JPS6365948A - Preparation of solid phase synthetic substance - Google Patents
Preparation of solid phase synthetic substanceInfo
- Publication number
- JPS6365948A JPS6365948A JP61209966A JP20996686A JPS6365948A JP S6365948 A JPS6365948 A JP S6365948A JP 61209966 A JP61209966 A JP 61209966A JP 20996686 A JP20996686 A JP 20996686A JP S6365948 A JPS6365948 A JP S6365948A
- Authority
- JP
- Japan
- Prior art keywords
- particle size
- solid phase
- less
- crushed
- particulate material
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Silicon Compounds (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、粒度が100μ以下の超微粉及び100μ〜
1,000μ程度の微粉(以下、単に微粉と言う)を複
数種類組合せて固相合成物を製造する方法に関する。Detailed Description of the Invention (Field of Industrial Application) The present invention provides ultrafine powder with a particle size of 100μ or less and ultrafine powder with a particle size of 100μ to
The present invention relates to a method for producing a solid-phase composite by combining multiple types of fine powder of about 1,000 microns (hereinafter simply referred to as fine powder).
(従来技術)
従来、上記同相合成物を製造する場合には、複数種類の
原料微粉を混合機で均一に混合し、該混合物を反応容器
に入れて高温加熱して化学反応を起させ、以て結晶状の
同相合成物をt;)でいる。(Prior art) Conventionally, when producing the above-mentioned in-phase composite, multiple types of raw material fine powders are uniformly mixed in a mixer, and the mixture is placed in a reaction vessel and heated at high temperature to cause a chemical reaction. The crystalline in-phase compound is t;).
(発明が解決しようとする問題点)
しかし上記方法では、混合物の構成粒子相互の接触が粗
いため高温加熱しても合成反応効率が悪く、また合成物
が得られた場合でも、その強度や密度が低かった。また
組合せる原料微粉間に大きな粒度差やかさ密度差がある
場合には、混合後化学合成工程までの間に偏析を生じて
混合状態が不均一になり、均質な固相合成物を得ること
ができなかった。更に原料微粉の混合物は飛散しやすく
、取扱いが厄介であった。(Problems to be Solved by the Invention) However, in the above method, the synthesis reaction efficiency is low even when heated at high temperature due to rough contact between the constituent particles of the mixture, and even when a composite is obtained, its strength and density was low. In addition, if there is a large difference in particle size or bulk density between the raw material fine powders to be combined, segregation may occur during the chemical synthesis process after mixing, resulting in an uneven mixing state and making it difficult to obtain a homogeneous solid phase composite. could not. Furthermore, the mixture of raw material fine powders was easily scattered and was difficult to handle.
本発明は上記のような事情に鑑みてなされたものであり
、複数種類の原料微粉から強度や密度の大きい同相合成
物を効率よく製造する方法を提供することを目的として
いる。The present invention has been made in view of the above-mentioned circumstances, and an object of the present invention is to provide a method for efficiently producing a homogeneous composite having high strength and density from a plurality of types of raw material fine powder.
C問題点を解決するための手段)
すなわち本発明による同相合成物の製造方法は、複数種
類の原料微粉を均一に混合し、践混合物を所定形状に圧
縮成形し、該成形物を粉砕して粒度が12朋以下の粒状
体と成し、該粒状体をそのまま、を起させることを特徴
としている。Means for Solving Problem C) That is, the method for producing an in-phase composite according to the present invention involves uniformly mixing multiple types of raw material fine powder, compressing the mixture into a predetermined shape, and pulverizing the molded product. It is characterized in that it is formed into granules with a particle size of 12 mm or less, and the granules are allowed to rise as they are.
(実施例)
以下、本発明を実施例に基づいて詳細に説明すると、図
面は本発明に係る固相合成物の製造工程を示し、複数の
種類の原料微粉(1) (2)及び反応助剤、結合剤等
(3)は各々計示機(4) (5) (6)で所定比に
なるよう計量され、混合機(7)(マラー型又はかく押
型)に投入されて均一に混合される。(Example) Hereinafter, the present invention will be explained in detail based on Examples. The drawings show the manufacturing process of the solid-phase composite according to the present invention, and show a plurality of types of raw material fine powder (1) (2) and a reaction aid. Agents, binders, etc. (3) are each weighed to a predetermined ratio using measuring machines (4), (5), and (6), and then put into a mixer (7) (Maller type or stamping type) to mix them uniformly. be done.
