JP2002050381A - Fuel cell reformer and its manufacturing method - Google Patents

Fuel cell reformer and its manufacturing method

Info

Publication number
JP2002050381A
JP2002050381A JP2000234771A JP2000234771A JP2002050381A JP 2002050381 A JP2002050381 A JP 2002050381A JP 2000234771 A JP2000234771 A JP 2000234771A JP 2000234771 A JP2000234771 A JP 2000234771A JP 2002050381 A JP2002050381 A JP 2002050381A
Authority
JP
Japan
Prior art keywords
metal shell
fuel cell
catalyst
reformer
holding
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
Application number
JP2000234771A
Other languages
Japanese (ja)
Other versions
JP4810721B2 (en
Inventor
Masanao Yasugata
政直 安形
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ibiden Co Ltd
Original Assignee
Ibiden Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Ibiden Co Ltd filed Critical Ibiden Co Ltd
Priority to JP2000234771A priority Critical patent/JP4810721B2/en
Publication of JP2002050381A publication Critical patent/JP2002050381A/en
Application granted granted Critical
Publication of JP4810721B2 publication Critical patent/JP4810721B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

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  • Hydrogen, Water And Hydrids (AREA)
  • Fuel Cell (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a reformer for a fuel cell in which installation work of a catalyst carrier and a carrying seal material into the metal shell is easy and binder combustion gas is not generated and its manufacturing method. SOLUTION: This is a manufacturing method of a fuel cell reformer 4 which comprises a catalyst carrier 3 carrying a reforming catalyst for reforming a hydrocarbon compound into hydrogen, a metal shell 2 covering the outer side of the catalyst carrier 3, and a carrying seal material 1 arranged between these two. The manufacturing method comprises a step in which the catalyst carrier 3 covered by the carrying seal material 1 is inserted in a pipe-form metal shell 2 that has an initial inside diameter D larger than the product inner diameter 'd' of the metal shell 2, and a step in which a spinning processing is made at least on the installation portion where the above catalyst carrier 3 is located in the metal shell 2, and thereby the initial inside diameter D of the installation portion is reduced to the above product inner diameter 'd'.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【技術分野】本発明は,例えば自動車に搭載する燃料電
池用改質器,及びその製造方法に関し,特に保持シール
材を触媒保持体と金属シエルとの間に組み付ける方法に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a reformer for a fuel cell mounted on an automobile, for example, and a method of manufacturing the same, and more particularly, to a method of assembling a holding seal material between a catalyst holder and a metal shell.

【0002】[0002]

【従来技術】水素をエネルギー源として用いる燃料電池
は,これに水素を供給するための燃料電池用改質器を併
設することがある。この燃料電池用改質器は,メタノー
ル,メタン,ブタン等の炭化水素化合物を水素に改質す
る触媒を保持する触媒保持体と,該触媒保持体の外方を
覆う金属シエルと,触媒保持体と金属シエルとの間に配
置される保持シール材とを具備している(後述する図3
参照)。
2. Description of the Related Art A fuel cell using hydrogen as an energy source is sometimes provided with a fuel cell reformer for supplying hydrogen thereto. This fuel cell reformer includes a catalyst holder for holding a catalyst for reforming a hydrocarbon compound such as methanol, methane, and butane to hydrogen, a metal shell for covering the outside of the catalyst holder, and a catalyst holder. And a holding sealing material disposed between the metal shell and the metal shell (see FIG. 3 described later).
reference).

【0003】上記保持シール材は,主としてセラミック
繊維などの無機質繊維マットからなる。上記保持シール
材は,触媒保持体が振動等により触媒保持体と当接した
際に,触媒保持体が破損することを防止するため,及び
触媒保持体と金属シエルとの間から上記炭化水素化合物
が漏洩することを防止するために配置されている。
The holding sealing material is mainly made of an inorganic fiber mat such as a ceramic fiber. The holding sealing material is used to prevent the catalyst holding body from being damaged when the catalyst holding body comes into contact with the catalyst holding body due to vibration or the like, and to prevent the hydrocarbon compound from being provided between the catalyst holding body and the metal shell. Is arranged to prevent leakage.

【0004】[0004]

【解決しようとする課題】しかしながら,上記保持シー
ル材は,上記機能を果すため,クッション性を有し,嵩
高である。そのため,保持シール材を触媒保持体ととも
に金属シエル内に装着するときに,保持シール材が両者
の間の適正位置に位置し難く,装着性が低下するおそれ
がある。そこで,保持シール材にバインダーを含浸させ
て保持シール材の嵩高性を抑え,その状態で金属シエル
内に圧入することが考えられる。しかし,この場合に
は,燃料電池用改質器の使用時にバインダーが燃焼して
バインダー燃焼ガスが発生し,これが水素ガス中に混入
するおそれがある。
However, the above-mentioned holding sealing material has a cushioning property and is bulky in order to fulfill the above-mentioned functions. Therefore, when the holding sealing material is mounted in the metal shell together with the catalyst holding body, it is difficult for the holding sealing material to be located at an appropriate position between the two, and there is a possibility that the mounting property may be reduced. Therefore, it is conceivable to impregnate the holding sealing material with a binder to suppress the bulkiness of the holding sealing material, and then press-fit the holding sealing material into the metal shell. However, in this case, when the fuel cell reformer is used, the binder burns to generate binder combustion gas, which may be mixed into the hydrogen gas.

