), the purity of hydrogen generated from the reformer can be maintained even higher. (2) Any one of claims 1 to 3 and the technical idea (1)
The fuel cell reformer according to claim 1, wherein the mat-like material is at least one kind of inorganic fiber material selected from crystalline alumina fibers and silica-alumina fibers. vessel.
【0041】(3) 請求項1〜3、技術的思想
(1),(2)のいずれか1項に記載の燃料電池用改質
器において、前記触媒保持体は、コージェライト、アル
ミナ、炭化珪素、または窒化珪素からなる多孔質のセラ
ミック焼結体であることを特徴とする燃料電池用改質
器。(3) In the reformer for a fuel cell according to any one of claims 1 to 3, and the technical ideas (1) and (2), the catalyst holder is made of cordierite, alumina, carbonized A reformer for a fuel cell, which is a porous ceramic sintered body made of silicon or silicon nitride.
【0042】(4) 請求項1〜3、技術的思想(1)
〜(3)のいずれか1項に記載の燃料電池用改質器にお
いて、前記触媒保持体は、ハニカム形状に成形され、そ
の外形状が略円柱形状をなすことを特徴とする燃料電池
用改質器。(4) Claims 1 to 3, Technical idea (1)
The reformer for a fuel cell according to any one of claims 1 to 3, wherein the catalyst holder is formed in a honeycomb shape, and an outer shape thereof is substantially cylindrical. Porcelain.
【0043】(5) 請求項1〜3、技術的思想(1)
〜(4)のいずれか1項に記載の燃料電池用改質器にお
いて、前記金属製パイプは、筒状または二分割されたシ
ェル状のパイプ片からなることを特徴とする燃料電池用
改質器。(5) Claims 1 to 3, Technical idea (1)
The reformer for a fuel cell according to any one of (1) to (4), wherein the metal pipe is formed of a tubular or two-piece shell-shaped pipe piece. vessel.
【0044】(6) 炭化水素化合物と反応して水素を
生成させる触媒を保持する触媒保持体と、同触媒保持体
を収容する金属製パイプとの間に配置されて前記触媒保
持体を保持する燃料電池用改質器の保持シール材におい
て、当該保持シール材は、低不純物濃度の無機繊維材料
からなり、かつ樹脂未含浸のマット状物であることを特
徴とする燃料電池用改質器の保持シール材。(6) A catalyst holder for holding a catalyst which reacts with a hydrocarbon compound to generate hydrogen and a metal pipe for holding the catalyst holder for holding the catalyst holder. The holding sealing material for a fuel cell reformer, wherein the holding sealing material is made of an inorganic fiber material having a low impurity concentration, and is a resin-impregnated mat-like material. Holding sealing material.
【0045】[0045]
【発明の効果】以上詳述したように、請求項1に記載の
発明によれば、生成される水素を高純度に維持すること
ができる。このため、水素純度の低下に起因する燃料電
池の発電効率の低下を確実に防止することができる。As described in detail above, according to the first aspect of the present invention, the generated hydrogen can be maintained at a high purity. Therefore, it is possible to reliably prevent a decrease in the power generation efficiency of the fuel cell due to a decrease in the hydrogen purity.
【0046】請求項2に記載の発明によれば、生成され
る水素をより確実に高純度に維持することができる。請
求項3に記載の発明によれば、生成される水素をさらに
確実に高純度に維持することができる。According to the second aspect of the present invention, the generated hydrogen can be more reliably maintained at a high purity. According to the third aspect of the invention, the generated hydrogen can be more reliably maintained at a high purity.
【図面の簡単な説明】[Brief description of the drawings]
【図1】本発明に係る燃料電池用改質器を用いた一実施
形態の燃料電池のブロック図。FIG. 1 is a block diagram of a fuel cell according to an embodiment using a fuel cell reformer according to the present invention.
【図2】同実施形態の燃料電池用改質器を示す斜視図。FIG. 2 is a perspective view showing the fuel cell reformer of the embodiment.
1…燃料電池、2…改質器、11…触媒保持体、12…
保持シール材、13…本体、14…金属製パイプ。DESCRIPTION OF SYMBOLS 1 ... Fuel cell, 2 ... Reformer, 11 ... Catalyst holder, 12 ...
