JPH0415191B2 - - Google Patents
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- JPH0415191B2 JPH0415191B2 JP62162240A JP16224087A JPH0415191B2 JP H0415191 B2 JPH0415191 B2 JP H0415191B2 JP 62162240 A JP62162240 A JP 62162240A JP 16224087 A JP16224087 A JP 16224087A JP H0415191 B2 JPH0415191 B2 JP H0415191B2
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Description
〔技術分野〕
本発明は粉末成形体中の添加剤の除去方法に関
し、より詳しくは、セラミツクス焼結体を得るた
めに、射出成形法または泥漿鋳込み成形法で成形
された粉末成形体より、成形助剤として用いられ
た添加剤を加熱・飛散させる方法、いわゆる粉末
成形体の脱脂方法に関する。
〔背景技術〕
形状が複雑でかつ量産されるセラミツクス焼結
体は、原料であるアルミナ、ジルコニア、炭化ケ
イ素、窒化ケイ素などの粉末を、射出成形法また
は泥漿鋳込み成形法によつて所望する形状に成形
し、脱脂後、ついでこの粉末成形体が焼結するに
必要な温度に強熱することにより工業的に生産さ
れている。
ここでいう射出成形法とは、上記アルミナなど
の粉末と混練されたとき、全体として可塑性を示
し成形し易くなるような、例えばポリスチレン、
ポリエチレン、ジエチレンフタレート、パラフイ
ン、脂肪酸エステル、ポリビニルアルコールなど
の添加剤を、粉末100重量部に対して20〜35重量
部加えて混練し、この混練物を所望する形状の金
型に圧入して成型する方法である。得られた粉末
成形体は金型から取り出され、添加剤を加熱によ
り飛散除去された後、強熱することによつて所望
する形状のセラミツクス焼結体とすることができ
る。
また、泥漿鋳込み成形法とは、アルミナなどの
粉末100重量部対して、水または水とアルコール
などとの混合物からなる添加剤20〜40重量部と、
少量のHCl、AlCl3、NaOH、水ガラスなどの解
膠剤を添加してよく混合し、流動性がありかつ粉
末が沈降しにくい安定な泥漿とし、この泥漿を石
膏のような多孔質からなる鋳型に流し込み、少な
くとも泥漿に含まれる添加剤を泥漿の流動性がな
くなるまで鋳型に吸収させた後、鋳型により粉末
成形体として取り出す方法である。この方法で得
られた粉末成形体には通常10〜15重量%の水など
の添加剤が残存するので、射出成形法の場合と同
様に、この残存した添加剤を加熱により飛散させ
た後、例えば、1300〜2300℃程度で強熱すること
によつてセラミツクス焼結体とすることができ
る。
以下、本発明においては、射出成形法および泥
漿鋳込み成形法において粉体に添加する熱可塑
剤、可塑剤、分散剤、溶剤等を総称して添加剤と
称することにする。なお、上記射出成形法及び泥
漿鋳込み成形法により得られた成形体中の残存す
るかかる添加剤を、加熱により飛散させる操作を
該技術分野における当業者の慣例用語を用い、以
下「脱脂」と表記する。
しかしながら、上記の如き方法、すなわち射出
成形法または泥漿鋳込み成形法によつて得られた
粉末成形体を、脱脂後強熱する方法によつて得ら
れたセラミツクス焼結体は、亀裂や表面剥離など
欠陥のある不良品(製品とはなし得ないもの)が
少なからずに発生すると云う問題がある。
更に、これらの欠陥が焼結体内部に発生したも
のは、製品化の段階で欠陥を発見することが困難
なため一部はそのまま製品化されてしまい、使用
中に破損し事故の原因となるという大きな問題も
ある。
しかしてここで特に指摘したいのは、上記亀裂
や表面剥離などの欠陥はその殆んどが脱脂工程に
おいて発明するということである。
すなわち、粉末成形体に添加剤が残存している
と、この粉末成形体を強熱してセラミツクス焼結
体とする際に、該残存添加剤が急激に気化し、こ
の膨張力のため、セラミツクス焼結体中に割れや
亀裂が発明する。これを防止する目的で粉末成形
体は強熱に先立つて脱脂工程を設け、添加剤を除
去しておくのである。従つて自明のことながら、
脱脂工程においては添加剤は極力完全に除去する
ことが望ましい。
しかしながら、粉末成形体は上述したように、
泥漿鋳込み成形法の場合でも10重量%以上、射出
成形体の場合においては更に多くの、即ち20重量
%以上もの添加剤を含んでいる。この様に多量の
添加剤を含んだ粉末成形体から、割れや亀裂を発
生させることなく、加熱により添加剤を飛散除去
させることは、該加熱飛散に伴う添加剤の大きな
膨張力が機械的強度の極めて低い粉末成形体に強
く作用するために、本質的に極めて難しい問題な
のである。
したがつて、従来この工程は、大気圧あるいは
5Kg/cm2程度以下の加圧下で粉末成形体を最高で
600℃程度に加熱して、添加剤を気化、分解、燃
焼などで飛散除去させることによつて行われてい
るが、このように添加剤の膨張力を低く抑える必
要上、粉末成形体の昇温速度は1〜3℃/hとい
つた極めて遅い条件で行われている。脱脂工程は
このような緩慢な昇温速度を採用せざるを得ない
ため、通常5〜7日間もの長時間を要し、著しく