【0005】本発明は,かかる問題点に鑑み,金属シエ
ル内への触媒保持体及び保持シール材の装着作業がしや
すく,バインダー燃焼ガスの発生がない,燃料電池用改
質器及びその製造方法を提供しようとするものである。
SUMMARY OF THE INVENTION In view of the above problems, the present invention makes it easy to mount a catalyst holder and a holding seal material in a metal shell, and does not generate a binder combustion gas. It is intended to provide.

【0006】[0006]

【課題の解決手段】請求項1の発明は,炭化水素化合物
を水素に改質する改質触媒を保持する触媒保持体と,該
触媒保持体の外方を覆う金属シエルと,上記触媒保持体
と金属シエルとの間に配置される保持シール材とを有す
る燃料電池用改質器を製造する方法において,上記触媒
保持体を,上記保持シール材により被覆する工程
と,,,上記保持シール材により被覆された触媒保持体
を,上記燃料電池用改質器における金属シエルの製品内
側径よりも大きい初期内径を有するパイプ状の金属シエ
ルの中に挿入する工程と,上記金属シエルにおける少な
くとも上記触媒保持体が位置する配設部分に,スピニン
グ加工を施して,該配設部分の初期内径を上記製品内側
径まで小さくする工程とからなることを特徴とする燃料
電池用改質器の製造方法である。
According to the first aspect of the present invention, there is provided a catalyst holder for holding a reforming catalyst for reforming a hydrocarbon compound into hydrogen, a metal shell for covering the outside of the catalyst holder, and the catalyst holder. A method of manufacturing a reformer for a fuel cell having a holding seal material disposed between a metal shell and a metal shell; a step of coating the catalyst holding body with the holding seal material; Inserting the catalyst holder coated with a metal shell into a pipe-shaped metal shell having an initial inner diameter larger than the inner diameter of the metal shell in the fuel cell reformer; and at least the catalyst in the metal shell. Spinning a portion where the holding body is located to reduce the initial inner diameter of the portion to the inside diameter of the product, a method for manufacturing a reformer for a fuel cell. A.

【0007】本発明においては,触媒保持体を保持シー
ル材により被覆し,これを製品内側径よりも大きい初期
内径のパイプ状の金属シエルの中に挿入した後,該触媒
保持体が位置する配設部分にスピニング加工を施す。そ
のため,このスピニング加工により,触媒保持体を挿入
した当初のパイプ状の金属シエルの外径が小さくなり,
それに伴い該金属シエルの初期内径も小さくなる。つま
り,金属シエルにおける触媒保持体挿入時の初期内径
が,上記スピニング加工により小さくなり,燃料電池用
改質器における金属シエルの製品内側径が上記初期内径
よりも小さくなる。
In the present invention, the catalyst holding body is covered with a holding sealing material, and is inserted into a pipe-shaped metal shell having an initial inner diameter larger than the inner diameter of the product. Spinning is applied to the set part. Due to this spinning, the outer diameter of the pipe-shaped metal shell into which the catalyst holder was inserted was reduced,
Accordingly, the initial inner diameter of the metal shell also becomes smaller. That is, the initial inner diameter of the metal shell when the catalyst holder is inserted is reduced by the spinning process, and the inner diameter of the metal shell in the fuel cell reformer is smaller than the initial inner diameter.

【0008】また,これにより触媒保持体と金属シエル
の間に充填されている保持シール材も金属シエルの内壁
により圧縮される。そのため,触媒保持体は,適度な面
圧の保持シール材によって保持されることになる。上記
スピニング加工は,しぼり加工の一種で,例えば金属シ
エルまたは成形用ローラの一方を回転させながら,金属
シエルに成形用ローラを押し付けることにより,金属シ
エルを塑性変形させる加工である。
[0008] Accordingly, the holding sealing material filled between the catalyst holding body and the metal shell is also compressed by the inner wall of the metal shell. Therefore, the catalyst holder is held by the holding seal material having an appropriate surface pressure. The spinning process is a kind of squeezing process, for example, a process of plastically deforming a metal shell by pressing a forming roller against the metal shell while rotating one of the metal shell and the forming roller.

【0009】以上のように,本発明においては,金属シ
エルの中に保持シール材で被覆した触媒保持体を配設す
るに当って,製品内側径よりも大きい初期内径の金属シ
エルの中に保持シール材を挿入し,その後上記スピニン
グ加工をしている。そのため,金属シエル内への触媒保
持体の挿入が容易となり,またスピニング加工によって
保持シール材の適度な面圧で金属シエルが保持される。
As described above, in the present invention, in disposing the catalyst support covered with the holding sealing material in the metal shell, the catalyst support is held in the metal shell having an initial inner diameter larger than the inner diameter of the product. After inserting the sealing material, the above spinning process is performed. Therefore, the insertion of the catalyst holder into the metal shell is facilitated, and the metal shell is held at an appropriate surface pressure of the holding sealing material by spinning.