該原料微粉の混合物(8)は、次に加圧圧縮成形機(9
)(プレス式又はロール式)にかけられて所定形状に圧
縮成形され、該圧縮成形物(11)は更に、解砕機(1
2) (ハンマー型、歯型又はロール型)で粒度12M
M以下に解砕される。このようにして解砕された粒状体
(13)は篩(14)にかけられて粒度分布1〜5WI
Nに整粒された上、化学合成工程(15)にて図示しな
い反応容器に入れられ、約1,500〜2,500°C
の範囲で加熱され、同相反応により結晶状の固相合成物
(16)となる。The mixture (8) of the raw material fine powder is then passed through a pressure compression molding machine (9).
) (press type or roll type) to compression mold into a predetermined shape, and the compression molded product (11) is further passed through a crusher (11).
2) Particle size 12M (hammer type, tooth type or roll type)
It is crushed to less than M. The thus crushed granules (13) are passed through a sieve (14) with a particle size distribution of 1 to 5 WI.
After being sized to N, it is placed in a reaction vessel (not shown) in the chemical synthesis step (15) and heated at approximately 1,500 to 2,500°C.
The mixture is heated in a range of 100 to 1000 mL, and a crystalline solid phase compound (16) is formed by an in-phase reaction.
なお前記粒状体(13)のうち粒度が1朋以下のものは
前記混合機(7)に再投入されて原料微粉(1)(2)
その他と共に混合され、また粒度が5朋以上のものは前
記解砕@(12)に再投入されて圧縮成形物(11)と
共に解砕される。Note that among the granules (13), those with a particle size of 1 tom or less are re-injected into the mixer (7) and turned into fine raw material powders (1) and (2).
Those mixed with others and having a particle size of 5 or more are re-injected into the crushing@(12) and crushed together with the compression molded product (11).
なお前記解砕機(12)で粒度12朋以下に解砕された
粒状体(13)は、微粉の柱類と化学合成工程(15)
における同相反応条件によっては、篩(14)にかける
ことなく直接化学合成工程(15)へ送られることもあ
る。The granules (13) crushed to a particle size of 12 mm or less by the crusher (12) are separated into columns of fine powder and chemical synthesis process (15).
Depending on the in-phase reaction conditions in , it may be sent directly to the chemical synthesis step (15) without passing through the sieve (14).
次に上記製造工程によって同相合成物を製造した実例を
下記に示す。Next, an example of producing an in-phase composite by the above production process will be shown below.
第1実施例
珪石粉(粒度約50μ以下、かさ密度0.6〜)40重
量部、黒鉛粉又はオイルコークス粉(粒度約50μ以下
、かさ密度0.7’/Δ)40重量部、木粉18重量部
、塩2重量部、結合剤として澱粉又はPVA (ポリビ
ニールアルコール)3重量部及び水15重量部をそれぞ
れ計量し、これら計量物をマラー型混合機に投入してマ
ラーに線圧2〜4にμの荷重をかけ、5分間回転作動さ
せて原料を均一に混合する。1st Example 40 parts by weight of silica powder (particle size of about 50μ or less, bulk density 0.6~), 40 parts by weight of graphite powder or oil coke powder (particle size of about 50μ or less, bulk density 0.7'/Δ), wood flour 18 parts by weight, 2 parts by weight of salt, 3 parts by weight of starch or PVA (polyvinyl alcohol) as a binder, and 15 parts by weight of water, and these weighed items were put into a Muller-type mixer, and the linear pressure was 2 parts by weight. Apply a load of μ to ~4 and rotate for 5 minutes to mix the raw materials uniformly.
次に該混合物をプレス式加圧圧縮成形機にかけて2〜4
tOn/1の加圧力を加え、直径20朋、厚さ約10〜
15MMの円盤状成形物にする。しかる後、該成形物を
解砕機で粒度12 ml以下に解砕した上筒にかけ、粒
度分布1〜5羽に整粒して乾燥させる。このようにして
得られた粒状物を図示しない反応容器に入れて約1,9
00°Cで加熱して、強度や密度の高い炭化珪素の同相
合成物を得た。Next, the mixture was applied to a press-type pressure compression molding machine for 2 to 4 hours.