生産性が阻害させるといつた問題があつた。
また、射出成形法においては、添加剤の量を多
くすると、脱脂工程で添加剤が除去されたときに
できる空〓が増すため、添加剤としてはその量が
できるだけ少なくて、しかも成形し易い性能が要
求され、同時に加熱・飛散させ易い性質も併せ要
求される。しかしながら、このような性能をいず
れも満足させることは、前記したポリスチレン、
ポリエチレンなどの高価なものを用いても、本質
的に極めて難しいといつた問題があつた。
更に、脱脂した粉末成形体は機械的強度が殆ど
零であるので、該成形体を次の焼結工程へ移行も
しくは輸送する過程で、僅かな振動、揺れ等によ
つて容易に割れや亀裂が発生し易く、これを防ぐ
ためにはこの際の振動、揺れなどを可能な限り防
止する必要があつた。
このように、著しく生産性が低く、極めて慎重
な操作を行つて生産されているにもかかわらず、
得られたセラミツクス焼結体には少なからず不良
品が発生し、その原因は主にこの脱脂工程で発生
する粉末成形体の欠陥に起因しているのが実情で
あつた。
〔発明の要旨〕
本発明は、このような従来技術の欠点を全く新
しい方法で解決することを目的としたもので、本
発明の方法に従えば脱脂工程を極めて短時間に行
うことができ、併せて上記した如き粉末成形体の
欠陥の発生を著しく抑えることが可能な新規な脱
脂方法が提供される。
〔発明の開示〕
本発明者らは従来技術の欠点を根本的になくす
ことを目的として鋭意検討を重ねた結果、極めて
低温でかつ短時間に添加剤を除去しても、粉末成
形体における割れや亀裂などの欠陥の発生を従来
よりも著しく抑えることができる方法を見出し、
本発明を完成するに至つたものである。
即ち、本発明の上記目的は、粉末に添加剤を加
えて成形した粉末成形体より該添加剤を加熱・飛
散させて除去する方法であつて、予め該粉末成形
体の表面の少なくとも一部を露出面として残すほ
かは残余を気密性がある樹脂薄膜で被覆し、該被
覆した面を静水圧加圧した状態で該粉末成形体を
加熱し、該添加剤を該露出面を通して飛散せしめ
ることによつて達成される。
〔発明を実施するための具体的要件〕
以下、本発明を詳細に説明する。
本発明では未だ添加剤を含んだ状態の粉末成形
体、例えば射出成形法や泥漿込み成形法等によつ
て得られた未だ添加剤を含んだ状態の粉末成形体
を脱脂するに当たり、予め粉末成形体の表面を一
部露出面として残す他は、残余を気密性がある樹
脂薄膜で被覆する。
かかる樹脂薄膜による被覆は、例えば溶媒が揮
発することや化学反応によつて固化する液状の樹
脂を成形体の表面に直接塗布、吹き付け、もしく
は浸漬−引き上げ等により薄く塗布し、必要によ
り乾燥や加熱等の処理を加えることによつて表面
に樹脂塗膜を形成せしめることにより実施するこ
とができる。この方法に使用可能な液状の樹脂を
列記すると、例えば、酢酸ビニル系エマルジヨ
ン、スチレンブタジエン系ラテツクス、アクリル
系エマルジヨン、天然ゴムラテツクスなどの工業
的に製造されている樹脂を挙げることが出来る。
また、ポリウレタン樹脂、ケイ素樹脂、エポキシ
樹脂、アクリル樹脂、ポリエステル樹脂、クロル
プレン樹脂、フエノール樹脂等も使用可能であ
る。さらにまた、アクリル樹脂、エポキシ樹脂、
ポリエステル樹脂などの中には、粉体の状態で塗
布しこれを加熱すれば該粉体が融合し塗膜となる
ように加工された樹脂があり、この様な樹脂も使
用可能である。
被覆する薄膜の厚みは、粉末成形体の形状、粉
末の粒径、静水圧加圧の圧力、薄膜の種類などに
よつて適宜選定すればよく、気密性を保つに必要
な最小限の厚み以上であればよい。
本発明者らの実験的知見では、薄膜の厚みは通
常10μm以上であることが望ましい。また、薄膜
の厚みの上限は特に規定されるものではないが、
取扱いの便宜上、5mm程度までが好ましい。勿論
薄膜の種類によつては、これ以下、もしくはこれ
以上の厚みのものでも実施できる。
また、樹脂薄膜は、ある程度弾力性のあるもの
がより好ましい。このような樹脂薄膜で形成体表
面を被覆し、後記するように該被覆薄膜を静水圧
加圧した状態で加熱脱脂することにより、該樹脂
薄膜は該静水圧で成形体表面に常に密着し、また
該静水圧は該薄膜を通して効果的に成形体に伝え
られ、添加剤が飛散して生じる成形体中の空〓を
静水圧加圧による成形体の等方的な収縮により、
極めて効果的に消すことが出来るのである。な
お、このためには、薄膜を形成する樹脂は、ある
程度弾性があることが好ましい。これは、脱脂操
作時の温度において、樹脂のガラス転移点が該操
作温度以下のものであること等を一応の目安とす
ることもできる。
本発明においては、粉末成形体の表面は少なく
ともその一部を被覆せずにその部分を露出させて
おくことが必要である。脱脂時には、該露出面よ
り添加剤が飛散する。露出面の位置は、粉末成形
体の形状や、これをセラミツクス焼結体としたと
きの部分的な機械的負荷を考慮して選定されるべ
きである。例えば粉末成形体の形状が軸対称であ
れば、軸方向の端部とするのが加圧操作が容易で
あるので好ましい。また、露出面は粉末成形体の
形状が例えば、第1図の如く円柱状であれば一方
の端部断面、第2図の如くプロペラ状であれば回
転軸の一方の端部断面が好ましい。その理由は露
出面の近傍は粉末が均等に加圧されにくいため、
この部分はセラミツクス焼結体としたときに機械
的負荷が大きくないからである。上記第1図及び
第2図に示したような露出面1は上記した条件に