【0010】また,本発明においては,上記方法を採用
するので,保持シール材にバインダーを含浸させて,嵩
高性を抑制し,薄肉化する工程も必要ない。また,その
ため,触媒保持体によって改質された改質ガス,特に水
素ガス中にバインダー燃焼ガスが混入することもない。
In the present invention, since the above method is employed, there is no need for a step of impregnating the holding sealing material with a binder to suppress bulkiness and reduce the thickness. Therefore, the binder combustion gas does not mix in the reformed gas reformed by the catalyst holder, particularly in the hydrogen gas.

【0011】次に,請求項2の発明のように,上記保持
シール材は,バインダーが含浸されていない無機質繊維
マットであることが好ましい。これにより,保持シール
材からバインダー燃焼ガスが排出されることがないと共
に,耐熱性が向上する。
Next, it is preferable that the holding sealing material is an inorganic fiber mat not impregnated with a binder. Thereby, the binder combustion gas is not discharged from the holding sealing material, and the heat resistance is improved.

【0012】上記無機質繊維マットは,アルミナまたは
シリカを含有する無機質繊維からなることが好ましい。
これにより,無機質繊維マットの耐熱性が一層向上す
る。特に,無機質繊維マットは,70〜100重量%の
アルミナ繊維を含有していることが好ましい。なお,か
かるアルミナ繊維としては,アルミナ比率が60重量%
以上であることが好ましい。これにより,高温時の弾性
力が高くなり,金属シエルと触媒保持体との熱膨張差を
吸収することができ,触媒保持体を保持する力が高ま
る。
It is preferable that the inorganic fiber mat is made of inorganic fibers containing alumina or silica.
Thereby, the heat resistance of the inorganic fiber mat is further improved. In particular, the inorganic fiber mat preferably contains 70 to 100% by weight of alumina fibers. The alumina fiber has an alumina ratio of 60% by weight.
It is preferable that it is above. As a result, the elastic force at high temperatures is increased, the difference in thermal expansion between the metal shell and the catalyst holder can be absorbed, and the force for holding the catalyst holder increases.

【0013】無機質繊維マットには,ニードルパンチン
グ処理が施されていることが好ましい。これにより,繊
維同士が絡み合い,マットの層間強度が向上するため,
金属シエル内へ挿入することが容易となる。
The inorganic fiber mat is preferably subjected to a needle punching treatment. As a result, the fibers are entangled and the interlayer strength of the mat is improved.
Insertion into the metal shell becomes easy.

【0014】次に,請求項3の発明のように,上記無機
質繊維マットは,その中のAl23,SiO2以外の物
質,つまり不純物が1重量%未満であることが好まし
い。この場合には,燃料電池用改質器において生成され
る水素を高純度に維持することができ,燃料電池の発電
効率を高めることができる。上記不純物が1重量%以上
の場合には,燃料電池用改質器の使用中に,保持シール
材中から徐々に不純物が改質ガス中に混入し,燃料電池
に用いる水素ガスを汚染し,燃料電池の発電効率を低下
させるおそれがある。上記不純物としては,塩素,硫
黄,リンなどがある。
Next, as in the third aspect of the present invention, the inorganic fiber mat preferably contains less than 1% by weight of substances other than Al 2 O 3 and SiO 2 , that is, impurities. In this case, the hydrogen generated in the fuel cell reformer can be maintained at a high purity, and the power generation efficiency of the fuel cell can be increased. When the above-mentioned impurity is 1% by weight or more, during use of the reformer for a fuel cell, the impurity is gradually mixed into the reformed gas from the holding sealing material and contaminates the hydrogen gas used for the fuel cell. The power generation efficiency of the fuel cell may be reduced. Examples of the impurities include chlorine, sulfur, and phosphorus.

【0015】次に,請求項4の発明のように,無機質繊
維マットはその中の塩素,硫黄又はリンの1種以上が合
計で300ppm未満であることが好ましい。この場合
には,燃料電池の発電効率を高くすることができる。上
記の塩素,硫黄,リンの1種以上の合計が300ppm
以上含有されている場合には,上記のごとく,燃料電池
用改質器の使用中に上記塩素等の電池作用有害物質が水
素中に混入し,燃料電池における電気化学作用を阻害
し,燃料電池の発電効率を低下させるおそれがある。
Next, as in the invention of claim 4, the inorganic fiber mat preferably has a total of less than 300 ppm of one or more of chlorine, sulfur and phosphorus therein. In this case, the power generation efficiency of the fuel cell can be increased. The total of one or more of the above chlorine, sulfur and phosphorus is 300 ppm
If it is contained, as described above, during the use of the fuel cell reformer, the above-mentioned cell-harmful substances such as chlorine enter the hydrogen, hindering the electrochemical action of the fuel cell, Power generation efficiency may be reduced.

【0016】次に,請求項5の発明のように,スピニン
グ加工前の上記保持シール材の厚みは,4〜12mmで
あることが好ましい。4mm未満では,金属シエルの内
径を小さくできる厚みが小さく,スピニング加工の際に
触媒保持体が破損するおそれがある。一方,12mmを
超える場合には,保持シール材が所望の充填密度になる
まで金属シエルの内径を小さくする前に,金属シエルが
破損するおそれがある。
Next, as in the invention of claim 5, the thickness of the holding sealing material before spinning is preferably 4 to 12 mm. If it is less than 4 mm, the thickness of the metal shell that can reduce the inner diameter is small, and the catalyst holder may be damaged during spinning. On the other hand, if it exceeds 12 mm, the metal shell may be damaged before the inner diameter of the metal shell is reduced until the holding sealing material has a desired packing density.

