JPS62158896A - Production of porous metallic body - Google Patents
Production of porous metallic bodyInfo
- Publication number
- JPS62158896A JPS62158896A JP17886A JP17886A JPS62158896A JP S62158896 A JPS62158896 A JP S62158896A JP 17886 A JP17886 A JP 17886A JP 17886 A JP17886 A JP 17886A JP S62158896 A JPS62158896 A JP S62158896A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- metal
- burning
- metallic body
- polyurethane foam
- 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
Landscapes
- Powder Metallurgy (AREA)
Abstract
Description
【発明の詳細な説明】
〈産業上の利用分野〉
本発明は、三次元網状金属多孔体の製造方法の改良に関
する。DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to an improvement in a method for producing a three-dimensional mesh porous metal body.
〈従来の技術〉
従来、三次元網状金属多孔体を製造する場合には、まず
、導電性を付与したポリウレタンフォームに電気メッキ
を施して金属化し、その後大気中で焙焼してポリウレタ
ンフォームを焼却し、次いで酸化した金属を馬ガスある
いは)L、20%、N280%の混合ガス中で還元して
完全な金属多孔体にするという方法がとられている。<Conventional technology> Conventionally, when manufacturing a three-dimensional mesh porous metal body, polyurethane foam that has been given conductivity is first metallized by electroplating, and then the polyurethane foam is incinerated by roasting in the atmosphere. Then, the oxidized metal is reduced in horse gas or a mixed gas of 20% L and 80% N2 to form a complete metal porous body.
〈発明が解決しようとする問題点〉
上述したように、従来においては還元工程でI−L、ガ
ス、あるいは鳴ガスとN2ガスとの混合ガスを使用して
いるが、どちらのガスも高価であるため生産コスト上問
題となってし)な。<Problems to be solved by the invention> As mentioned above, conventionally, IL, gas, or a mixed gas of N gas and N2 gas are used in the reduction process, but both gases are expensive and expensive. (This poses a problem in terms of production costs.)
よって、本発明は上記問題点に鑑み、還元工程に使用す
る高価なN2ガス、あるいはIt、ガスとNガスとの混
合ガスの量を減少させてガス代を節約しうろ金属多孔体
の製造方法を提供することを目的とする。Therefore, in view of the above-mentioned problems, the present invention provides a method for manufacturing a hollow metal porous body that reduces the amount of expensive N2 gas or a mixed gas of It gas and N gas used in the reduction process to save gas costs. The purpose is to provide
く問題点を解決するための手段〉
前記目的を達成する本発明の構成は、金属メッキが施さ
れたポリウレタンフォームを培焼することによりこのポ
リウレタンフォームを焼却して多孔金属を得るとともに
ボリウレクンフォーム焼却時に発生する焙焼発生ガスを
大気と混合させずに1−ラップし、この焙焼発生ガス、
あるいはこの焙焼発生ガスに馬ガス又(よN2ガスとN
2ガスとの混合ガスを混入させたガスの雰囲気下で前記
多孔金属を還元することを特徴とする。Means for Solving the Problems> The structure of the present invention to achieve the above object is to incinerate polyurethane foam coated with metal to obtain porous metal and to obtain polyurethane foam. The torrefied gas generated during foam incineration is 1-wrapped without being mixed with the atmosphere, and this torrefied gas is
Alternatively, this roasting gas may be combined with horse gas (N2 gas and N2 gas).
The method is characterized in that the porous metal is reduced in an atmosphere of a gas mixed with two gases.
上述の焙焼工程においては、ポリウレタンフォームは完
全燃焼するので、このとき発生する焙焼発生ガスは、C
o2.N2及び馬と微量のCnHm及び02とからなり
、中性雰囲気のガスである。よってこの焙焼発生ガスを
大気と混合させないようにトラップすれば、これを用い
て多孔金属を還元することが可能である。In the above-mentioned roasting process, the polyurethane foam is completely combusted, so the roasting gas generated at this time is C
o2. It is a gas in a neutral atmosphere, consisting of N2 and a trace amount of CnHm and 02. Therefore, if this roasting gas is trapped so as not to mix with the atmosphere, it is possible to reduce the porous metal using this gas.
また、このとき安全を見てわずかの鶴ガス、又はN2ガ
スとN2ガスとの混合ガスを上記焙焼発生ガスに混合し
て弱y元雰囲気のガスとしてもよい。ここでの混合割合
は望む還元状態によって異なるが、例えば焙焼発生ガス
80、%に鳩ガス又(よT(2:N、、=20=80の
混合ガスを20%用いればよい。Further, at this time, for safety reasons, a small amount of Tsuru gas or a mixed gas of N2 gas and N2 gas may be mixed with the roasting gas to create a weak y-element atmosphere. The mixing ratio here varies depending on the desired reduction state, but for example, it is sufficient to use 80% of the roasted gas and 20% of the mixed gas of pigeon gas or (2:N, =20=80).
く作 用〉
従来廃棄していた焙焼発生ガスを多孔金属の還元に用い
ることにより、還元用のガス代を激減することができろ
。Effect> By using the gas generated from roasting, which was previously discarded, for the reduction of porous metals, the cost of reducing gas can be drastically reduced.
く実 施 例〉
実施例1
導電性を付与したポリウレタンフォームに電気メッキを
施して金属化し、これを焙焼してポリウレタンフォーム
を焼却するとともに、このときの発生ガスを1−ラップ
しておく。Examples Example 1 A polyurethane foam imparted with electrical conductivity is electroplated to metallize it, and is roasted to incinerate the polyurethane foam, and the gas generated at this time is wrapped.