合致する。
露出面の面積は、この面より添加剤が飛散する
と云う要請があるため、その面積が小さすぎると
脱脂に要する時間が長くなり、逆に露出面積が大
きくなりすぎると粉末成形体に均等に圧縮されに
くい部分が増してくる。これらの傾向と粉末成形
体の大きさ及び形状を併せて考慮して、妥当な露
出面積が選定される。本発明者らの実験的知見に
よると、露出面積は目安として全表面積の0.5〜
20%、好ましくは1〜10%程度の範囲で実施され
る。
このようにして少なくとも一部の残し残部を樹
脂薄膜で被覆された粉末成形体は、次に該被覆面
を静水圧加圧した状態で加熱する。
静水圧加圧の方法は、被覆面を液体に浸漬した
状態で、この液体をポンプなどで加圧する方法で
よく、加圧用液体としては濃度30重量%程度のホ
ウ酸水や油力作動油などが好適である。ここで液
体に加えられる圧力は、添加剤が加熱されて生ず
る膨張力が粉末成形体に亀裂などの欠陥を発生さ
せることのない圧力とすべきであり、添加剤の種
類、加熱温度、粉末成形体の形状などによつて適
宜選定されるが、この目的の達成のため圧力は5
Kg/cm2以上であることが好ましい。
更に、静水圧加圧の圧力は、添加剤が飛散して
生じる空〓を静水圧加圧による粉末成形体の等方
的な収縮によつて消すことが出来るような圧力と
するのが望ましく、このためには500Kg/cm2以上
10T/cm2以下の圧力とすることが好ましい。
被覆面のみを加圧する方法としては、例えば、
第3図に示したような方法がある。即ち第3図の
粉末成形体3と中空の耐圧管5とを接続しておい
て、粉末成形体の表面と耐圧管の外面とを一体の
薄膜で被覆する。このようにすれば中空の耐圧管
の内部に接する粉末成形体の表面は薄膜で被覆し
ていない露出面となり、この状態で被覆面を加圧
すればよい。
なお、本発明では露出面の近傍の部分に歪みを
生じさせないためには、露出面は何らかの方法で
圧接するのが好ましく、例えば第4図に示した如
く、通気性のある多孔質体を露出面に接触させて
中空の耐圧管内に位置させる方法が有効である。
多孔質体の孔径は少なくとも5mm以下、好ましく
は1mm以下であることが好ましく、より好ましく
は0.1mm以下0.01μm以上である。
このようにして、形成体の被覆した面を静水圧
加圧した状態で、外部から成形体を加熱して添加
剤を蒸発、分解もしくは昇華等により気化させ、
かくして気化した添加剤は、成形体の該薄膜で被
覆されていない露出面を通して、成形体外へ飛散
せしめられ除去される。添加剤を飛散させるため
の粉末成形体の加熱は、加圧されたホウ酸水や油
力作動油等の液を加熱すればよく、昇温速度、到
達温度、保持時間は添加剤の種類によつて適宜選
択される。
なお、本発明においては、添加剤の種類を選択
するについても次のような工業的利点を発現でき
る。即ち本発明は粉末成形体を静水圧加圧しなが
ら添加剤を飛散させる方法であるので、この飛散
によつて成形体の内部の空〓が生じたとしても、
該空〓は静水圧加圧による成形体の等方的な収縮
によつて容易に消されうるのである。従つて本発
明で射出成形体を採用する場合、添加剤は従来用
いられてきたポリスチレン、ポリエチレン等の高
価なものを必ずしも使用する必要はなく、例え
ば、水にポリビニルアルコール、カルボキシメチ
ルセルロース、ポリエチレングリコールなどの水
溶性高分子を0.1〜5%程度溶解させた粘稠な液
や、アルコールにラウリン酸、パルミチン酸、ス
テアリン酸、グリセリンなどの油脂類を1〜20%
程度溶解させた液など安価な液でも充分使用可能
である。
なお、本発明において、泥漿鋳込み成形法を採
用する場合、添加剤は従来と同様、水または水と
アルコールの混合物に少量のHCl、AlCl3、
NaOH、水ガラスなどの解膠剤を添加したもの
が使用される。
本発明においては添加剤として上記の如き従来
のポリスチレンやポリエチレンより沸点の低い物
質も使用可能であるので、脱脂時の加熱温度をは
るかに低い温度で実施することも可能である。
本発明においては脱脂時における粉末成形体の
加熱様式は、もちろん任意であるが、本発明者等
の実験的知見により次の様式が好ましいものの一
つとして挙げられる。即ち、常温から添加剤中の
揮発成分の沸点より15℃程度低い温度迄は任意の
速度で昇温して良いが、この温度に到達したらこ
の温度〜揮発成分の沸点より2℃程度低い温度の
範囲に3〜10時間保持し、この間に揮発成分の40
〜60%程度を飛散・除去させる。次に揮発成分の
沸点以上に加熱して残余の揮発成分を飛散・除去
させ脱脂を完了させるのである。
なお、上記のごとくして、加熱する際、該露出
面を通してフアン、ブロワー等の排風装置で吸引
することも、揮発成分を速やかに成形体外へ飛散
させる上で好ましい実施の態様である。
本発明はこの様な脱脂方法であるので、例えば
粉末成形体の容積が1程度であれば、延べ加熱
時間は24時間以内という従来に比してはるかに短
時間で脱脂を完了することが出来る。
〔発明の効果〕
本発明は、粉末成形体の表面を一部露出し、残
余は気密性がある樹脂薄膜で被覆した後、たとえ
ば500Kg/cm2以上の圧力で静水圧加圧しながら添
加剤を該露出面を通じて飛散させる方法であるの
で、本発明に従えば、添加剤が加熱気化されて生
じる膨張力を該静水圧により効果的に抑制するこ
とができるのである。このため極めて短時間に脱
脂を行うことができ、しかも同時に脱脂に併う割