【0017】請求項6の発明のように,スピニング加工
後の上記保持シール材の充填密度は,0.20〜0.6
0g/cmであることが好ましい。0.20g/cm
未満では,保持シール材による触媒保持体の保持力が
低下する。一方,0.60g/cmを超える場合に
は,保持シール材の中の繊維が折れ,反発力が低下し
て,触媒保持体を保持する性能が低下するおそれがあ
る。
According to a sixth aspect of the present invention, the packing density of the holding sealing material after spinning is 0.20 to 0.6.
It is preferably 0 g / cm 3 . 0.20g / cm
If it is less than 3 , the holding force of the holding member by the holding sealing material decreases. On the other hand, if it exceeds 0.60 g / cm 3 , the fibers in the holding sealing material may be broken, the repulsion may be reduced, and the performance of holding the catalyst holding body may be reduced.

【0018】次に,請求項7の発明は,炭化水素化合物
を水素に改質する改質触媒を保持する触媒担持体と,該
触媒保持体の外方を覆う金属シエルと,上記触媒保持体
と上記金属シエルとの間に配置される保持シール材とか
ら構成されている燃料電池用改質器であって,上記金属
シエルにおける少なくとも上記触媒保持体が位置する配
設部分には,スピニング加工が施されていることを特徴
とする燃料電池用改質器である。
Next, a seventh aspect of the present invention relates to a catalyst carrier for holding a reforming catalyst for reforming a hydrocarbon compound into hydrogen, a metal shell for covering the outside of the catalyst carrier, and the catalyst carrier. A fuel cell reformer comprising a holding seal material disposed between the metal shell and the metal shell, wherein at least a portion of the metal shell where the catalyst holder is located is provided with a spinning process. This is a reformer for a fuel cell characterized by having been subjected to the following.

【0019】本発明においては,金属シエルにおける上
記触媒保持体の配設部分にスピニング加工が施され,金
属シエルの内径が当初より縮小されているため,保持シ
ール材の適度な面圧により触媒保持体を保持できる。
In the present invention, the portion of the metal shell where the catalyst holding member is disposed is subjected to spinning, and the inner diameter of the metal shell is reduced from the beginning, so that the catalyst holding is performed by an appropriate surface pressure of the holding sealing material. Can hold body.

【0020】次に,請求項8の発明のように,上記保持
シール材は,バインダーが含浸されていない無機質繊維
マットであることが好ましい。この場合には,保持シー
ル材からバインダー燃焼ガスが排出されることがないと
共に耐熱性が向上する。
Next, it is preferable that the holding sealing material is an inorganic fiber mat not impregnated with a binder. In this case, the binder combustion gas is not discharged from the holding sealing material, and the heat resistance is improved.

【0021】次に,請求項9の発明のように,上記無機
質繊維マットは,その中のAl23,SiO2以外の物
質,つまり不純物が1重量%未満であることが好まし
い。この場合には,請求項3の発明と同様に,燃料電池
の発電効率を高めることができる。
Next, as in the ninth aspect of the present invention, the inorganic fiber mat preferably contains less than 1% by weight of substances other than Al 2 O 3 and SiO 2 , that is, impurities. In this case, the power generation efficiency of the fuel cell can be increased, as in the third aspect of the invention.

【0022】次に,請求項10の発明のように,無機質
繊維マットはその中の塩素,硫黄又はリンの1種以上が
合計で300ppm未満であることが好ましい。この場
合には,請求項4の発明と同様に,塩素等の電池作用有
害物質が水素中に殆ど混入しないので,燃料電池の発電
効率を高めることができる。
Next, as in the tenth aspect of the present invention, the inorganic fiber mat preferably contains at least one of chlorine, sulfur and phosphorus in the inorganic fiber mat in a total of less than 300 ppm. In this case, similar to the fourth aspect of the present invention, since harmful substances acting on the cell such as chlorine are hardly mixed into the hydrogen, the power generation efficiency of the fuel cell can be improved.

【0023】上記において,上記炭化水素化合物として
は,メタノール,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,ブタンなどが用いられ
る。また,上記触媒保持体は,コージエライト,アルミ
ナ,炭素珪素,窒化珪素等のセラミックスで作製された
ハニカム等のモノリスの通気性多孔質体が用いられる。
また,金属シエルは,ステンレス鋼等の金属を用いた,
円形,楕円形などのパイプを用いる。また,上記触媒保
持体に担持する触媒は,使用する炭化水素化合物の改質
に応じたものを用いるが,例えば炭化水素化合物として
メタノールを用いる場合には,触媒として銅化合物等を
用いる。
In the above, methanol, ethanol, propanol, butanol, methane, ethane, propane, butane and the like are used as the hydrocarbon compound. Further, as the catalyst holder, a gas-permeable porous body of a monolith such as a honeycomb made of ceramics such as cordierite, alumina, carbon silicon, and silicon nitride is used.
The metal shell was made of metal such as stainless steel.
Use circular or elliptical pipes. As the catalyst supported on the catalyst holder, a catalyst corresponding to the reforming of the hydrocarbon compound used is used. For example, when methanol is used as the hydrocarbon compound, a copper compound or the like is used as the catalyst.