上記焙焼によって得られた多孔金属を還元炉内に移し、
この還元炉内へトラップしておいた焙焼発生ガスを20
rn’ / hrで導入するとともに別途比ガスを5
rn’ / hrで導入し、熱処理を行った。これに
より多孔金属は完全に還元されて三次元網状金属多孔体
が得られた。The porous metal obtained by the above roasting is transferred into a reduction furnace,
The roasting generated gas trapped in this reduction furnace is
Introduce rn'/hr and add a separate specific gas of 5
It was introduced at rn'/hr and heat treated. As a result, the porous metal was completely reduced and a three-dimensional network-like porous metal body was obtained.
比較のため、同様な多孔金属をN2ガス5 m’/hr
十N2ガス20 m / hrの混合ガスを導入しなが
ら還元したが、上記実施例と同様な三次元網状金属多孔
体が得られた。For comparison, a similar porous metal was heated with N2 gas at 5 m'/hr.
Reduction was carried out while introducing a mixed gas of 10N2 gas at a rate of 20 m/hr, and a three-dimensional network-like porous metal body similar to the above example was obtained.
したがって、本実施例においては比較例に較べてN2ガ
ス20 rn’ / hrの節約となっている。Therefore, in this example, 20 rn'/hr of N2 gas was saved compared to the comparative example.
実 施 例 2
実施例1と同様にして得た多孔金属を還元する場合に焙
焼混合ガスだけを25 rn’ / hrで導入しt二
ところ、多孔金属が完全に還元されて、実施例1と同様
な三次元網状金属多孔体が得られた。Example 2 When reducing the porous metal obtained in the same manner as in Example 1, only the roasting mixed gas was introduced at 25 rn'/hr, and the porous metal was completely reduced. A three-dimensional network-like porous metal material similar to that was obtained.
比較のためH,ガス25 m / hrを導入して同様
な多孔金属を還元しても同様な三次元網状金属多孔体で
あった。For comparison, when a similar porous metal was reduced by introducing H gas at 25 m/hr, a similar three-dimensional network porous metal body was obtained.
しtこがって本実施例においては比較例に較べて)%ガ
ス25 rn’ / hrの節約とtrっでいろ。Therefore, in this example, compared to the comparative example, a saving of 25% gas rn'/hr was achieved.
〈発明の効果〉
以上、実施例とともに具体的に説明したように、本発明
方法によれば金属多孔体製造における還元工程のガス代
を激減することができるので、低コストの金属多孔体を
提供する、ことができる。<Effects of the Invention> As specifically explained above in conjunction with Examples, according to the method of the present invention, the gas cost in the reduction process in producing a porous metal body can be drastically reduced, thereby providing a low-cost porous metal body. can do.
特 許 出 願 人 住友電気工業株式会社 代 理 人Patent applicant Sumitomo Electric Industries, Ltd. People
Claims (1)
ことによりこのポリウレタンフォームを焼却して多孔金
属を得るとともにポリウレタンフォーム焼却時に発生す
る焙焼発生ガスを大気と混合させずにトラップし、この
焙焼発生ガス、あるいはこの焙焼発生ガスにH_2ガス
又はH_2ガスとN_2ガスとの混合ガスを混入させた
ガスの雰囲気下で前記多孔金属を還元することを特徴と
する金属多孔体の製造方法。By roasting metal-plated polyurethane foam, this polyurethane foam is incinerated to obtain porous metal, and the roasting gas generated when polyurethane foam is incinerated is trapped without mixing with the atmosphere, and this roasting gas is trapped. A method for producing a porous metal body, characterized in that the porous metal is reduced in an atmosphere of a gas or a gas in which H_2 gas or a mixed gas of H_2 gas and N_2 gas is mixed with the roasting generated gas.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17886A JPS62158896A (en) | 1986-01-07 | 1986-01-07 | Production of porous metallic body |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17886A JPS62158896A (en) | 1986-01-07 | 1986-01-07 | Production of porous metallic body |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62158896A true JPS62158896A (en) | 1987-07-14 |
Family
ID=11466751
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP17886A Pending JPS62158896A (en) | 1986-01-07 | 1986-01-07 | Production of porous metallic body |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62158896A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8597383B2 (en) | 2011-04-11 | 2013-12-03 | Saudi Arabian Oil Company | Metal supported silica based catalytic membrane reactor assembly |
US9745191B2 (en) | 2011-04-11 | 2017-08-29 | Saudi Arabian Oil Company | Auto thermal reforming (ATR) catalytic structures |
-
1986
- 1986-01-07 JP JP17886A patent/JPS62158896A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8597383B2 (en) | 2011-04-11 | 2013-12-03 | Saudi Arabian Oil Company | Metal supported silica based catalytic membrane reactor assembly |
US9745191B2 (en) | 2011-04-11 | 2017-08-29 | Saudi Arabian Oil Company | Auto thermal reforming (ATR) catalytic structures |
US10071909B2 (en) | 2011-04-11 | 2018-09-11 | Saudi Arabian Oil Company | Auto thermal reforming (ATR) catalytic structures |
US10093542B2 (en) | 2011-04-11 | 2018-10-09 | Saudi Arabian Oil Company | Auto thermal reforming (ATR) catalytic structures |
US10252910B2 (en) | 2011-04-11 | 2019-04-09 | Saudi Arabian Oil Company | Auto thermal reforming (ATR) catalytic structures |
US10252911B2 (en) | 2011-04-11 | 2019-04-09 | Saudi Arabian Oil Company | Auto thermal reforming (ATR) catalytic systems |
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