JPS6237682B2 - - Google Patents
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- Publication number
- JPS6237682B2 JPS6237682B2 JP55069032A JP6903280A JPS6237682B2 JP S6237682 B2 JPS6237682 B2 JP S6237682B2 JP 55069032 A JP55069032 A JP 55069032A JP 6903280 A JP6903280 A JP 6903280A JP S6237682 B2 JPS6237682 B2 JP S6237682B2
- Authority
- JP
- Japan
- Prior art keywords
- tungsten
- molybdenum
- powder
- alloy
- solid solution
- 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
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- 229910052721 tungsten Chemical class 0.000 claims description 32
- 229910052750 molybdenum Inorganic materials 0.000 claims description 30
- 239000000843 powder Substances 0.000 claims description 25
- 239000000956 alloy Substances 0.000 claims description 19
- 229910045601 alloy Inorganic materials 0.000 claims description 19
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical class [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 16
- 239000011733 molybdenum Substances 0.000 claims description 16
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical class [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 claims description 15
- 239000010937 tungsten Chemical class 0.000 claims description 15
- 229910052751 metal Inorganic materials 0.000 claims description 11
- 239000002184 metal Substances 0.000 claims description 11
- 238000004519 manufacturing process Methods 0.000 claims description 8
- 150000003863 ammonium salts Chemical class 0.000 claims description 5
- 150000002739 metals Chemical class 0.000 claims description 2
- 238000011946 reduction process Methods 0.000 claims description 2
- 239000006104 solid solution Substances 0.000 description 10
- 229910052799 carbon Inorganic materials 0.000 description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 8
- 239000002245 particle Substances 0.000 description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 5
- 229910052739 hydrogen Inorganic materials 0.000 description 5
- 239000001257 hydrogen Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 239000010941 cobalt Substances 0.000 description 3
- 229910017052 cobalt Inorganic materials 0.000 description 3
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 3
- 238000004108 freeze drying Methods 0.000 description 3
- 150000001247 metal acetylides Chemical class 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000011812 mixed powder Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 238000000790 scattering method Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000012916 structural analysis Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 235000011089 carbon dioxide Nutrition 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 238000010000 carbonizing Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 238000000975 co-precipitation Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- -1 iron group metals Chemical class 0.000 description 1
- 229910000476 molybdenum oxide Inorganic materials 0.000 description 1
- MGRWKWACZDFZJT-UHFFFAOYSA-N molybdenum tungsten Chemical group [Mo].[W] MGRWKWACZDFZJT-UHFFFAOYSA-N 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- VVRQVWSVLMGPRN-UHFFFAOYSA-N oxotungsten Chemical class [W]=O VVRQVWSVLMGPRN-UHFFFAOYSA-N 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 229910001930 tungsten oxide Inorganic materials 0.000 description 1
Landscapes
- Ceramic Products (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
Description
本発明は安定した、モリブデンとタングステン
からなる複合炭化物の製造に適した、モリブデン
とタングステンを含む合金粉末の製造法に関する
ものである。
従来、MoC―WCの固溶体の製造法としては、
WC、MoおよびC粉末、またはW、MoおよびC
粉末に、コバルトを加え混合粉末とした後、炭素
容器に充填して1600〜2000℃の温度で反応させる
方法が普通採られている(W.Dawihl,Z.anorg.