【0024】[0024]

【発明の実施の形態】実施形態例1 本発明の実施形態例に係る燃料電池用改質器の製造方法
について,図1〜図3を用いて説明する。本例の燃料電
池用改質器4は,図1に示すごとく,炭化水素化合物を
水素に改質する改質触媒を保持する触媒保持体3と,該
触媒保持体3の外方を覆う金属シエル2と,上記触媒保
持体3と金属シエル2との間に配置される保持シール材
1とからなる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiment 1 A method for manufacturing a fuel cell reformer according to an embodiment of the present invention will be described with reference to FIGS. As shown in FIG. 1, the fuel cell reformer 4 of the present embodiment includes a catalyst holder 3 for holding a reforming catalyst for reforming a hydrocarbon compound into hydrogen, and a metal covering the outside of the catalyst holder 3. It comprises a shell 2 and a holding sealing material 1 disposed between the catalyst holding body 3 and the metal shell 2.

【0025】そして,上記改質器を製造するに当って
は,図1〜図3に示すごとく,まず,触媒保持体3を,
保持シール材1により被覆する工程(図2a,b)と,
上記保持シール材1により被覆された触媒保持体3(図
2b)を,上記燃料電池用改質器における金属シエル2
の製品内側径dよりも大きい初期内径Dを有するパイプ
状の金属シエル2の中に挿入する工程(図2c,d,図
3a)を行なう。次に,上記金属シエル2における少な
くとも上記触媒保持体3が位置する配設部分L(図3
b)に,スピニング加工を施して,該配設部分Lの初期
内径Dを上記製品内側径dまで小さくする工程を行な
う。
In manufacturing the reformer, first, as shown in FIGS.
A step of covering with the holding sealing material 1 (FIGS. 2a and 2b);
The catalyst holding body 3 (FIG. 2b) covered with the holding sealing material 1 is connected to the metal shell 2 in the fuel cell reformer.
(FIGS. 2C, 2D, and 3A) of inserting into a pipe-shaped metal shell 2 having an initial inner diameter D larger than the product inner diameter d. Next, an arrangement portion L of the metal shell 2 where at least the catalyst holder 3 is located (FIG.
In step b), a step of performing spinning to reduce the initial inner diameter D of the disposition portion L to the product inner diameter d is performed.

【0026】本例において,上記触媒保持体3は,セラ
ミックの一種であるコーディエライト製である。触媒保
持体3は,図1に示すごとく,多数のセル31の集合体
からなるモノリスのハニカム構造体である。上記セル3
1は,断面6角形状の通路であり,ハニカム壁33の間
に形成されている。そして,上記セル31の間に,ガス
状態の炭化水素化合物を通過させる。この間に,炭化水
素化合物は触媒作用によって水素を主成分とする改質ガ
スに改質される。
In this embodiment, the catalyst holder 3 is made of cordierite which is a kind of ceramic. As shown in FIG. 1, the catalyst holder 3 is a monolith honeycomb structure composed of an aggregate of many cells 31. Cell 3 above
Reference numeral 1 denotes a passage having a hexagonal cross section, which is formed between the honeycomb walls 33. Then, a gaseous hydrocarbon compound is passed between the cells 31. During this time, the hydrocarbon compound is reformed into a reformed gas containing hydrogen as a main component by a catalytic action.

【0027】上記燃料電池用改質器4には,入口側に炭
化水素化合物としてのメタノールを貯蔵した原料タンク
9が入口パイプ91を介して接続されている。一方,燃
料電池用改質器4の出口側には水素を含む改質ガスを燃
料電池5へ導出する出口パイプ92が接続されている。
なお,燃料電池5は,改質ガス中の水素を精製する装置
を有する(図示略)。
A raw material tank 9 storing methanol as a hydrocarbon compound is connected to the fuel cell reformer 4 via an inlet pipe 91 at the inlet side. On the other hand, an outlet pipe 92 for leading a reformed gas containing hydrogen to the fuel cell 5 is connected to the outlet side of the fuel cell reformer 4.
The fuel cell 5 has a device for purifying hydrogen in the reformed gas (not shown).

【0028】また,燃料電池5には,上記水素と反応さ
せて電池作用を惹起させるための酸素ガスを供給する。
燃料電池5において得られた電気エネルギーは,例えば
自動車走行用,車両電装品の駆動用などに用いるモータ
51に供給する。燃料電池5において,生じた水はリサ
イクル及び排水される。また,上記燃料電池用改質器4
において,上記金属シエル2は,入口パインプ91に接
続するフランジ部28,出口パイプ92に接続するフラ
ンジ部29を有する。また,上記触媒保持体には,触媒
としての白金が担持されている。
Further, oxygen gas is supplied to the fuel cell 5 so as to react with the above-mentioned hydrogen to cause a cell action.
The electric energy obtained in the fuel cell 5 is supplied to a motor 51 used for, for example, driving an automobile or driving electric components of a vehicle. In the fuel cell 5, generated water is recycled and drained. The fuel cell reformer 4
In the above, the metal shell 2 has a flange portion 28 connected to the inlet pine 91 and a flange portion 29 connected to the outlet pipe 92. Further, platinum as a catalyst is supported on the catalyst holder.