Holding seal material, 13: body, 14: metal pipe.
Claims (3)
せる触媒を保持する触媒保持体と、同触媒保持体を収容
する金属製パイプと、前記触媒保持体及び前記金属製パ
イプの間に配置されて前記触媒保持体を保持する保持シ
ール材とを備える燃料電池用改質器において、 前記保持シール材は、低不純物濃度の無機繊維材料から
なり、かつ樹脂未含浸のマット状物であることを特徴と
する燃料電池用改質器。1. A catalyst holder for holding a catalyst for producing hydrogen by reacting with a hydrocarbon compound, a metal pipe for housing the catalyst holder, and a metal pipe disposed between the catalyst holder and the metal pipe. And a holding seal material holding the catalyst holding body, wherein the holding seal material is made of an inorganic fiber material having a low impurity concentration and is a resin-impregnated mat-like material. A reformer for a fuel cell, comprising:
いて、 前記マット状物中における不純物濃度は、1%未満であ
ることを特徴とする燃料電池用改質器。2. The reformer for a fuel cell according to claim 1, wherein an impurity concentration in the mat-like material is less than 1%.
池用改質器において、 前記マット状物中における塩素、硫黄及びリンの濃度
は、300ppm以下であることを特徴とする燃料電池用
改質器。3. The fuel cell reformer according to claim 1, wherein the concentration of chlorine, sulfur and phosphorus in the mat-like material is 300 ppm or less. Reformer.
Priority Applications (1)
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JP02767999A JP4362159B2 (en) | 1999-02-04 | 1999-02-04 | Holding seal material for fuel cell reformer |
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---|---|---|---|
JP02767999A JP4362159B2 (en) | 1999-02-04 | 1999-02-04 | Holding seal material for fuel cell reformer |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002068709A (en) * | 2000-09-01 | 2002-03-08 | Ibiden Co Ltd | Reformer for fuel cells |
JP2003342430A (en) * | 2002-05-16 | 2003-12-03 | Bayer Inc | Halogen- and sulfur-free molded article comprising peroxide curable compound of butyl rubber |
KR100542911B1 (en) * | 2003-10-25 | 2006-01-11 | 한국과학기술연구원 | POX reforming structured catalyst of gasoline for fuel cell powered vehicle application, and method for preparing the structured catalyst |
JP2007054826A (en) * | 2005-07-13 | 2007-03-08 | Boc Group Inc:The | Reactor sealing method |
WO2008026803A1 (en) * | 2006-08-28 | 2008-03-06 | Korea Institute Of Science And Technology | Sealing composite for flat solid oxide fuel cell stack having high fracture resistance and the fabrication method thereof |
JP2010215468A (en) * | 2009-03-18 | 2010-09-30 | Ngk Insulators Ltd | Reactor |
-
1999
- 1999-02-04 JP JP02767999A patent/JP4362159B2/en not_active Expired - Lifetime
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002068709A (en) * | 2000-09-01 | 2002-03-08 | Ibiden Co Ltd | Reformer for fuel cells |
JP4491939B2 (en) * | 2000-09-01 | 2010-06-30 | イビデン株式会社 | Fuel cell reformer |
JP2003342430A (en) * | 2002-05-16 | 2003-12-03 | Bayer Inc | Halogen- and sulfur-free molded article comprising peroxide curable compound of butyl rubber |
KR100542911B1 (en) * | 2003-10-25 | 2006-01-11 | 한국과학기술연구원 | POX reforming structured catalyst of gasoline for fuel cell powered vehicle application, and method for preparing the structured catalyst |
JP2007054826A (en) * | 2005-07-13 | 2007-03-08 | Boc Group Inc:The | Reactor sealing method |
WO2008026803A1 (en) * | 2006-08-28 | 2008-03-06 | Korea Institute Of Science And Technology | Sealing composite for flat solid oxide fuel cell stack having high fracture resistance and the fabrication method thereof |
JP2010215468A (en) * | 2009-03-18 | 2010-09-30 | Ngk Insulators Ltd | Reactor |
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