れや亀裂などの欠陥の発生を、従来よりも著しく
抑えることができるのである。
また、添加剤を除去した部分に生じる粉末成形
体の内部の空〓は、成形体の等方的圧縮によつて
容易に消されうるため、添加量が少量でも粉末と
混練したときに可塑性を示しやすく、かつ加熱・
飛散させ易い添加剤として開発されてきた高価な
ポリスチレンなどを使う必要は必ずしもなくなる
という利点もある。
更にまた、粉末成形体に被覆された樹脂薄膜
は、粉末成形体を補強する役割も有するため、特
に脱脂後の粉末成形体が焼結工程へ移行する過程
で生じる割れや亀裂などを防ぐ効果もある。
また、本発明では添加剤としてポリスチレンや
ポリエチレンなどより沸点の低い物質を使用しう
るので、ポリスチレンやポリエチレンを使用した
場合の様に必ずしも600℃程度の高温で脱脂する
必要はなく、添加剤の種類によつてはこれよりは
るかに低い、例えば後記実施例に示すごとく250
℃以下の温度で実施することさえも出来るので、
消費する熱エネルギーの面でもきわめて有利であ
る。なお、実施温度は好ましくは300〜50℃程度
の範囲である。
本発明はこのような有利な効果を有するので、
射出成形法や泥漿鋳込み成形法などの方法を必要
とする比較的複雑な形状のセラミツクス焼結体で
あつて、更に機械的強度に信頼性を必要とするも
のを製造する場合に、特に効果的に適用すること
が出来るのである。
〔実施例及び比較例〕
以下実施例及び比較例により本発明を具体的に
説明する。
実施例 1
原料粉末として、比表面積が15m2/gで電子顕
微鏡像による平均粒子径が0.3μmの窒化ケイ素粉
末100重量部と、比表面積が12m2/gで電子顕微
鏡像による平均粒子径が0.35μmの酸化マグネシ
ウム5重量部を用い、これに添加剤としてエタノ
ール25重量部及びラウリン酸5重量部とを加えて
混練して得た混合物を射出圧力500Kg/cm2で射出
成形し、直径15mm、長さ50mmの円柱状の窒化ケイ
素質の粉末成形体を得た。得られた粉末成形体の
見掛け容積に対する原料粉末が占める容積(以後
「粉末充填率」という)は57%であつた。
第4図に示したごとく、この粉末成形体3の一
方の端部にアルミナ製多孔質体8(直径15mm、長
さ10mm、平均孔径10μm)を重ね合わせ、耐圧容
器に固着した中空の耐圧管5に接合した状態で、
これらの表面を厚さ120μmの樹脂薄膜2で被覆
した。露出面積は全表面積の6%であつた。被覆
の方法としては液状のスチレン−ブタジエンラテ
ツクス(スチレン60%、ブタジエン40%の共重合
体)を粉末成形体に浸漬−引き上げ法により塗布
し、該ラテツクス中の水を乾燥させ樹脂薄膜を表
面に形成させることによつて行つた。
次に、耐圧容器を濃度30重量%のホウ酸水で満
たし、このホウ酸水をポンプ圧縮によつて1500
Kg/cm2に加圧した状態でヒーターで加熱すること
により、粉末成形体を昇温させ脱脂を行つた。な
お、ホウ酸水の加熱様式は次のよう行つた。
すなわち、室温より75℃まで30℃/hの速度で
昇温、75℃で3時間保持、75℃から174℃まで30
℃/hの速度で昇温、174℃で2時間保持、174℃
から210℃まで30℃/hの速度で昇温、210℃で1
時間保持、以降自然放冷により室温まで冷却。昇
温開始より室温に冷却するまでの通算時間は19時
間であつた。この間ホウ酸水は1500Kg/cm2の加圧
状態に保持しておいた。
なお、粉末成形体に含まれていたエタノール及
びラウリン酸は、樹脂薄膜で被覆されていない露
出面の部分よりアルミナ質多孔体8及び中空の耐
圧管5を通つて耐圧容器の外部に飛散したが、こ
の外部の圧力は大気圧とした。
耐圧容器より取り出した粉末成形体3には、亀
裂の発生や樹脂薄膜の破損といつた外観上の変化
は全く認められず、エタノール及びラウリン酸は
99%以上が飛散していた。また粉末充填率は62%
と脱脂前よりも増加していた。
次に、この粉末成形体を圧力5Kg/cm2Gの窒素
ガス雰囲気下で1800℃に2時間加熱してセラミツ
クス焼結体を得た。得られた焼結体の密度は3.14
g/cm3であつたが、これは窒化ケイ素の理論密度
の99%に相当する。
この焼結体より20片の試験片を切り出し、
JISR−1601の規定に準じて曲げ強度を測定した
結果、平均強度は82Kg/mm2で標準偏差は3.1Kg/
mm2であつた。
比較例 1
実施例1と全く同様にして射出成形法で得た円
柱状の窒化ケイ素質の粉末成形体を、樹脂薄膜で
被覆せずにそのまま常圧の空気中で実施例1と全
く同じ加熱様式にして加熱し脱脂を行つた。
脱脂後の粉末成形体には2〜4mmの間〓で多数
の亀裂が発生しており、また表面の約40%に厚さ
1〜2mmの剥離が生じていた。
比較例 2
実施例1で用いたと同じ窒化ケイ素粉末100重
量部と酸化マグネシウム5重量部からなる原料粉
末に、ポリプロピレン19重量部、ポリエチレン10
重量部、ステアリン酸1重量部を加え、これらを
混練して得た混合物を実施例1と全く同様にして
射出成形し、粉末充填率が59%の粉末成形体を得
た。
次に、この粉末成形体を従来より行われている
次のような高温、長時間の加熱様式で脱脂した。
すなわち室温より100℃まで30℃/hで昇温、100
℃より600℃まで2℃/hで昇温、600℃で2時間
保持、以降自然放冷により室温まで冷却。雰囲気
は600℃で2時間保持した段階では、添加剤を酸
化分解させるために空気雰囲気とし、この段階以
