JPH0372569B2 - - Google Patents
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- Publication number
- JPH0372569B2 JPH0372569B2 JP58154410A JP15441083A JPH0372569B2 JP H0372569 B2 JPH0372569 B2 JP H0372569B2 JP 58154410 A JP58154410 A JP 58154410A JP 15441083 A JP15441083 A JP 15441083A JP H0372569 B2 JPH0372569 B2 JP H0372569B2
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- JP
- Japan
- Prior art keywords
- reaction
- magnesium
- temperature
- boron carbide
- hours
- Prior art date
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Description
【発明の詳細な説明】
本発明は、炭化硼素粉末の製法、さらに詳しく
は硼酸マグネシウム、マグネシウムおよび炭素の
混合物を還元および炭化反応させる炭化硼素粉末
の製造方法に関する。
従来から、炭化硼素粉末の製法としてはいろい
ろ提案されているが、工業的には硼酸や無水硼酸
等の硼素含有物質にマグネシウム等の還元性金属
および黒鉛やコークス等の炭素を添加し400〜600
℃の温度で水分や揮発分を除去した後、高温下還
元および炭化反応させ、副生した酸化マグネシウ
ム等の不純物を酸によつて除去し、炭化硼素粉末
とする方法が採用されている。さらに説明する
と、この方法は、例えば二酸化硼素、マグネシウ
ムおよび炭素を原料として次式(1)に従つて還元お
よび炭化反応を行わせるものである。
2B2O3+6Mg+C→B4C+6MgO ……(1)
この反応は発熱反応であり、約280Kcal/
B4C・molの多量の発熱を伴うため一亘反応が開
始されるとその反応は急速に進行し原料の飛散、
生成ガスの急膨張などの好ましくない現象を生ず
るので安全性に問題がある他、収率が低くまた炭
化硼素粉末の品質が悪いという欠点があつた。
これらの欠点をなくすため、原料を予め還元お
よび炭化反応の開始温度より低い温度300〜600℃
で熱処理し、水分などの揮発分を除去した後、炭
化硼素の生成温度に加熱する方法を採用している
が、発生する反応熱との作用により還元炭化反応
時に局部的な温度上昇を生じやすいこと、また原
料に微細な粒度のものを用いるにしても、原料同
志の接触機会に限度があり、反応完了に至るまで
の時間的余裕が無く、原料の飛散:あるいはマグ
ネシウムが散逸するため収率が安定しにくいとい
う欠点がある。
本発明は、これらの欠点を解決することを目的
とするもので硼酸マグネシウム、マグネシウムお
よび炭素の混合物を原料としこれを還元および炭
化反応させることにより、高純度の炭化硼素粉末
を、収率よく取得できる炭化硼素粉末の製造方法
を提供しようとするものである。
すなわち、本発明は硼酸マグネシウム、マグネ
シウムおよび炭素の混合物を高温で反応させて炭
化硼素粉末を製造する方法において、前記混合物
を温度700〜1000℃で1〜4時間熱処理した後、
さらに温度1450〜1650℃で少くとも0.5時間以上
熱処理することを特徴とする。
以下さらに本発明を詳しく説明する。
本発明において硼酸マグネシウムとは3MgO・
B2O3、および/または2MaO・B2O3を主成分と
して含有するものである。
以下本発明においてMgO・B2O3を主成分とす
る硼酸マグネシウムを例に説明するが、これによ
つて本発明は限定されるものではない。即ち、硼
酸マグネシウムを原料とする反応は、3MgO・
B2O3を例にすれば、反応式(2)で示めされる。
2(3MgO・B2O3)+6Mg+C→B4C
+12MgO……(2)
この反応は、
3MgO・B2O3+3Mg→2B+6MgO ……(3)
4B+C→B4C ……(4)
の2つの基本反応に分解される。
還元および炭化の反応式(2)の炭化硼素の収率安
定のためには、まず反応式(3)の還元反応を安定し
て完了させる必要がある。しかし、この反応の開
始温度は600〜900℃で安定しにくいこと、また反