chem. 262(1950)、212)。このときコバルトは
炭化物の生成を助け、かつMoとCがWC中に固
溶するのを促進するとされており、Coが存在し
ないと、(Mo,W)Cの固溶体は得られないこと
も知られている。しかしながら、この方法で得た
(Mo,W)C粉末をWCの代換品として超硬合金
製造に用いたところ、合金中では(Mo,W)C
が分解して(Mo,W)2Cとしての針状結晶が析
出し、合金中で少量のMo2Cは凝集して析出する
め合金強度を著しく劣化させてしまう。このよう
な理由から、今まではWCの代換品として、積極
的にMoCを使用する試みは為されなかつた。
本発明者等は、合金中で(Mo,W)Cが安定
すればこの粉末は高価なWCの代換品として十分
使用できると考え、安定した(Mo,W)Cの製
造法を検討してきたが、このたび(Mo,W)C
の生成過程における次のような新しい知見を得
た。
(Mo,W)Cの固溶体の製造にあたり、まず
1600℃以上の温度で加熱する必要があるが、これ
はMo,Wの金属または炭化物の粉末同志の拡散
を行なわせて均一な固溶体とするためである。し
かしながら、従来のように数μのMo,Wの金属
粉末を互に拡散固溶させようとすると、第1表の
ような高い温度と、長時間の加熱が必要である。
The present invention relates to a method for producing an alloy powder containing molybdenum and tungsten, which is suitable for producing a stable composite carbide composed of molybdenum and tungsten. Conventionally, the manufacturing method of MoC-WC solid solution is as follows:
WC, Mo and C powder or W, Mo and C
The usual method is to add cobalt to the powder to make a mixed powder, then fill it in a carbon container and react at a temperature of 1,600 to 2,000 degrees Celsius (W. Dawihl, Z. anorg.
chem. 262 (1950), 212). At this time, cobalt is said to help the formation of carbides and promote the solid solution of Mo and C in WC, and it is also known that a solid solution of (Mo, W)C cannot be obtained if Co is not present. It is being However, when the (Mo,W)C powder obtained by this method was used as a substitute for WC in the production of cemented carbide, it was found that (Mo,W)C was found in the alloy.
decomposes and precipitates acicular crystals as (Mo, W) 2 C, and a small amount of Mo 2 C in the alloy aggregates and precipitates, significantly deteriorating the alloy strength. For these reasons, until now no attempt has been made to actively use MoC as a substitute for WC. The inventors believe that if (Mo, W)C is stable in the alloy, this powder can be used as a substitute for expensive WC, and have been studying methods for producing stable (Mo,W)C. However, this time (Mo, W)C
We obtained the following new findings regarding the production process. In producing a solid solution of (Mo,W)C, first
It is necessary to heat at a temperature of 1,600° C. or higher, in order to cause the Mo, W metal or carbide powders to diffuse into each other to form a uniform solid solution. However, in order to diffuse and form a solid solution of Mo and W metal powders of several μm with each other as in the conventional method, high temperatures and long-time heating as shown in Table 1 are required.
【表】
これに対し、粉末粒子が非常に微細であれば拡
散は容易に行なわれ、しかも拡散助剤である鉄族
金属が不要となるため良質な炭化物を得ることが
可能になる。したがつて微細な(Mo,W)金属
粉末を製造することが課題となつてくる。
従来、(Mo,W)メタルの製造においては、水
酸化物のスラリー状態での機械的混合法や水酸化
物の化学的共沈法が主に採られてきたが、前者は
機械的混合によるため分子レベルの混合が達成さ
れないという欠点があり、後者は酸分解によりモ
リブデンとタングステンの酸化物の析出す酸濃度
(PH)が異なるため析出組成が一定しないという
欠点があつて、共に微細な(Mo,W)メタルを
得ることはできなかつた。
この発明者等はこのたび、凍結乾燥法によりは
じめて微細に分散した(Mo,W)メタルの製造
が可能になることを見出し、本発明に到達したも
のである。凍結乾燥とは、元来、熱によつて分解
され易い物質または泡立ち易い物質などを、高真
空下で凍結後、氷を昇華させて水蒸気として取除
くことにより乾燥する方法である。
そして炭化物製造にあたつて、凍結乾燥法によ
り製造した(Mo,W)メタルを使用することに
より、従来のようにコバルト等の拡散助剤を用い
ることなく、単に(Mo,W)メタルとカーボン
を混合して炭化することにより理論結合炭素量を
有する炭化物を製造することが可能となつた。
