JPH031065Y2 - - Google Patents
Info
- Publication number
- JPH031065Y2 JPH031065Y2 JP1984159035U JP15903584U JPH031065Y2 JP H031065 Y2 JPH031065 Y2 JP H031065Y2 JP 1984159035 U JP1984159035 U JP 1984159035U JP 15903584 U JP15903584 U JP 15903584U JP H031065 Y2 JPH031065 Y2 JP H031065Y2
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- gas
- oxidation reaction
- ignition
- porous solid
- 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.)
- Expired
Links
- 238000007254 oxidation reaction Methods 0.000 claims description 26
- 239000003054 catalyst Substances 0.000 claims description 21
- 239000007787 solid Substances 0.000 claims description 18
- 239000007809 chemical reaction catalyst Substances 0.000 claims description 17
- 239000007789 gas Substances 0.000 description 25
- 239000000446 fuel Substances 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 4
- 239000002737 fuel gas Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 230000020169 heat generation Effects 0.000 description 2
- 239000011343 solid material Substances 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 229910052878 cordierite Inorganic materials 0.000 description 1
- 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 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229910001120 nichrome Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000011949 solid catalyst Substances 0.000 description 1
- 230000002459 sustained effect Effects 0.000 description 1
Landscapes
- Gas Burners (AREA)
- Lighters Containing Fuel (AREA)
- Catalysts (AREA)
Description
【考案の詳細な説明】
産業上の利用分野
本考案は、ガスライターやガスコンロの如きガ
ス燃料器具で発熱体として組込み可能なガス着火
用触媒に関するものである。[Detailed Description of the Invention] Industrial Application Field The present invention relates to a gas ignition catalyst that can be incorporated as a heating element in gas fuel appliances such as gas lighters and gas stoves.
従来の技術
従来、この種のガス着火用触媒としては酸化ア
ルミナ等の多孔質固型体で形成した酸化反応用触
媒が一般に用いられている。BACKGROUND ART Conventionally, as this type of gas ignition catalyst, an oxidation reaction catalyst formed of a porous solid material such as alumina oxide has been generally used.
考案が解決しようとする問題点
然し、この多孔質固型体の酸化反応用触媒では
ガス燃料器具の噴出ノズルからガスが作用する個
所にしか酸化反応が発生しない。例えば、ガス噴
出ノズルの先端を酸化反応用触媒の略中央に対応
させて配置すると、その中央部分には酸化反応が
生ずるものの、周辺部分では酸化反応が生じない
ため発火作用面が局部的になつて着火効率が悪い
ばかりでなく、ガス燃焼効率も良くない欠点があ
る。Problems to be Solved by the Invention However, with this porous solid catalyst for oxidation reactions, the oxidation reaction occurs only at the location where gas acts from the jet nozzle of the gas fuel appliance. For example, if the tip of the gas jet nozzle is placed so as to correspond to the approximate center of the oxidation reaction catalyst, the oxidation reaction will occur in the center, but not in the periphery, so the ignition action surface will be localized. Not only is the ignition efficiency poor, but the gas combustion efficiency is also poor.
問題点を解決するための手段
本考案に係るガス着火用触媒においては多孔質
固型体の酸化反応用触媒で発火面を形成するもの
の、その背面側で噴出ノズルからガスが噴射され
る側に綿状の酸化反応用触媒を一体に積層するよ
う構成されている。Means for Solving the Problems In the gas ignition catalyst according to the present invention, the ignition surface is formed of a porous solid oxidation reaction catalyst, but the ignition surface is formed on the back side of the oxidation reaction catalyst on the side where gas is injected from the jet nozzle. It is constructed so that flocculent oxidation reaction catalysts are laminated together.
作 用
このガス着火用触媒の構造では、綿状の酸化用
触媒が全体的に均等な酸化反応を生ずることによ
り、その酸化反応が発火面の多孔質固型体に作用
して全体として均一な着火作用を発揮できるよう
になる。Function: In the structure of this gas ignition catalyst, the cotton-like oxidation catalyst causes an oxidation reaction that is uniform throughout, and the oxidation reaction acts on the porous solid body on the ignition surface, resulting in a uniform oxidation reaction as a whole. Becomes capable of igniting.