【0029】次に,本例の燃料電池用改質器の製造方法
について,具体的に説明する。まず,70重量%のアル
ミナ繊維と30重量%のシリカ繊維とを混合し,ウェッ
ブを形成する。ウェッブにニードルパンチング処理を施
す。これにより,ウェッブ内の繊維同士に絡み合いが形
成され,無機質繊維マットからなる保持シール材1が形
成される。このときの保持シール材1の厚みは12mm
であり,嵩密度は0.1g/cmである。
Next, a method for manufacturing the fuel cell reformer of this embodiment will be specifically described. First, a web is formed by mixing 70% by weight of alumina fiber and 30% by weight of silica fiber. Needle punching is applied to the web. Thereby, the entanglement is formed between the fibers in the web, and the holding sealing material 1 made of the inorganic fiber mat is formed. At this time, the thickness of the holding sealing material 1 is 12 mm.
And the bulk density is 0.1 g / cm 3 .

【0030】次に,図2(a)に示すごとく,保持シー
ル材1に切断加工をして,長尺体とするとともに,その
両端に,触媒保持体3の外周を巻回したときに互いに係
合する凹部11と凸部12とを形成する。また,図2
(b),(c)に示すごとく,外径130mm,長さ1
00mmの触媒保持体3,及び初期内径Dが155m
m,厚み1.5mm,長さ300mmのパイプ状の金属
シエル2を準備する。
Next, as shown in FIG. 2 (a), the holding sealing material 1 is cut into a long body, and when the outer periphery of the catalyst holding body 3 is wound around both ends thereof, The engaging concave portion 11 and the convex portion 12 are formed. Also, FIG.
(B), as shown in (c), outer diameter 130 mm, length 1
00mm catalyst holder 3, and initial inner diameter D is 155m
A pipe-shaped metal shell 2 having a length of m, a thickness of 1.5 mm and a length of 300 mm is prepared.

【0031】また,図2(b)に示すごとく,触媒保持
体3の外周を保持シール材1により巻回被覆して,凹部
11と凸部12とを係合させる。そして,この状態で,
図2(d)に示すごとく,金属シエル2の中に挿入す
る。即ち,触媒保持体3の軸方向外周に保持シール材1
を被覆した状態(図2b)で,これらを金属シエル2の
中に挿入し,触媒保持体3と金属シエル2との間に保持
シール材1を位置させる(図2d,図3a)。
Further, as shown in FIG. 2B, the outer periphery of the catalyst holder 3 is wound and covered with the holding sealing material 1 so that the concave portion 11 and the convex portion 12 are engaged. And in this state,
As shown in FIG. 2 (d), it is inserted into the metal shell 2. That is, the holding sealing material 1 is placed on the outer periphery of the catalyst holding body 3 in the axial direction.
Are inserted into the metal shell 2 in a state where they are covered (FIG. 2B), and the holding sealing material 1 is positioned between the catalyst holding body 3 and the metal shell 2 (FIGS. 2D and 3A).

【0032】次に,図3(a)に示すごとく,触媒保持
体3及び保持シール材1を挿入配置した上記金属シエル
2の外周に,スピニング加工を施す。スピニング加工
は,成形用ローラ6を,回転する金属シエル2の軸方向
に移動させ,金属シエル2の半径方向に徐々に加圧する
ことにより行う。これにより,図4(b)に示すごと
く,金属シエル2において触媒保持体3が位置する配設
部分Lの初期の初期内径D(155mm)を製品内側径
d(138mm)にまで小さくする。
Next, as shown in FIG. 3A, the outer periphery of the metal shell 2 in which the catalyst holder 3 and the holding sealing material 1 are inserted and arranged is subjected to spinning. The spinning process is performed by moving the forming roller 6 in the axial direction of the rotating metal shell 2 and gradually applying pressure in the radial direction of the metal shell 2. Thereby, as shown in FIG. 4B, the initial initial inner diameter D (155 mm) of the disposition portion L where the catalyst holder 3 is located in the metal shell 2 is reduced to the product inner diameter d (138 mm).

【0033】また,図1に示すごとく,触媒保持体3が
位置していない両端部分は徐々に開口部に向けて狭く
し,両末端にフランジ部28,29を設ける。スピニン
グ加工後の保持シール材1の厚みは約4mmであり,充
填密度は0.3g/cmである。以上により,本例の
燃料電池用改質器が得られる。
As shown in FIG. 1, both end portions where the catalyst holder 3 is not located are gradually narrowed toward the opening, and flange portions 28 and 29 are provided at both ends. The thickness of the holding sealing material 1 after spinning is about 4 mm, and the packing density is 0.3 g / cm 3 . As described above, the fuel cell reformer of this example is obtained.

