JPS5852697B2 - catalyst - Google Patents
catalystInfo
- Publication number
- JPS5852697B2 JPS5852697B2 JP51023447A JP2344776A JPS5852697B2 JP S5852697 B2 JPS5852697 B2 JP S5852697B2 JP 51023447 A JP51023447 A JP 51023447A JP 2344776 A JP2344776 A JP 2344776A JP S5852697 B2 JPS5852697 B2 JP S5852697B2
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- gas
- nitrogen
- ammonia
- present
- 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
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
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Landscapes
- Catalysts (AREA)
Description
【発明の詳細な説明】 本発明は鋼材の熱処理用触媒に関する。[Detailed description of the invention] The present invention relates to a catalyst for heat treatment of steel materials.
一般に鋼板の光輝熱処理には水素雰囲気、又はアンモニ
ヤ分解ガス雰囲気が利用される。Generally, a hydrogen atmosphere or an ammonia decomposition gas atmosphere is used for bright heat treatment of steel sheets.
水素雰囲気で熱処理するのが最良であるが、価格の点で
一般に安価なアンモニヤ分解ガスが利用されている。Heat treatment in a hydrogen atmosphere is best, but ammonia decomposition gas is generally used since it is inexpensive.
アンモニヤガスをニッケルを触媒として熱分解して生成
した水素ガスと窒素ガスの混合ガスを一般にアンモニヤ
分解ガスと呼んでイル。The mixed gas of hydrogen gas and nitrogen gas produced by thermally decomposing ammonia gas using nickel as a catalyst is generally called ammonia decomposition gas.
このアンモニヤ分解ガス中には未分解のアンモニヤが数
百〜数千ppm残り、この未分解アンモニヤが被熱処理
鋼材の表面と反応し、被熱処理鋼材の表面近傍に有害な
窒素化合物が生成し、鋼材の加工性を害している。Several hundred to several thousand ppm of undecomposed ammonia remains in this ammonia decomposition gas, and this undecomposed ammonia reacts with the surface of the steel to be heat treated, producing harmful nitrogen compounds near the surface of the steel to be heat treated. This impairs the processability of
アルミキルド鋼の熱処理には特に有害である。It is particularly harmful to the heat treatment of aluminized steel.
即ち未分解のアンモニヤガスが鋼材と接することにより
、熱処理温度でFeが触媒となり、未分解アンモニヤが
分解して活性の高い発生機の窒素が発生し、鋼材中に存
在する微量のAeと反応してAeNの微粒子が鋼材表面
近傍に析出し、鋼材の絞り加工性が劣化する。In other words, when undecomposed ammonia gas comes into contact with the steel material, Fe becomes a catalyst at the heat treatment temperature, and the undecomposed ammonia decomposes to generate nitrogen, a highly active generator, which reacts with the trace amount of Ae present in the steel material. As a result, fine particles of AeN precipitate near the surface of the steel material, deteriorating the drawability of the steel material.
自動車ボディーなどの深絞り加工をする鋼材には特に悪
い結果を与える。This is especially bad for steel materials that are deep drawn, such as those used in automobile bodies.
本発明は上記した様な微量の未分解アンモニヤによる。The present invention relies on a trace amount of undecomposed ammonia as described above.
被熱処理鋼材の絞り加工性に悪影響を与えるのを防止す
るための触媒に関するものである。This invention relates to a catalyst for preventing an adverse effect on the drawability of heat-treated steel materials.
即ち、窒素ガスとの親和性の高い元素、Ae、Ti、B
、Si、Zrのうち少くとも1種以上を含むFe合金粉
末を、第1図に示す様な金属で構成された連通気孔1を
有する三次元不規則網目状の骨格構造の該骨格2表面に
塗布、焼付けて、1体化した触媒に関するものである。That is, elements with high affinity for nitrogen gas, Ae, Ti, B
Fe alloy powder containing at least one of , Si, and Zr is applied to the surface of the skeleton 2, which has a three-dimensional irregular network skeleton structure having communicating pores 1 made of metal as shown in FIG. This relates to a catalyst that is integrated by coating and baking.