外は窒素ガス雰囲気とし圧力は大気圧とした。昇
温開始より室温に冷却するまでの通算時間は260
時間と云う長時間を要した。
容器より取り出した粉末成形体には、亀裂の発
生、表面剥離といつた外観上の変化は観察され
ず、ポリプロピレン等の添加剤は99.5%以上が飛
散しており、粉末充填率は脱脂前と同じ59%であ
つた。
次にこの粉末成形体を実施例1と全く同様にし
て1800℃で2時間加熱して焼結させた。焼結体の
密度は3.10g/cm3であつた。
得られた焼結体より実施例1と全く同様にして
試験片を切り出し、曲げ強度を測定した結果、平
均強度は68Kg/mm2で標準偏差は6.6Kg/mm2であつ
た。
実施例1と比較例1との比較により、粉末成形
体に薄膜を被覆して被覆面を静水圧加圧した状態
で脱脂することが、亀裂や表面剥離の防止に顕著
な効果があることが分かる。
また実施例1と従来技術の脱脂法である比較例
2との比較より、本発明で脱脂した粉末成形体は
はるかに低温、短時間で脱脂したにもかかわら
ず、この粉末充填率は従来技術のそれよりも高い
こと、及び本発明では焼結体の曲げ強度が大きく
なり、かつそのバラツキもはるかに小さくなるこ
とが分かる。
実施例 2〜4
原料粉末としては実施例1と同じ窒化ケイ素粉
末と酸化マグネシウム粉末を用い、これら100重
量部と5重量部に添加剤としては表−1に示した
ものを表−1に示した重量部加えて混練して得た
混合物を、実施例1と全く同様にして射出成形
し、表−1に示した粉末充填率の窒化ケイ素質の
粉末成形体を得た。
次に、これらの粉末成形体を実施例1と同様に
して、第4図に示した如くアルミナ製多孔質体を
介して中空の耐圧管に接合した状態で、これらの
表面を樹脂薄膜で被覆した。被覆の方法としては
実施例2においては同様にしてアクリル系エマル
ジヨンを塗布し水を乾燥することで行い、実施例
3及び4においては酢酸エチルを溶剤とするクロ
ルプレン樹脂を塗布し溶剤を乾燥することで行つ
た。樹脂薄膜の厚さは実施例2では120μm、実
施例3及び4では230μmであつた。
次にこれら粉末成形体の被覆面を実施例1と同
様にして濃度30重量%のホウ酸水で1500Kg/cm2の
圧力に静水圧加圧した状態のもとで、ホウ酸水を
ヒーターで加熱し昇温させ脱脂を行つた。
ここで加熱様式は、実施例2は実施例1と全く
同様にして、実施例3及び4は次のようにした。
すなわち、室温より98℃まで30℃/hで昇温、98
℃で5時間保持、98℃から110℃まで10℃/hで
昇温、110℃で2時間保持、以降自然放冷により
室温まで冷却。昇温開始より室温に冷却するまで
の通算時間は15時間であつた。
耐圧容器より取り出した粉末成形体には、亀裂
の発生、薄膜の破損といつた外観上の変化はみら
れず、添加剤はいずれも99%以上が飛散してい
た。また粉末充填率は表−1に示したようにいず
れも脱脂前よりも増加していた。
次にこれらの粉末成形体を実施例1と全く同様
にして、1800℃で2時間加熱して表−1に示した
密度の焼結体を得た。
[Technical Field] The present invention relates to a method for removing additives from a powder compact, and more specifically, in order to obtain a ceramic sintered body, the present invention relates to a method for removing additives from a powder compact formed by injection molding or slurry casting. This invention relates to a method of heating and scattering an additive used as an auxiliary agent, a so-called method of degreasing a powder compact. [Background technology] Ceramic sintered bodies, which have complex shapes and are mass-produced, are produced by molding raw material powders of alumina, zirconia, silicon carbide, silicon nitride, etc. into the desired shape by injection molding or slurry casting. It is produced industrially by compacting, degreasing, and then igniting the powder compact to a temperature necessary for sintering. The injection molding method here refers to polystyrene, which exhibits plasticity as a whole and becomes easy to mold when mixed with the above-mentioned powder such as alumina.