応式(2)のマグネシウムが650℃で融液となり、蒸
気圧が著しく高くなるため反応系外に散逸しやす
い。
また、反応式(3)で生じる硼素は、いわゆるモア
サンの硼素と呼ばれる非常に活性に富むものであ
るが、通常数%程度のマグネシウムや酸素を含ん
でいる。この硼素は反応式(4)に従つて、あらかじ
め配合された炭素と反応して炭化硼素となる。こ
の反応は1450℃以上で急速に進行するが、同時に
硼素中に含まれていたマグネシウムや酸素のほと
んどは酸化マグネシウム等に変化し、炭化硼素の
純化が行われる。
本発明は、前記反応を効率よく行うために、
700〜1000℃の温度で1〜4時間保持し、マグネ
シウムの蒸気圧を低く保持しながら、反応式(3)で
示す還元反応を完了させることによつて収率の安
定を図り、その後1450〜1650℃の温度まで少くと
も0.5時間以上加熱し、炭化硼素とすることを特
徴とするものである。以下さらに本発明を詳しく
説明する。
原料の熱処理において、第1段の熱処理温度を
700〜1000℃に限定した理由は、700℃未満の温度
では還元反応が実質的に進行しないし、1000℃を
越えるとマグネシウムの揮散が著しく、還元反応
が安定して完了しにくいためである。また、この
温度での保持時間は1〜4時間である。1時間未
満では反応が充分進行しないし、また4時間を越
えるとそれ以上の反応の進行は認められないから
である。
次に、第2段の熱処理温度は1450〜1650℃であ
り、このように限定した理由は1450℃未満では式
(4)の炭化反応が充分に進行せず、また1650℃を越
えると反応式(5)で示す反応が急速となり収率低下
が著しくなるからである。また、この温度で少く
とも0.5時間保持することが必要である。0.5時間
未満では反応が充分に進行せず高純度の炭化硼素
を得ることが難い。
B4C+5MgO→4BO↑+5Mg↑+CO↑ ……(5)
以上説明したように本発明は特定の硼酸マグネ
シウム、マグネシウムおよび炭素を高温で反応さ
せて炭化硼素粉末を製造する方法において、第1
段熱処理を700〜1000℃で1〜4時間第2段熱処
理を1450〜1650℃で少くとも0.5時間以上行う方
法であつて、本発明によれば従来法に比べて炭化
硼素を製造する際に、発生する反応の急速な進行
を防止することができるので、安全性に問題はな
く、しかも高品質の炭化硼素が収率よく得られる
という利点がある。
実施例
工業用硼酸(USボラツクス社製)1500gと、
軟質工業用酸化マグネシウム(神島化学製スター
マグU)1500gを混合し、この混合物をアルミナ
製ルツボに収め、大気雰囲気下1000℃で4時間焼
成した。その粉末のX線回析によれば3MgO・
B2O3を主要鉱物とし、少量の2MgO・B2O3を含
む硼酸マグネシウムであつた。
上記操作で得た硼酸マグネシウム2054gに、マ
グネシウム粉(山石金属製−100メツシユ)828g
および人造黒鉛粉(ロンザ社商品名「KS−15」)
68gを加え、充分に混合した後、黒鉛製ルツボに
充填し、アルゴンガス雰囲気下表に示した加熱条
件により熱処理を行つた。その生成物をボールミ
ルで粉砕した後、これを温度90℃に加熱した15%
塩酸溶液中に浸漬し副生酸化マグネシウムを除去
した。次に、ガラスフイルターを用いてこれを濾
別し、ケーキを160℃で真空乾燥して炭化硼素298
gを得た。その収率および化学分析値を表に示
す。
比較例
熱処理条件を表のように変えた以外は実施例と
同様に行つた。
【表】DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing boron carbide powder, and more particularly to a method for producing boron carbide powder in which a mixture of magnesium borate, magnesium, and carbon is reduced and carbonized. Various methods have been proposed to produce boron carbide powder, but industrially, reducing metals such as magnesium and carbon such as graphite and coke are added to boron-containing substances such as boric acid and boric anhydride.