Apply pressure of tOn/1, diameter 20mm, thickness about 10~
Make a 15 MM disc-shaped molded product. Thereafter, the molded product is crushed in a crusher to a particle size of 12 ml or less, placed on an upper cylinder, sized to a particle size distribution of 1 to 5 particles, and dried. The granules thus obtained were placed in a reaction container (not shown) and approximately 1.9
By heating at 00°C, an in-phase composite of silicon carbide with high strength and density was obtained.
なお上記加圧圧縮工程で、混合物をロール式加圧圧縮機
にかけて線圧2〜6t00//crnの加圧力を加え、
寸法が19X14X9羽のアーモンド形成形物に圧縮成
形した場合においても、同様の固相合成物が得られた。In addition, in the pressure compression step, the mixture is applied to a roll-type pressure compressor to apply a linear pressure of 2 to 6 t00//crn,
A similar solid phase composite was obtained when compression molded into almond shapes with dimensions of 19X14X9 wings.
また本粉や塩は珪石粉や黒鉛粉又はオイルコークス粉の
種類により、添加量に増減がある。Further, the amount of this powder and salt added varies depending on the type of silica powder, graphite powder, or oil coke powder.
第2実施例
ホウ酸粉(粒度約50μ以下、かさ密度o、s’/H)
40重量部、黒鉛粉又はオイルコークス粉(粒度約50
μ以下、かさ密度0.7?/屑)40重量部、木粉18
重量部、塩2重量部、結合剤として澱粉又はPVA3重
示部及び水15重量部を原料とし、第1実施例の場合と
同様にして混合、加圧圧縮及び解砕を行い、粒度分布1
〜5flの粒状体にし、これを図示しない反応容器に入
れた上、電気炉で約2,500°Cに加熱して、強度や
密度の高い炭化ホウ素の固相合成物を得た。Second Example Boric acid powder (particle size approximately 50μ or less, bulk density o, s'/H)
40 parts by weight, graphite powder or oil coke powder (particle size approximately 50
Less than μ, bulk density 0.7? / scraps) 40 parts by weight, wood flour 18
Parts by weight, 2 parts by weight of salt, 3 parts by weight of starch or PVA as a binder, and 15 parts by weight of water were mixed, compressed and crushed in the same manner as in the first example to obtain a particle size distribution of 1.
This was made into granules of ~5 fl, placed in a reaction vessel (not shown), and heated to about 2,500°C in an electric furnace to obtain a solid phase composite of boron carbide with high strength and density.
第3実施例
珪素粉(粒度約50μ以下、かさ密度0.5〜0.67
)とマグネシウム粉C粒度約700μ以下、かさ密度0
.7〜0.8〜)とを同量比か又はマグネシウム粉80
重量%程度までの配合比とし、窒素ガスによる不活性雰
囲気下で第1実施例の場合と同様にして均のアーモンド
形成形物とし、これを解砕機で粒度12羽以下の粒状体
に解砕し、該粒状体を図示しない反応容器に入れた上、
高温加熱して、均質な珪素マグネシウムの固相合成物を
得た。Third Example Silicon powder (particle size approximately 50μ or less, bulk density 0.5 to 0.67
) and magnesium powder C particle size approximately 700μ or less, bulk density 0
.. 7-0.8-) in the same ratio or magnesium powder 80
The blending ratio was adjusted to about % by weight, and the same method as in the first embodiment was made under an inert atmosphere of nitrogen gas to form a uniform almond shape, which was then crushed into granules with a particle size of 12 feathers or less using a crusher. Then, the granules were placed in a reaction container (not shown), and
A homogeneous silica-magnesium solid-phase composite was obtained by heating at high temperature.
なお本実施例の混合工程で、マラー型混合機に代えてか
く押型混合機を使用しても混合効果はほぼ同じであった
。In addition, in the mixing process of this example, the mixing effect was almost the same even if a push-type mixer was used instead of the Muller-type mixer.