実施例
以下、添付図面を参照して説明すれば、次の通
りである。Embodiments The following description will be made with reference to the accompanying drawings.
このガス着火用触媒は多孔質固型体の酸化反応
用触媒1と綿状の酸化反応用触媒2とを一体に積
層した多層体として形成されている(第1,2図
参照)。それら酸化反応用触媒のうち、多孔質固
型体1はAl2O3、コージライト等のハニカム状或
いはランダム多孔状のセラミツク焼成体を用いる
ことができ、また綿状体のもの2としては硅酸ガ
ラス繊維等を適用するようにできる。この多孔質
固型体1では被燃焼物或いは被加熱物に熱を印加
する発火面を形成するものであり、また綿状の酸
化反応用触媒2ではガス燃料の噴射側に位置する
よう多孔質固型体1の背面側に一体に装着されて
いる。 This gas ignition catalyst is formed as a multilayer body in which a porous solid oxidation reaction catalyst 1 and a cotton-like oxidation reaction catalyst 2 are laminated together (see FIGS. 1 and 2). Among these oxidation reaction catalysts, the porous solid body 1 can be a honeycomb-shaped or randomly porous fired ceramic body such as Al 2 O 3 or cordierite, and the cotton-like body 2 can be silicon. Acid glass fiber etc. can be applied. This porous solid body 1 forms an ignition surface that applies heat to the object to be burned or heated, and the flocculent oxidation reaction catalyst 2 has a porous solid body so as to be located on the gas fuel injection side. It is integrally attached to the back side of the solid body 1.
このように構成するガス着火用触媒はガスライ
ター,ガスコンロ等の発熱体として組込むことが
でき、その取付器具の形態に応じて適宜な大きさ
のブロツク或いは板状に形成することができる。
この触媒Aを各種のガス器具に組込んで発熱体と
して機能させるときには、その器具の噴出ノズル
Bからガスを触媒Aに供給し、このガス燃料Cに
対して放電ノズルからの火花やニクロム線の発熱
等で着火する。そのとき、燃料ガスは綿状の酸化
反応用触媒2の内部で繊維組織に沿つて全体的に
分散しつつ流通するため、この触媒組織内では少
なくとも全体的にガス燃焼が生ずるようになる。
この燃焼効果は多孔質固型体1の全面に波及作用
し、この固型体1の全域から発熱できるようにな
る。この発熱で、タバコに火を付け或いは被加熱
体を効率よく加熱することができ、その燃料ガス
の噴出を継続すればガス燃焼を持続できるように
なる。 The gas ignition catalyst constructed in this manner can be incorporated as a heating element in a gas lighter, gas stove, etc., and can be formed into a block or plate shape of an appropriate size depending on the form of the fitting.
When this catalyst A is incorporated into various gas appliances to function as a heating element, gas is supplied to the catalyst A from the jet nozzle B of the appliance, and the gas fuel C is exposed to sparks from the discharge nozzle and nichrome wire. It ignites due to heat generation, etc. At this time, the fuel gas flows within the flocculent oxidation reaction catalyst 2 while being dispersed throughout along the fiber structure, so that gas combustion occurs at least throughout the catalyst structure.
This combustion effect has a ripple effect on the entire surface of the porous solid body 1, and heat can be generated from the entire area of the solid body 1. This heat generation can ignite a cigarette or efficiently heat an object to be heated, and if the fuel gas continues to be ejected, gas combustion can be sustained.