本発明においては、モリブデンとタングステン
のアンモニウム塩を凍結乾燥した後空気中で焙焼
することによりタングステンとモリブデンの酸化
物を均一微細化した後、還元工程を経て合金と
し、合金粉末を製造する。該合金粉末は炭素粉末
と反応させ、ヘキサゴナルモノカーバイドの固溶
体結晶構造を有するモリブデンとタングステンか
らなる複合炭化物を製造することができる。
タングステン―モリブデン全率固溶体粒子の組
成は重量比でMo/W=0.005〜10が適当であり、
0.005末満では耐酸化性、耐熱性で純Wと同等と
なつてMoの特徴が生かされず、10以上では炭化
物段階でWCと同等な単純ヘキサゴナルの結晶形
を有しなくなるので適当でない。したがつて合金
製造の段階でもMo/W=0.005〜10(重量)とす
るのがよい。
タングステンとモリブデンの酸化物を均一微細
化後の還元では、水素または炭素(還元と炭化を
同時に行なう)など公知の還元剤が用いられ、炭
素還元は粉末層内で生成するCOガスを媒介にし
て行なわれるので、その反応温度は炭素の活性化
温度、即ち800℃以上である。
上記合金粉末の製造にあたり、モリブデン、タ
ングステン以外のa、a、a族の1種また
はそれ以上の金属のアンモニウム塩を加えること
もでき、これにより合金の微細化および安定化が
期待できる。添加量は0.5〜40重量%が望まし
い。即ち、0.5重量%以下では顕著な添加効果が
認められず、また40重量%以上では合金が2相以
上に分解し易くなるため適当でない。
実施例 1
0.7モルのモリブデンおよび0.3モルのタングス
テンのアンモニウム溶液200ml(液温25℃)を2
ml/秒の割合で液体窒素中にスプレーで噴霧し、
急速に凍結させた。これを0.01torrまで減圧した
後、試料を液体窒素からドライアイス、食塩+
氷、氷、水溶液と徐々に昇温していき氷を昇華さ
せ、第8時間後に約50gの白色粉末を得た。この
粉末をこの粉末を大気中400℃まで1時間で昇温
し、大気を10/分流しながら40分間焙焼するこ
とによつて、34gの酸化物粉末を得た。X線回析
による構造解析およびレーザ散乱法による平均粒
度分布測定の結果、平均粒度0.16μの均質な酸化
物が形成されていることがわかつた。得られた酸
化物を水素雰囲気(10/分の水素気流)中、1
時間で900℃まで昇温し、900℃にて1時間保持し
て還元を行ない、20gの合金粉末を得た。X線に
より得られた合金の格子定数を測定したところ
3,152Åであり、完全固溶体になつていること
がわかつた。又平均粒度は0.18μであつた。
参考例 1
実施例1のようにして製造した合金粉末91.0重
量%および炭素粉末9.0重量%を混合し、この混
合粉末を水素気流中1700℃で30分間反応させた。
得られた炭化物の特性を調べたところ、第2表に
示す如く、結合炭素が理論値近く十分に入り、す
べてWCタイプのモノカーバイドになつていた。[Table] On the other hand, if the powder particles are very fine, diffusion will be easily carried out, and since iron group metals as diffusion aids will be unnecessary, it will be possible to obtain high-quality carbides. Therefore, it becomes a challenge to produce fine (Mo, W) metal powder. Traditionally, in the production of (Mo, W) metal, mechanical mixing of hydroxide in a slurry state and chemical co-precipitation of hydroxide have been mainly used; This has the disadvantage that mixing at the molecular level cannot be achieved, and the latter has the disadvantage that the acid concentration (PH) at which molybdenum and tungsten oxides are precipitated by acid decomposition is different, so the precipitated composition is not constant. Mo, W) metal could not be obtained. The inventors have now discovered that finely dispersed (Mo, W) metal can be produced for the first time by freeze-drying, and have arrived at the present invention. Freeze-drying is originally a method of drying substances that are easily decomposed by heat or that easily foam by freezing them under a high vacuum and then removing them as water vapor by sublimating the ice. When producing carbide, by using (Mo, W) metal produced by freeze-drying, it is possible to simply combine (Mo, W) metal and carbon without using a diffusion aid such as cobalt as in the past. By mixing and carbonizing the mixture, it has become possible to produce a carbide having a theoretical combined carbon content. In the present invention, the ammonium salts of molybdenum and tungsten are freeze-dried and then roasted in the air to uniformly refine the oxides of tungsten and molybdenum, which are then subjected to a reduction process to form an alloy to produce an alloy powder. The alloy powder is reacted with carbon powder to produce a composite carbide consisting of molybdenum and tungsten having a solid solution crystal structure of hexagonal monocarbide. The suitable composition of the tungsten-molybdenum solid solution particles is Mo/W=0.005 to 10 in terms of weight ratio,