20 to 35 parts by weight of additives such as polyethylene, diethylene phthalate, paraffin, fatty acid ester, polyvinyl alcohol, etc. are added to 100 parts by weight of powder and kneaded, and the kneaded product is press-fitted into a mold of the desired shape and molded. This is the way to do it. The obtained powder compact is taken out from the mold, the additives are scattered and removed by heating, and then ignited to form a ceramic sintered body in a desired shape. In addition, the slurry casting method involves adding 20 to 40 parts by weight of an additive made of water or a mixture of water and alcohol to 100 parts by weight of powder such as alumina.
A small amount of deflocculant such as HCl, AlCl 3 , NaOH, or water glass is added and mixed well to form a stable slurry that is fluid and does not easily allow powder to settle.This slurry is made of a porous material similar to gypsum. This is a method in which the slurry is poured into a mold, at least the additives contained in the slurry are absorbed into the mold until the slurry loses its fluidity, and then taken out from the mold as a powder compact. The powder compact obtained by this method usually contains 10 to 15% by weight of additives such as water, so the remaining additives are dispersed by heating, as in the injection molding method, and then For example, a ceramic sintered body can be obtained by igniting at about 1300 to 2300°C. Hereinafter, in the present invention, thermoplasticizers, plasticizers, dispersants, solvents, etc. added to powder in injection molding and slurry casting will be collectively referred to as additives. The operation of scattering the additives remaining in the molded body obtained by the above injection molding method and slurry casting method by heating is hereinafter referred to as "degreasing" using the common terminology of those skilled in the art. do. However, ceramic sintered bodies obtained by the method described above, that is, by degreasing and igniting a powder compact obtained by injection molding or slurry casting, do not exhibit cracks or surface peeling. There is a problem in that a considerable number of defective products (that cannot be considered as products) occur. Furthermore, if these defects occur inside the sintered body, it is difficult to detect the defects at the stage of product production, so some of the products end up being produced as is, causing damage during use and causing accidents. There is also a big problem. However, what I would particularly like to point out here is that most of the defects such as the above-mentioned cracks and surface peeling occur during the degreasing process. In other words, if any additives remain in the powder compact, when the powder compact is ignited to form a ceramic sintered body, the residual additive will rapidly vaporize, and this expansion force will cause the ceramic sintering to fail. Cracks and fissures appear in the structure. In order to prevent this, the powder compact is subjected to a degreasing step prior to ignition to remove additives. Therefore, although it is self-evident,
In the degreasing process, it is desirable to remove additives as completely as possible. However, as mentioned above, powder compacts
Even in the case of slurry casting, the amount of additives is 10% by weight or more, and in the case of injection molded products, it is even higher, ie, 20% by weight or more. In this way, it is possible to remove the additives by scattering them from a powder compact containing a large amount of additives by heating without causing cracks or cracks. This is essentially an extremely difficult problem because it acts strongly on powder compacts with extremely low viscosity. Therefore, conventionally, this process involves forming powder compacts under atmospheric pressure or a pressure of about 5 kg/cm 2 or less.