上記構成の触媒に未分解アンモニヤを含む、アンモニヤ
分解ガスが高温(500℃〜1400℃)で接すると、
Feの触媒作用により、未分解アンモニヤが分解され、
その時に発生する発生機の窒素ガスが、上記Fe合金粉
末中に少くとも1種以上含まれている窒素との親和性の
大ぎいA es T i−B、Si、Zrの元素と結合
して、A八、TiN、BN、 Si 3 N、 、 Z
rNの窒素化合物を生成し、未分解アンモニヤ及び活性
の高い発生機の窒素を含まない、安定なアンモニヤ分解
ガスを供給することができる。When ammonia decomposition gas containing undecomposed ammonia comes into contact with the catalyst having the above structure at high temperature (500°C to 1400°C),
Due to the catalytic action of Fe, undecomposed ammonia is decomposed,
The nitrogen gas generated by the generator at that time combines with the elements Aes Ti-B, Si, and Zr, which have a high affinity for nitrogen and are contained in at least one kind of the Fe alloy powder. , A8, TiN, BN, Si 3 N, , Z
It is possible to generate a nitrogen compound of rN and supply a stable ammonia decomposition gas that does not contain undecomposed ammonia and highly active generator nitrogen.
ここでA e、T i q B、S 1 、Z rの元
素を選んだのは窒素との親和力を示す。The elements A e, T i q B, S 1 , and Z r were selected here because of their affinity with nitrogen.
窒化物の生成自由エネルギーが、Aeで−80kcae
/m ole 、 T iで−100kcae/mol
e 、 Bで−60kcaff、’molaSiで−
40kcal/mole 、 Z rで一120kc
al/moleと他元素にくらべて窒素との親和性が非
常に大きいのが理由である。The free energy of nitride formation is -80 kcae in Ae.
/mole, Ti -100kcae/mol
e, -60 kcaff in B, - in 'molaSi
40kcal/mole, 120kc in Zr
The reason is that al/mole has a much greater affinity with nitrogen than with other elements.
そのため被熱処理鋼゛材中に含まれるAe、Ti、B、
Si、Zr等の添加元素と窒素ガスが反応することが防
止され、深絞り加工性のよい熱処理鋼材を得ることがで
きる。Therefore, Ae, Ti, B,
It is possible to prevent the nitrogen gas from reacting with additive elements such as Si and Zr, and to obtain a heat-treated steel material with good deep drawing workability.
本発明の触媒はFe中に固溶している窒素との親和性の
高い原子状の金属元素と原子状の発生機の窒素が反応す
るため、比較的低温でも反応は進行する。In the catalyst of the present invention, an atomic metal element having a high affinity for nitrogen dissolved in Fe reacts with nitrogen as an atomic generator, so that the reaction proceeds even at a relatively low temperature.
熱天秤測定により、520℃以上の温紋で効果が認めら
れる。According to thermobalance measurement, the effect is recognized when the temperature is 520°C or higher.
しかし実際にはFe中への窒素の固溶度の大きいγFe
(オーステナイト)の存在する領域である約900℃〜
1400℃の範囲が反応にとって良好である。However, in reality, γFe has a high solid solubility of nitrogen in Fe.
Approximately 900℃, which is the region where (austenite) exists
A range of 1400°C is good for the reaction.
鉄合金粉末に含まれる元素は窒素との親和性の大きなA
e、T t 、B−S i、Z rが考えらレルが、経
済的な面より考えて、Aeが良好である。The element contained in iron alloy powder is A, which has a high affinity for nitrogen.
Considering e, T t , B-S i, and Z r, Ae is better from an economic point of view.
Fe−Ae金合金粉末中Ae添加量はアンモニヤ分解ガ
ス中の未分解アンモニヤの量、触媒の寿命(添加したA
eがすべてl’Nになった時に寿命になる)を考えて適
宜に選択されるが、Ae添加量は50原子悌以下が最適
である。The amount of Ae added in the Fe-Ae gold alloy powder depends on the amount of undecomposed ammonia in the ammonia cracked gas, the life of the catalyst (the amount of added A
The amount of Ae added is optimally 50 atoms or less.