なお、上述した実施例では多孔質固型体1と綿
状の酸化反応用触媒2との二層に形成したが、そ
の綿状酸化反応用触媒2をサンドイツチ状に挾ん
で多孔質固型体1,3で三層に形成することもで
きる(第4,5図参照)。この場合には、最内層
に積層する酸化反応用触媒2は発火面を形成する
ものと同質のもので形成でき、或いは別の材質で
多孔質固型体に形成してもよい。この触媒構造で
は最内層の固型体3が燃料ガスを集中的に受取
り、それを中間の綿状触媒2に全面均等に分散す
るよう導通できるため、ガス噴出ノズルBとの間
隔をあけて相互に設置しても燃料ガスの飛散を防
止できるようになる。また、上述した多孔質固型
体1,3では孔内或いは表面も含めてアルミナ等
の粉状酸化反応触媒を付着すると、ガスとの接触
面積を増して反応効率を向上するようにできる。
この粉状酸化反応触媒は多孔質固型体,3の焼成
前に散布し、その後に焼成処理を行うようにする
固型体1,3に固着することができる。 In the above-mentioned embodiment, the porous solid body 1 and the flocculent oxidation reaction catalyst 2 were formed in two layers, but the flocculent oxidation reaction catalyst 2 was sandwiched in a sandwich pattern to form a porous solid body. It is also possible to form three layers of layers 1 and 3 (see Figures 4 and 5). In this case, the oxidation reaction catalyst 2 laminated in the innermost layer may be formed of the same material as that forming the ignition surface, or may be formed into a porous solid body of a different material. In this catalyst structure, the solid body 3 in the innermost layer receives the fuel gas intensively and can conduct it to the intermediate flocculent catalyst 2 so as to distribute it evenly over the entire surface. This will prevent fuel gas from scattering even if installed in Furthermore, if a powdered oxidation reaction catalyst such as alumina is attached to the porous solid bodies 1 and 3, including the inside of the pores or the surface thereof, the contact area with the gas can be increased and the reaction efficiency can be improved.
This powdered oxidation reaction catalyst can be dispersed before firing the porous solid bodies 1 and 3, and then fixed on the solid bodies 1 and 3 to be subjected to the firing process.
考案の効果
以上の如く、本考案に係るガス着火用触媒構造
に依れば、ガス燃料による発火を効率よく行える
ものであり、しかも発火面が多孔質固型体で形成
されているため、それが被燃焼体や被加熱体と接
触しても変形し或いは摩耗する如き事態を生ずる
ことがない。Effects of the invention As described above, according to the catalyst structure for gas ignition according to the invention, it is possible to efficiently ignite gas fuel, and moreover, since the ignition surface is formed of a porous solid material, Even if it comes into contact with a burnt object or a heated object, it will not be deformed or worn out.
第1図は本考案に係る触媒の一実施例を示す斜
視図、第2図は同触媒の側断面図、第3図は同触
媒の発熱作用を示す説明図、第4図は別の実施例
に係る触媒の斜視図、第5図は同触媒の側断面図
である。
1,3:多孔質固型体の酸化反応用触媒、2:
綿状体の酸化反応用触媒。
Fig. 1 is a perspective view showing one embodiment of the catalyst according to the present invention, Fig. 2 is a side sectional view of the catalyst, Fig. 3 is an explanatory view showing the exothermic action of the catalyst, and Fig. 4 is another embodiment. FIG. 5 is a perspective view of the catalyst according to the example, and FIG. 5 is a side sectional view of the same catalyst. 1, 3: Catalyst for oxidation reaction of porous solid body, 2:
Catalyst for oxidation reaction of flocculent material.
Claims (1)
し、その背面側に綿状体の酸化反応用触媒を一体
に積層してなることを特徴とするガス着火用触媒
構造。 A gas ignition catalyst structure characterized in that an ignition surface is formed of a porous solid oxidation reaction catalyst, and a cotton-like oxidation reaction catalyst is integrally laminated on the back side of the ignition surface.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1984159035U JPH031065Y2 (en) | 1984-10-19 | 1984-10-19 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1984159035U JPH031065Y2 (en) | 1984-10-19 | 1984-10-19 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6175839U JPS6175839U (en) | 1986-05-22 |
| JPH031065Y2 true JPH031065Y2 (en) | 1991-01-14 |
Family
ID=30716996
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1984159035U Expired JPH031065Y2 (en) | 1984-10-19 | 1984-10-19 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH031065Y2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2531439B2 (en) * | 1993-06-22 | 1996-09-04 | 日本電気株式会社 | Composite catalyst |
-
1984
- 1984-10-19 JP JP1984159035U patent/JPH031065Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6175839U (en) | 1986-05-22 |
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