This is done by heating the powder to around 600°C and scattering and removing the additive through vaporization, decomposition, combustion, etc. However, due to the need to keep the expansion force of the additive low, the rise of the powder compact is difficult. The heating rate is extremely slow, such as 1 to 3°C/h. Since the degreasing process has no choice but to adopt such a slow temperature increase rate, it usually takes a long time of 5 to 7 days, which poses a problem that productivity is significantly inhibited. In addition, in the injection molding method, when the amount of additives is increased, the voids formed when the additives are removed in the degreasing process increase, so it is necessary to use as few additives as possible and to improve moldability. At the same time, properties that make it easy to heat and scatter are also required. However, it is difficult to satisfy all of these properties by using the polystyrene mentioned above,
Even if expensive materials such as polyethylene were used, the problem was that it was inherently extremely difficult. Furthermore, since the mechanical strength of a degreased powder compact is almost zero, it can easily crack or crack due to slight vibrations or shakes during the process of transferring or transporting the compact to the next sintering process. This is likely to occur, and in order to prevent this, it was necessary to prevent vibrations, shaking, etc. at this time as much as possible. In this way, despite being produced with extremely low productivity and with extremely careful operations,
The resulting ceramic sintered bodies had quite a few defective products, and the actual situation was that these were mainly caused by defects in the powder compacts that occurred during this degreasing process. [Summary of the Invention] The purpose of the present invention is to solve the drawbacks of the conventional techniques using a completely new method. According to the method of the present invention, the degreasing process can be carried out in an extremely short time. In addition, a novel degreasing method is provided which can significantly suppress the occurrence of defects in powder compacts as described above. [Disclosure of the Invention] The present inventors have conducted intensive studies with the aim of fundamentally eliminating the drawbacks of the conventional technology, and have found that even if additives are removed at extremely low temperatures and in a short period of time, cracks in powder compacts do not occur. We have discovered a method that can significantly suppress the occurrence of defects such as cracks and cracks compared to conventional methods.
This has led to the completion of the present invention. That is, the above-mentioned object of the present invention is to provide a method for removing additives from a powder compact formed by adding additives to powder by heating and scattering the additives, and in which at least a portion of the surface of the powder compact is removed in advance. Except for leaving the exposed surface, the remaining surface is covered with an airtight resin thin film, and the powder compact is heated while the coated surface is subjected to hydrostatic pressure to scatter the additive through the exposed surface. It is achieved by doing so. [Specific Requirements for Carrying Out the Invention] The present invention will be described in detail below. In the present invention, when degreasing a powder compact that still contains additives, for example, a powder compact that still contains additives obtained by injection molding, slurry molding, etc., Except for a portion of the body surface left exposed, the rest is covered with an airtight resin thin film. For coating with such a thin resin film, for example, a liquid resin that solidifies by volatilization of a solvent or a chemical reaction is applied directly to the surface of the molded object, by spraying, or by dipping and pulling up, and if necessary, it is dried or heated. This can be carried out by forming a resin coating on the surface by applying treatments such as the following. Examples of liquid resins that can be used in this method include industrially produced resins such as vinyl acetate emulsion, styrene-butadiene latex, acrylic emulsion, and natural rubber latex.
Further, polyurethane resins, silicone resins, epoxy resins, acrylic resins, polyester resins, chlorprene resins, phenolic resins, etc. can also be used. Furthermore, acrylic resin, epoxy resin,
Among polyester resins, there are resins that are processed so that when applied in the form of powder and heated, the powder fuses to form a coating film, and such resins can also be used. The thickness of the thin film to be coated may be selected appropriately depending on the shape of the powder compact, the particle size of the powder, the pressure of hydrostatic pressing, the type of thin film, etc., and should be at least the minimum thickness necessary to maintain airtightness. That's fine. According to the experimental findings of the present inventors, the thickness of the thin film is usually preferably 10 μm or more. In addition, although the upper limit of the thickness of the thin film is not particularly defined,
For convenience of handling, it is preferably up to about 5 mm. Of course, depending on the type of thin film, the thickness may be less than or greater than this. Further, it is more preferable that the resin thin film has some degree of elasticity. By coating the surface of the molded body with such a resin thin film and heating and degreasing the coating thin film under hydrostatic pressure as described later, the resin thin film always adheres to the surface of the molded body due to the hydrostatic pressure, In addition, the hydrostatic pressure is effectively transmitted to the molded body through the thin film, and the air in the molded body created by the scattering of additives is removed by isotropic contraction of the molded body due to hydrostatic pressure.
It can be erased very effectively. Note that for this purpose, it is preferable that the resin forming the thin film has some degree of elasticity. This can be based on the fact that the glass transition point of the resin is below the operating temperature at the temperature during the degreasing operation. In the present invention, it is necessary that at least a part of the surface of the powder compact be left uncovered and exposed. During degreasing, additives are scattered from the exposed surface. The position of the exposed surface should be selected in consideration of the shape of the powder compact and the local mechanical load when it is made into a ceramic sintered body. For example, if the shape of the powder compact is axially symmetrical, it is preferable to use the ends in the axial direction because the pressing operation is easy. Further, the exposed surface is preferably a cross section of one end if the powder compact has a cylindrical shape as shown in FIG. 1, or a cross section of one end of the rotating shaft if the shape is a propeller as shown in FIG. The reason is that it is difficult for the powder to be evenly compressed near the exposed surface.
This is because this portion does not receive a large mechanical load when it is made into a ceramic sintered body. The exposed surface 1 as shown in FIGS. 1 and 2 above meets the above conditions. The area of the exposed surface is required to prevent additives from scattering from this surface, so if the area is too small, the time required for degreasing will be longer; on the other hand, if the exposed area is too large, it will not be possible to compress the powder evenly into a compact. There are more and more difficult parts. An appropriate exposed area is selected by considering these trends together with the size and shape of the powder compact. According to the experimental findings of the present inventors, the exposed area is approximately 0.5 to 0.5 of the total surface area.