50原子俤以上になるとFeとAeの複雑な金属間化合
物が生成し、融点が低下したり、Aeの酸化皮膜が生成
するため不向きである。If it exceeds 50 atoms, a complex intermetallic compound of Fe and Ae will be formed, the melting point will be lowered, and an oxide film of Ae will be formed, which is not suitable.
50原子多以下の場合には、Fe−Aeの固溶したα相
の範囲であり、触媒作用が高いためである。This is because when the number is 50 atoms or less, it is in the range of α phase in which Fe-Ae is dissolved in solid solution, and the catalytic action is high.
工業的には上記Fe−Ae等の合金粉粒を反応塔内に充
填し、その中を未分解アンモニヤを含むアンモニヤ分解
ガスが流れる時に未分解アンモニヤが分解され、発生し
た発生機の窒素ガスがAe等と反応して、安定なAeN
等の化合物になる反応が行われる。Industrially, alloy powder particles such as Fe-Ae are filled into a reaction tower, and when ammonia decomposition gas containing undecomposed ammonia flows through the reaction tower, the undecomposed ammonia is decomposed and the generated nitrogen gas from the generator is Stable AeN by reacting with Ae etc.
A reaction is carried out to form a compound such as
従って触媒充填層としては、気体の流れを良く即ち圧力
損失を少くする事、触媒層との接触を密に行わせる等の
条件を満足させるため、各種の形状のものが利用される
。Therefore, catalyst packed beds of various shapes are used in order to satisfy conditions such as improving gas flow, that is, reducing pressure loss, and ensuring close contact with the catalyst layer.
本発明のいま1つの条件は、耐熱性のある。Another condition of the present invention is heat resistance.
たとえばNiで連通気孔を有する三次元不規則網状の骨
格構造をなす第1図に示した様な金属発泡体を形成し、
これを触媒担体とし、この担体発泡体の立体構造を形成
する骨格表面に、上記Fe合金粉末を薄く塗布、被覆し
て強固に焼付けたものを触媒とする。For example, by forming a metal foam with Ni as shown in Figure 1, which has a three-dimensional irregular network skeleton structure with continuous pores,
This is used as a catalyst carrier, and the above-mentioned Fe alloy powder is thinly applied and coated on the surface of the skeleton forming the three-dimensional structure of this carrier foam, and the catalyst is then firmly baked.
この様な金属発泡体触媒は、多孔率が95〜98俤でか
さは大きいが、非常に軽量で圧力損失が小さい。Although such a metal foam catalyst has a porosity of 95 to 98 pores and is bulky, it is extremely lightweight and has a small pressure loss.
さらに立体構造が網目状に連結しているため強匪も強い
特徴を有する。Furthermore, because the three-dimensional structure is connected in a network, it also has strong characteristics.
該発泡体の製法はポリウレタンフォームに導電処理をし
て、電気メッキしたのち、該ポリウレタンフォームを焙
焼除去したもので、連通気孔の平均孔径を任意に変化さ
せることもでき、比表面積も15000TrLV77L
3も可能である。The foam is manufactured by subjecting polyurethane foam to conductive treatment, electroplating, and then roasting and removing the polyurethane foam.The average pore diameter of the continuous pores can be changed arbitrarily, and the specific surface area is 15,000TrLV77L.
3 is also possible.
比表面積が極度に高い事は、ガスと触媒との接触面積が
大となり接触反応である触媒反応の効率を良くする。The extremely high specific surface area increases the contact area between the gas and the catalyst, improving the efficiency of the catalytic reaction.
また多孔率が高いために圧力損失が小さい。Also, due to its high porosity, pressure loss is small.
本発明の触媒の効果は数百ppm残在していた未分解ア
ンモニヤガスが10ppm以下に減じた。The effect of the catalyst of the present invention was that undecomposed ammonia gas, which remained at several hundred ppm, was reduced to 10 ppm or less.
以下実施例により本発明の効果を詳述する。The effects of the present invention will be explained below in detail with reference to Examples.