If it is less than 0.005, the oxidation resistance and heat resistance will be equivalent to pure W, and the characteristics of Mo will not be utilized, and if it is more than 10, it will not have a simple hexagonal crystal form equivalent to WC in the carbide stage, so it is not suitable. Therefore, it is preferable that Mo/W=0.005 to 10 (weight) even at the stage of alloy production. After the oxides of tungsten and molybdenum are uniformly refined, a known reducing agent such as hydrogen or carbon (which performs reduction and carbonization at the same time) is used to reduce the oxides of tungsten and molybdenum. The reaction temperature is the activation temperature of carbon, that is, 800°C or higher. In producing the above-mentioned alloy powder, an ammonium salt of one or more metals in the A, A, and A groups other than molybdenum and tungsten can be added, which can be expected to refine and stabilize the alloy. The amount added is preferably 0.5 to 40% by weight. That is, if it is less than 0.5% by weight, no significant addition effect is observed, and if it is more than 40% by weight, the alloy tends to decompose into two or more phases, which is not appropriate. Example 1 200 ml of ammonium solution (liquid temperature 25°C) of 0.7 mol molybdenum and 0.3 mol tungsten was
sprayed into liquid nitrogen at a rate of ml/sec,
Frozen quickly. After reducing the pressure to 0.01 torr, the sample was transferred from liquid nitrogen to dry ice, salt +
The temperature was gradually increased through ice, ice, and an aqueous solution to sublimate the ice, and about 50 g of white powder was obtained after 8 hours. This powder was heated to 400° C. in the atmosphere for 1 hour and roasted for 40 minutes while flowing air at 10/min to obtain 34 g of oxide powder. As a result of structural analysis by X-ray diffraction and average particle size distribution measurement by laser scattering method, it was found that a homogeneous oxide with an average particle size of 0.16μ was formed. The obtained oxide was heated for 1 hour in a hydrogen atmosphere (hydrogen flow 10/min).
The temperature was raised to 900°C over an hour, and the temperature was maintained at 900°C for 1 hour to perform reduction, and 20g of alloy powder was obtained. When the lattice constant of the obtained alloy was measured using X-rays, it was found to be 3,152 Å, indicating that it was a complete solid solution. The average particle size was 0.18μ. Reference Example 1 91.0% by weight of the alloy powder produced as in Example 1 and 9.0% by weight of carbon powder were mixed, and this mixed powder was reacted in a hydrogen stream at 1700° C. for 30 minutes.
When the properties of the obtained carbide were investigated, as shown in Table 2, the amount of bonded carbon was sufficiently close to the theoretical value, and all of the carbides were WC type monocarbide.