【0034】本例においては,保持シール材1により巻
回した触媒保持体3を,上記製品内側径dよりも大きい
初期内径Dの金属シエル2の中に挿入しているため,保
持シール材1の配置を無理なく行えうことができる。ま
た,挿入後は,スピニング加工により,金属シエル2の
初期内径Dを所定の製品内側径dにまで小さくしてい
る。そのため,金属シエル2内に挿入されている保持シ
ール材1が触媒保持体3の内壁面によって圧縮される。
これにより,保持シール材1は,触媒保持体3にある程
度の面圧を与え,金属シエル2内に触媒保持体3を安定
して保持することができる。また,本例の燃料電池用改
質器においては保持シール材1に,バインダを含浸させ
ていないため,使用中に保持シール材からバインダー燃
焼ガスが排出されることはない。
In the present embodiment, the catalyst holding body 3 wound by the holding seal material 1 is inserted into the metal shell 2 having an initial inner diameter D larger than the product inner diameter d. Can be easily arranged. After the insertion, the initial inner diameter D of the metal shell 2 is reduced to a predetermined product inner diameter d by spinning. Therefore, the holding sealing material 1 inserted into the metal shell 2 is compressed by the inner wall surface of the catalyst holding body 3.
As a result, the holding sealing material 1 can apply a certain surface pressure to the catalyst holding body 3 and stably hold the catalyst holding body 3 in the metal shell 2. Further, in the fuel cell reformer of the present embodiment, since the binder is not impregnated in the holding seal material 1, the binder combustion gas is not discharged from the holding seal material during use.

【0035】[0035]

【発明の効果】本発明によれば,金属シエル内への触媒
保持体及び保持シール材の装着作業がしやすく,バイン
ダー燃焼ガスの発生がない,燃料電池用改質器及びその
製造方法を提供することができる。
According to the present invention, there is provided a reformer for a fuel cell and a method for manufacturing the same, in which the work of mounting the catalyst holding body and the holding sealing material in the metal shell is easy and no binder combustion gas is generated. can do.

【図面の簡単な説明】[Brief description of the drawings]

【図1】実施形態例1における燃料電池用改質器及びそ
の周辺機器等の説明図。
FIG. 1 is an explanatory diagram of a fuel cell reformer and its peripheral devices in a first embodiment.

【図2】実施形態例1における,燃料電池用改質器の製
造方法を示す説明図(a)〜(d)。
FIGS. 2A to 2D are diagrams illustrating a method for manufacturing a fuel cell reformer according to the first embodiment.

【図3】図2に続く,燃料電池用改質器の製造方法を示
す説明図(a)〜(b)。
FIG. 3 is an explanatory view (a)-(b) showing a method of manufacturing a reformer for a fuel cell, following FIG. 2;

【符号の説明】[Explanation of symbols]

1...保持シール材, 2...金属シエル, 3...触媒保持体, 4...燃料電池用改質器, 5....燃料電池, 6...成形用ローラ, 1. . . 1. holding sealing material, . . 2. metal shell; . . 3. catalyst holder, . . 4. reformer for fuel cell, . . . Fuel cell, 6. . . Forming roller,

Claims (10)