550 ppm の未分解アンモニヤを含むアンモヤ
分解ガスを1 m3/ Hr の速度で1100℃に
加熱した本発明の触媒層(直径5Qmmφ、厚さ50m
0を通過させ通過ガス中の未分解アンモニヤの量を測定
した結果及び本発明の触媒層通過后のアンモニヤ分解ガ
スで、一般のアルミキルド鋼材ヲ1100℃で2時間熱
処理した後の該熱処理鋼材中の増加窒素ガスを分析した
結果を下表に示した。The catalyst layer of the present invention (diameter 5Q mmφ, thickness 50 m
The results of measuring the amount of undecomposed ammonia in the passing gas and the results of measuring the amount of undecomposed ammonia in the gas passing through the catalyst layer of the present invention and the results of heat-treating general aluminum killed steel materials at 1100 ° C. for 2 hours using the ammonia decomposition gas after passing through the catalyst layer of the present invention. The results of analyzing the increased nitrogen gas are shown in the table below.
本実施例に示した様に、アンモニヤ分解ガス中の未分解
アンモニヤの減少及び被熱処理鋼材中の増加窒素ガス量
が、本発明の触媒を用いることにより極端に減少し、本
発明の効果が高いことが解る。As shown in this example, the reduction of undecomposed ammonia in the ammonia decomposition gas and the increased amount of nitrogen gas in the heat-treated steel material are extremely reduced by using the catalyst of the present invention, and the effect of the present invention is high. I understand.
なお、Niよりなる発泡体の骨格表面にFe合金粉末を
焼付けることも一方法であるが、これに限定されるもの
でなく、Fe合金の骨格よりなる発泡体を利用すること
も可能である。Incidentally, one method is to bake Fe alloy powder onto the surface of the skeleton of a foam made of Ni, but the method is not limited to this, and it is also possible to use a foam made of a skeleton of Fe alloy. .
上記触媒の利用個所としては、例えばアンモニウム分解
炉の出口に設置するか、鋼材の熱処理炉内に設置したり
、被熱処理材を本発明の触媒で被覆する等々の方法で利
用される。The catalyst may be used, for example, by installing it at the outlet of an ammonium decomposition furnace, installing it in a steel heat treatment furnace, or coating a material to be heat treated with the catalyst of the present invention.
【図面の簡単な説明】
第1図は該触媒に使用する連通気孔を有する三次元不規
則網状金属発泡体の概念図で、1は空孔を、2は骨格を
示す。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a conceptual diagram of a three-dimensional irregular network metal foam having continuous pores used in the catalyst, where 1 indicates the pores and 2 indicates the skeleton.
Claims (1)
1、B、Si、Zrのうち少くとも1種以上の元素を含
有している鉄合金粉末を、連通気孔を有する三次元不規
則網目状の骨格構造を有する金属発泡体の該骨格表面上
に塗布し、焼付けた事を特徴とする、アンモニヤ分解ガ
スによる鋼材の熱処理用触媒。1 A e 4T, an element with high affinity for nitrogen gas
1. Iron alloy powder containing at least one element among B, Si, and Zr is placed on the skeletal surface of a metal foam having a three-dimensional irregular network skeletal structure with continuous pores. A catalyst for heat treatment of steel materials using ammonia decomposition gas, which is coated and baked.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51023447A JPS5852697B2 (en) | 1976-03-03 | 1976-03-03 | catalyst |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51023447A JPS5852697B2 (en) | 1976-03-03 | 1976-03-03 | catalyst |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS52105589A JPS52105589A (en) | 1977-09-05 |
| JPS5852697B2 true JPS5852697B2 (en) | 1983-11-24 |
Family
ID=12110747
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP51023447A Expired JPS5852697B2 (en) | 1976-03-03 | 1976-03-03 | catalyst |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5852697B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58139743A (en) * | 1982-02-13 | 1983-08-19 | Ishikawajima Harima Heavy Ind Co Ltd | Production of metallic nickel catalyst |
-
1976
- 1976-03-03 JP JP51023447A patent/JPS5852697B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS52105589A (en) | 1977-09-05 |
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