第4実施例
タングステン粉c粒度200μ以下、かさ密度4,5〜
)約90重量部、黒鉛粉(粒度501・以下、かさ密度
0.2外り約10重量部、結合剤としてPVA約1重量
部及び水約1重量部を原料とし、第1実施例の場合と同
様にして均一に混合する。次に該混合物をロール式加圧
圧縮成形機にかけて線圧2〜6tOn//、Iにて寸法
19X14X9朋のアーモンド形成形物に圧縮成形し、
これを解砕して1〜5Hの粒状体に整粒し、該粒状体を
図示しない反応容器に入れた上、電気炉で約1,500
°Cに加熱して、均質な炭化タングステンの固相合成物
を得た。Fourth example tungsten powder c particle size 200μ or less, bulk density 4.5~
), about 90 parts by weight of graphite powder (particle size 501 mm or less, bulk density 0.2 or less, about 10 parts by weight, about 1 part by weight of PVA and about 1 part by weight of water as a binder, in the case of the first example) Mix uniformly in the same manner as above.Next, the mixture is compressed into an almond shape having dimensions of 19 x 14 x 9 using a roll pressure compression molding machine at a linear pressure of 2 to 6 tOn///I,
This was crushed and sized into granules of 1 to 5H, and the granules were placed in a reaction vessel (not shown), and then heated in an electric furnace to a size of about 1,500
C. to obtain a homogeneous tungsten carbide solid phase composite.
(発明の効果)
以上の説明から明らかなように、本発明は複数種類の原
料微粉を混合機で均一に混合した後、該混合物を化学合
成工程の前に加圧圧縮成形し、更に所定粒度に解砕して
構成粒子相互の接触が密な粒状体となしたから、固相反
応効率が良く、得られた合成物の強度や密度も向上する
。また組合せる原料微粉間に大きな粒度差やかさ密度差
がある場合(第3実施例及び第4実施例)でも、混合径
粒状体にされることにより偏析を生ずることがなく、均
一な混合状態で高温反応に供することができるから、均
質な内相合成物を得ることができろ。(Effects of the Invention) As is clear from the above description, the present invention involves uniformly mixing multiple types of raw material fine powders in a mixer, then pressurizing and compression molding the mixture before the chemical synthesis process, and further obtaining a predetermined particle size. Since the particles are crushed into granules in which the constituent particles are in close contact with each other, the solid phase reaction efficiency is high, and the strength and density of the resulting composite are also improved. In addition, even if there is a large difference in particle size or bulk density between the raw material fine powders to be combined (as in the third and fourth embodiments), by forming them into mixed diameter granules, segregation will not occur and a uniform mixing state will be maintained. Since it can be subjected to high-temperature reactions, a homogeneous internal phase compound can be obtained.
更に原料微粉は混合径粒状体にされるため飛散すること
がなく、取扱いが容易になる。Furthermore, since the raw material fine powder is made into granules with mixed diameters, it does not scatter, making it easier to handle.
肉面は本発明に係る同相合成物の製造工程を示す。 ・夛〆 特許出願人 新東工業株式会社1..・シト≦ The meat side shows the manufacturing process of the in-phase composite according to the present invention. ・夛〆 Patent applicant: Shinto Kogyo Co., Ltd. 1. ..・Sito≦
Claims (1)
状に圧縮成形し、該成形物を粉砕して粒度が12mm以
下の粒状体と成し、該粒状体をそのまま、若しくは粒度
分布が1〜5mmとなるよう整粒した後、これを高温加
熱反応させることを特徴とする固相合成物の製造方法。Multiple types of raw material fine powders are uniformly mixed, the mixture is compression molded into a predetermined shape, the molded product is crushed to form granules with a particle size of 12 mm or less, and the granules can be used as is or with a particle size distribution of 1. A method for producing a solid-phase composite, which comprises sizing the particles to a size of ~5 mm and then subjecting the particles to a high-temperature heating reaction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61209966A JPS6365948A (en) | 1986-09-05 | 1986-09-05 | Preparation of solid phase synthetic substance |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61209966A JPS6365948A (en) | 1986-09-05 | 1986-09-05 | Preparation of solid phase synthetic substance |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6365948A true JPS6365948A (en) | 1988-03-24 |
Family
ID=16581628
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61209966A Pending JPS6365948A (en) | 1986-09-05 | 1986-09-05 | Preparation of solid phase synthetic substance |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6365948A (en) |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS52144000A (en) * | 1976-05-26 | 1977-11-30 | Ibiden Co Ltd | Industrial continuous production of carbide |
| JPS6047753A (en) * | 1983-08-26 | 1985-03-15 | 中西金属工業株式会社 | Duplex type trolley-conveyor |
-
1986
- 1986-09-05 JP JP61209966A patent/JPS6365948A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS52144000A (en) * | 1976-05-26 | 1977-11-30 | Ibiden Co Ltd | Industrial continuous production of carbide |
| JPS6047753A (en) * | 1983-08-26 | 1985-03-15 | 中西金属工業株式会社 | Duplex type trolley-conveyor |
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