【特許請求の範囲】[Claims] 【請求項1】 炭化水素化合物を水素に改質する改質触
媒を保持する触媒保持体と,該触媒保持体の外方を覆う
金属シエルと,上記触媒保持体と金属シエルとの間に配
置される保持シール材とを有する燃料電池用改質器を製
造する方法において,上記触媒保持体を,上記保持シー
ル材により被覆する工程と,上記保持シール材により被
覆された触媒保持体を,上記燃料電池用改質器における
金属シエルの製品内側径よりも大きい初期内径を有する
パイプ状の金属シエルの中に挿入する工程と,上記金属
シエルにおける少なくとも上記触媒保持体が位置する配
設部分に,スピニング加工を施して,該配設部分の初期
内径を上記製品内側径まで小さくする工程とからなるこ
とを特徴とする燃料電池用改質器の製造方法。
1. A catalyst holder for holding a reforming catalyst for reforming a hydrocarbon compound into hydrogen, a metal shell covering the outside of the catalyst holder, and a metal shell disposed between the catalyst holder and the metal shell. A method for manufacturing a fuel cell reformer having a holding seal material, wherein the step of coating the catalyst holding body with the holding seal material, and the step of: A step of inserting the metal shell into a pipe-shaped metal shell having an initial inner diameter larger than the inner diameter of the product in the fuel cell reformer; and a step of disposing at least the catalyst holder in the metal shell. Performing a spinning process to reduce the initial inner diameter of the disposition portion to the inner diameter of the product.
【請求項2】 請求項1において,上記保持シール材
は,バインダーが含浸されていない無機質繊維マットで
あることを特徴とする燃料電池用改質器の製造方法。
2. The method according to claim 1, wherein the holding sealing material is an inorganic fiber mat not impregnated with a binder.
【請求項3】 請求項2において,上記無機質繊維マッ
トは,その中のAl 23,SiO2以外の物質が1重量
%未満であることを特徴とする燃料電池用改質器の製造
方法。
3. The inorganic fiber mat according to claim 2, wherein
The Al in it TwoOThree, SiOTwo1 weight of other substances
% Of a reformer for a fuel cell, characterized by being less than 0.1%
Method.
【請求項4】請求項2又は3において,無機質繊維マッ
トはその中の塩素,硫黄又はリンの1種以上が合計で3
00ppm未満であることを特徴とする燃料電池用改質
器の製造方法。
4. The inorganic fiber mat according to claim 2, wherein at least one of chlorine, sulfur and phosphorus in said inorganic fiber mat has a total of 3 or more.
A method for producing a reformer for a fuel cell, wherein the amount is less than 00 ppm.
【請求項5】 請求項1〜4のいずれか一項において,
スピニング加工前の上記保持シール材の厚みは4〜12
mmであることを特徴とする燃料電池用改質器の製造方
法。
5. The method according to claim 1, wherein:
The thickness of the holding sealing material before spinning is 4 to 12
mm, the method for producing a reformer for a fuel cell.
【請求項6】 請求項1〜5のいずれか1項において,
スピニング加工後の上記保持シール材の充填密度は,
0.20〜0.60g/cmであることを特徴とする
燃料電池用改質器の製造方法。
6. The method according to claim 1, wherein:
The filling density of the above holding sealing material after spinning is
0.20~0.60g / cm 3 A method of manufacturing a reformer for a fuel cell, characterized in that.
【請求項7】 炭化水素化合物を水素に改質する改質触
媒を保持する触媒担持体と,該触媒保持体の外方を覆う
金属シエルと,上記触媒保持体と上記金属シエルとの間
に配置される保持シール材とから構成されている燃料電
池用改質器であって,上記金属シエルにおける少なくと
も上記触媒保持体が位置する配設部分には,スピニング
加工が施されていることを特徴とする燃料電池用改質
器。
7. A catalyst carrier for holding a reforming catalyst for reforming a hydrocarbon compound into hydrogen, a metal shell for covering the outside of the catalyst holder, and a metal shell between the catalyst holder and the metal shell. A fuel cell reformer comprising: a holding sealing material to be disposed; wherein a spinning process is applied to at least a portion of the metal shell where the catalyst holding body is located. For a fuel cell.
【請求項8】 請求項7において,上記保持シール材
は,バインダーが含浸されていない無機質繊維マットで
あることを特徴とする燃料電池用改質器。
8. The reformer for a fuel cell according to claim 7, wherein the holding sealing material is an inorganic fiber mat not impregnated with a binder.
【請求項9】 請求項8において,上記無機質繊維マッ
トは,その中のAl 23,SiO2以外の物質が1重量
%未満であることを特徴とする燃料電池用改質器。
9. The inorganic fiber mat according to claim 8, wherein
The Al in it TwoOThree, SiOTwo1 weight of other substances
% Of the fuel cell.
【請求項10】請求項8又は9において,無機質繊維マ
ットはその中の塩素,硫黄又はリンの1種以上の1種以
上が合計で300ppm未満であることを特徴とする燃
料電池用改質器。
10. The reformer for a fuel cell according to claim 8, wherein the inorganic fiber mat has a total of less than 300 ppm of at least one of chlorine, sulfur and phosphorus therein. .
JP2000234771A 2000-08-02 2000-08-02 Manufacturing method of fuel cell reformer Expired - Fee Related JP4810721B2 (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2394679A (en) * 2002-08-06 2004-05-05 Visteon Global Tech Inc Spin-forming a catalytic converter
CN100341189C (en) * 2004-02-26 2007-10-03 三星Sdi株式会社 Reformer for fuel cell system and fuel cell system having the same

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0633755A (en) * 1992-05-21 1994-02-08 Minnesota Mining & Mfg Co <3M> Catalytic converter with metallic monolith mounted by heat-insulating mat of fireproof ceramic fiber
JP2000007304A (en) * 1998-06-29 2000-01-11 Ngk Insulators Ltd Reforming reactor
JP2000045762A (en) * 1998-07-30 2000-02-15 Tokyo Roki Co Ltd Catalyst converter and manufacture thereof
JP2001205354A (en) * 2000-01-20 2001-07-31 Sango Co Ltd Manufacturing method of treatment apparatus for gas
JP2001280124A (en) * 2000-03-31 2001-10-10 Ngk Insulators Ltd Cell structural body storage container and its assembly

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0633755A (en) * 1992-05-21 1994-02-08 Minnesota Mining & Mfg Co <3M> Catalytic converter with metallic monolith mounted by heat-insulating mat of fireproof ceramic fiber
JP2000007304A (en) * 1998-06-29 2000-01-11 Ngk Insulators Ltd Reforming reactor
JP2000045762A (en) * 1998-07-30 2000-02-15 Tokyo Roki Co Ltd Catalyst converter and manufacture thereof
JP2001205354A (en) * 2000-01-20 2001-07-31 Sango Co Ltd Manufacturing method of treatment apparatus for gas
JP2001280124A (en) * 2000-03-31 2001-10-10 Ngk Insulators Ltd Cell structural body storage container and its assembly

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2394679A (en) * 2002-08-06 2004-05-05 Visteon Global Tech Inc Spin-forming a catalytic converter
GB2394679B (en) * 2002-08-06 2005-01-12 Visteon Global Tech Inc Spin-forming method for making catalytic converter
CN100341189C (en) * 2004-02-26 2007-10-03 三星Sdi株式会社 Reformer for fuel cell system and fuel cell system having the same
US8486162B2 (en) 2004-02-26 2013-07-16 Samsung Sdi Co., Ltd. Reformer for fuel cell system and fuel cell system having the same

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