The method used is to remove moisture and volatile matter at a temperature of °C, then perform a reduction and carbonization reaction at high temperatures, and remove by-product impurities such as magnesium oxide with acid to obtain boron carbide powder. To explain further, in this method, for example, boron dioxide, magnesium and carbon are used as raw materials to perform a reduction and carbonization reaction according to the following formula (1). 2B 2 O 3 +6Mg+C→B 4 C+6MgO...(1) This reaction is exothermic and approximately 280Kcal/
Since a large amount of heat is generated by B 4 C・mol, once the reaction starts, it progresses rapidly, causing the raw materials to scatter,
In addition to causing safety problems due to undesirable phenomena such as rapid expansion of the produced gas, there are also disadvantages of low yield and poor quality of boron carbide powder. In order to eliminate these drawbacks, the raw materials are heated in advance to a temperature of 300 to 600℃ lower than the starting temperature of the reduction and carbonization reaction.
After heat treatment to remove volatile components such as moisture, the method is heated to the temperature at which boron carbide is produced.However, due to the reaction heat generated, local temperature increases tend to occur during the reductive carbonization reaction. In addition, even if fine particles are used as raw materials, there is a limit to the opportunities for contact between the raw materials, and there is not enough time to complete the reaction, resulting in scattering of the raw materials or the dissipation of magnesium, resulting in lower yields. The disadvantage is that it is difficult to stabilize. The purpose of the present invention is to solve these drawbacks. By using a mixture of magnesium borate, magnesium, and carbon as a raw material and subjecting it to a reduction and carbonization reaction, high-purity boron carbide powder can be obtained in good yield. The present invention aims to provide a method for producing boron carbide powder that can be produced using the following methods. That is, the present invention provides a method for producing boron carbide powder by reacting a mixture of magnesium borate, magnesium, and carbon at high temperature, in which the mixture is heat-treated at a temperature of 700 to 1000°C for 1 to 4 hours, and then
It is further characterized by heat treatment at a temperature of 1450 to 1650°C for at least 0.5 hours or more. The present invention will be further explained in detail below. In the present invention, magnesium borate is 3MgO.
It contains B 2 O 3 and/or 2MaO.B 2 O 3 as a main component. In the following, the present invention will be explained using magnesium borate containing MgO.B 2 O 3 as a main component, but the present invention is not limited thereto. In other words, the reaction using magnesium borate as a raw material produces 3MgO.
Taking B 2 O 3 as an example, the reaction is shown by reaction formula (2). 2 (3MgO・B 2 O 3 ) + 6Mg + C → B 4 C
+12MgO...(2) This reaction is decomposed into two basic reactions: 3MgO・B 2 O 3 +3Mg→2B+6MgO...(3) 4B+C→B 4 C...(4). In order to stabilize the yield of boron carbide in reaction formula (2) of reduction and carbonization, it is first necessary to stably complete the reduction reaction in reaction formula (3). However, the starting temperature of this reaction is 600 to 900°C, which is difficult to stabilize, and the magnesium in reaction formula (2) becomes a melt at 650°C, resulting in a significantly high vapor pressure, which easily dissipates out of the reaction system. Further, the boron produced in reaction formula (3) is so-called Moisan boron and is highly active, but it usually contains about several percent of magnesium and oxygen. This boron reacts with carbon mixed in advance to form boron carbide according to reaction formula (4). This reaction progresses rapidly at temperatures above 1450°C, but at the same time, most of the magnesium and oxygen contained in boron are converted to magnesium oxide, etc., and boron carbide is purified. In order to efficiently carry out the reaction, the present invention provides the following features:
The yield is stabilized by holding at a temperature of 700 to 1000°C for 1 to 4 hours to complete the reduction reaction shown in reaction formula (3) while keeping the vapor pressure of magnesium low. It is characterized in that it is heated to a temperature of 1650°C for at least 0.5 hours to form boron carbide. The present invention will be further explained in detail below. In the heat treatment of raw materials, the first stage heat treatment temperature is
The reason why the temperature is limited to 700 to 1000°C is that at temperatures below 700°C, the reduction reaction does not substantially proceed, and at temperatures above 1000°C, magnesium volatilization is significant, making it difficult for the reduction reaction to stabilize and complete. Further, the holding time at this temperature is 1 to 4 hours. This is because if the reaction time is less than 1 hour, the reaction will not proceed sufficiently, and if the reaction time exceeds 4 hours, no further progress of the reaction will be observed. Next, the heat treatment temperature in the second stage is 1450 to 1650℃, and the reason for this limitation is that below 1450℃, the formula
This is because the carbonization reaction (4) does not proceed sufficiently, and when the temperature exceeds 1650°C, the reaction shown in reaction formula (5) becomes rapid and the yield decreases significantly. It is also necessary to hold at this temperature for at least 0.5 hour. If the time is less than 0.5 hours, the reaction will not proceed sufficiently and it will be difficult to obtain highly pure boron carbide. B 4 C + 5MgO → 4BO↑ + 5Mg↑ + CO↑ ...(5) As explained above, the present invention provides a method for producing boron carbide powder by reacting specific magnesium borate, magnesium, and carbon at high temperature.