【表】
実施例 2
実施例1による方法にて、0.7モルのモリブデ
ン、0.25モルのタングステン、0.05モルのクロム
のアンモニウム溶液200mlを液温50℃にて1ml/
秒の割合で液体窒素中にスプレーで噴霧し、急速
に凍結した。これを実施例1と同様の方法で10時
間かけて氷を昇華させ約45gの白色粉末を得た。
この粉末を大気中400℃まで1時間で昇温し、400
℃で40分間焙焼を行ない、31gの酸化粉末を得
た。X線回析による構造回析およびレーザー散乱
法による粒度分布測定の結果、平均粒度0.18μの
均質な酸化物であることがわかつた。この粉末
を、10/分の水素気流中、1時間で900℃まで
昇温し、900℃にて1時間保持して還元を行つた
ところ、22gの合金粉末を得た。この粉末は平均
粒度が0.19μであり、格子定数は3.162Åで完全
固溶体であつた。[Table] Example 2 Using the method of Example 1, 200 ml of an ammonium solution containing 0.7 mol of molybdenum, 0.25 mol of tungsten, and 0.05 mol of chromium was mixed into 1 ml/ml at a liquid temperature of 50°C.
Spray into liquid nitrogen at a rate of seconds and freeze quickly. The ice was sublimated in the same manner as in Example 1 over 10 hours to obtain about 45 g of white powder.
This powder was heated to 400℃ in the atmosphere for 1 hour, and
Roasting was performed at ℃ for 40 minutes to obtain 31 g of oxidized powder. As a result of structural analysis using X-ray diffraction and particle size distribution measurement using laser scattering method, it was found that it was a homogeneous oxide with an average particle size of 0.18μ. This powder was heated to 900° C. in 1 hour in a hydrogen flow of 10/min, and was maintained at 900° C. for 1 hour to perform reduction, and 22 g of alloy powder was obtained. This powder had an average particle size of 0.19μ, a lattice constant of 3.162Å, and was a complete solid solution.
Claims (1)
を凍結乾燥した後空気中で焙焼することによりタ
ングステンとモリブデンの酸化物を均一微細化さ
せた後、還元工程を経て合金とすることを特徴と
する、モリブデンとタングステンからなる合金粉
末の製造方法。 2 モリブデンとタングステンのアンモニウム塩
に、モリブデン、タングステン以外のa、
a、a族の1種またはそれ以上の金属のアンモ
ニウム塩を加える特許請求の範囲1記載の合金粉
末の製造方法。[Claims] 1. The invention is characterized in that the ammonium salts of molybdenum and tungsten are freeze-dried and then roasted in the air to uniformly refine the oxides of tungsten and molybdenum, which are then subjected to a reduction process to form an alloy. A method for producing an alloy powder consisting of molybdenum and tungsten. 2 In the ammonium salt of molybdenum and tungsten, a, other than molybdenum and tungsten,
2. The method for producing an alloy powder according to claim 1, wherein an ammonium salt of one or more metals of Group A and Group A is added.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6903280A JPS56166311A (en) | 1980-05-26 | 1980-05-26 | Manufacture of alloy powder containing molybdenum and tungsten |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6903280A JPS56166311A (en) | 1980-05-26 | 1980-05-26 | Manufacture of alloy powder containing molybdenum and tungsten |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56166311A JPS56166311A (en) | 1981-12-21 |
| JPS6237682B2 true JPS6237682B2 (en) | 1987-08-13 |
Family
ID=13390826
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6903280A Granted JPS56166311A (en) | 1980-05-26 | 1980-05-26 | Manufacture of alloy powder containing molybdenum and tungsten |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS56166311A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3226648C2 (en) * | 1982-07-16 | 1984-12-06 | Dornier System Gmbh, 7990 Friedrichshafen | Heterogeneous tungsten alloy powder |
| US5055441A (en) * | 1990-02-01 | 1991-10-08 | E. I. Du Pont De Nemours And Company | Process for preparation of metal oxides of molybdenum or mlybdenum and tungsten |
| JP4492877B2 (en) * | 2005-09-27 | 2010-06-30 | 日本新金属株式会社 | Method for producing high purity molybdenum-tungsten alloy powder used as raw material powder for sputtering target |
| CN110695367A (en) * | 2019-10-29 | 2020-01-17 | 金堆城钼业股份有限公司 | Preparation method of molybdenum-tungsten alloy powder |
-
1980
- 1980-05-26 JP JP6903280A patent/JPS56166311A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56166311A (en) | 1981-12-21 |
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