A method in which stage heat treatment is performed at 700 to 1000°C for 1 to 4 hours, and second stage heat treatment is performed at 1450 to 1650°C for at least 0.5 hours, and according to the present invention, when manufacturing boron carbide, compared to conventional methods, Since rapid progress of the reaction that occurs can be prevented, there is no problem with safety, and there is an advantage that high quality boron carbide can be obtained in good yield. Example: 1500g of industrial boric acid (manufactured by US Borax),
1500 g of soft industrial magnesium oxide (Star Mag U manufactured by Kamishima Chemical Co., Ltd.) was mixed, and this mixture was placed in an alumina crucible and fired at 1000° C. for 4 hours in an air atmosphere. According to the X-ray diffraction of the powder, 3MgO・
It was a magnesium borate containing B 2 O 3 as the main mineral and a small amount of 2MgO.B 2 O 3 . To 2054 g of magnesium borate obtained in the above procedure, 828 g of magnesium powder (manufactured by Yamaishi Metal - 100 mesh)
and artificial graphite powder (Lonza product name “KS-15”)
After adding 68 g and thoroughly mixing, the mixture was filled into a graphite crucible and heat-treated under the heating conditions shown in the table under an argon gas atmosphere. After grinding the product in a ball mill, it was heated to a temperature of 90℃ to 15%
By-product magnesium oxide was removed by immersing it in a hydrochloric acid solution. Next, this was filtered out using a glass filter, and the cake was vacuum-dried at 160°C to remove boron carbide 298
I got g. The yield and chemical analysis values are shown in the table. Comparative Example The same procedure as in Example was carried out except that the heat treatment conditions were changed as shown in the table. 【table】
Claims (1)
の混合物を高温で反応させて炭化硼素粉末を製造
する方法において、前記混合物を温度700〜1000
℃で1〜4時間熱処理した後、さらに温度1450〜
1650℃で少くとも0.5時間以上熱処理することを
特徴とする炭化硼素粉末の製造方法。 2 硼酸マグネシウムが3MgO・B2O3および/
または2MgO・B2O3を主成分とするものからな
る特許請求の範囲第1項記載の製造方法。[Claims] 1. A method for producing boron carbide powder by reacting a mixture of magnesium borate, magnesium and carbon at high temperature, wherein the mixture is heated at a temperature of 700 to 1000.
After heat treatment at ℃ for 1 to 4 hours, further temperature 1450 ~
A method for producing boron carbide powder, characterized by heat treatment at 1650°C for at least 0.5 hours. 2 Magnesium borate is 3MgO・B 2 O 3 and/
or 2MgO.B 2 O 3 as a main component, the manufacturing method according to claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58154410A JPS6046909A (en) | 1983-08-24 | 1983-08-24 | Production of boron carbide powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58154410A JPS6046909A (en) | 1983-08-24 | 1983-08-24 | Production of boron carbide powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6046909A JPS6046909A (en) | 1985-03-14 |
| JPH0372569B2 true JPH0372569B2 (en) | 1991-11-19 |
Family
ID=15583537
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58154410A Granted JPS6046909A (en) | 1983-08-24 | 1983-08-24 | Production of boron carbide powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6046909A (en) |
-
1983
- 1983-08-24 JP JP58154410A patent/JPS6046909A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6046909A (en) | 1985-03-14 |
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