It is carried out in a range of about 20%, preferably about 1 to 10%. The powder compact whose remaining portion is coated with a resin thin film in this manner is then heated while the coated surface is subjected to hydrostatic pressure. Hydrostatic pressurization can be done by immersing the coated surface in liquid and pressurizing the liquid with a pump, etc. The pressurizing liquid may be boric acid water with a concentration of about 30% by weight, hydraulic oil, etc. is suitable. The pressure applied to the liquid here should be such that the expansion force generated when the additive is heated will not cause defects such as cracks in the powder compact, and the pressure must be such that the type of additive, heating temperature, powder compaction, etc. The pressure is selected appropriately depending on the shape of the body, etc., but in order to achieve this purpose, the pressure should be 5.
It is preferable that it is Kg/cm 2 or more. Furthermore, it is desirable that the pressure of the hydrostatic pressurization is such that the air space created by the scattering of the additive can be eliminated by the isotropic contraction of the powder compact due to the hydrostatic pressurization. For this purpose, 500Kg/cm2 or more
The pressure is preferably 10T/cm 2 or less. As a method of applying pressure only to the coated surface, for example,
There is a method as shown in FIG. That is, the powder compact 3 shown in FIG. 3 and the hollow pressure tube 5 are connected, and the surface of the powder compact and the outer surface of the pressure tube are coated with an integral thin film. In this way, the surface of the powder compact that is in contact with the inside of the hollow pressure tube becomes an exposed surface that is not covered with a thin film, and the coated surface can be pressurized in this state. In the present invention, in order to avoid distortion in the vicinity of the exposed surface, it is preferable to press the exposed surface by some method. For example, as shown in FIG. An effective method is to place it in a hollow pressure tube in contact with a surface.
The pore diameter of the porous body is preferably at least 5 mm or less, preferably 1 mm or less, and more preferably 0.1 mm or less and 0.01 μm or more. In this way, while the coated surface of the formed body is subjected to hydrostatic pressure, the formed body is heated from the outside to vaporize the additive by evaporation, decomposition, sublimation, etc.
The thus vaporized additive is scattered out of the molded body through the exposed surface of the molded body that is not covered with the thin film, and is removed. Heating the powder compact to disperse the additives can be done by heating a liquid such as pressurized boric acid water or hydraulic oil, and the heating rate, temperature reached, and holding time depend on the type of additive. Therefore, it is selected appropriately. In addition, in the present invention, the following industrial advantages can be realized by selecting the type of additive. That is, since the present invention is a method of scattering additives while applying hydrostatic pressure to a powder compact, even if this scattering causes voids inside the compact,
The voids can be easily eliminated by isotropic shrinkage of the molded product by isostatic pressure. Therefore, when an injection molded article is used in the present invention, it is not necessarily necessary to use expensive additives such as conventionally used polystyrene and polyethylene; for example, it is not necessary to use expensive additives such as polystyrene, polyethylene, etc. A viscous liquid containing 0.1 to 5% of water-soluble polymer dissolved in alcohol, or 1 to 20% of oils and fats such as lauric acid, palmitic acid, stearic acid, and glycerin in alcohol.
Inexpensive liquids such as liquids that have been dissolved to some extent can also be used satisfactorily. In addition, in the present invention, when adopting the slurry casting method, the additives are water or a mixture of water and alcohol with a small amount of HCl, AlCl 3 ,
A deflocculant such as NaOH or water glass is added. In the present invention, since it is possible to use as an additive a substance having a boiling point lower than that of the conventional polystyrene or polyethylene as described above, it is also possible to carry out the heating temperature during degreasing at a much lower temperature. In the present invention, the method of heating the powder compact during degreasing is of course arbitrary, but the following method is listed as one of the preferable methods based on the experimental findings of the present inventors. In other words, the temperature may be raised at any rate from room temperature to a temperature approximately 15°C lower than the boiling point of the volatile components in the additive, but once this temperature is reached, the temperature must be increased from this temperature to a temperature approximately 2°C lower than the boiling point of the volatile components. Hold in range for 3-10 hours, during which time 40% of the volatile components
~60% will be scattered and removed. Next, the remaining volatile components are scattered and removed by heating above the boiling point of the volatile components to complete degreasing. In addition, when heating as described above, it is also a preferred embodiment to suction through the exposed surface with an exhaust device such as a fan or blower in order to quickly scatter volatile components out of the molded article. Since the present invention is such a degreasing method, for example, if the volume of the powder compact is about 1, the total heating time is less than 24 hours, which is much shorter than the conventional method. . [Effects of the Invention] The present invention exposes a part of the surface of a powder compact and covers the rest with an airtight resin thin film, and then adds additives while applying hydrostatic pressure at a pressure of, for example, 500 kg/cm 2 or more. Since this is a method of scattering through the exposed surface, according to the present invention, the expansion force generated when the additive is heated and vaporized can be effectively suppressed by the hydrostatic pressure. For this reason, degreasing can be carried out in an extremely short period of time, and at the same time, the occurrence of defects such as cracks and cracks due to degreasing can be significantly suppressed compared to conventional methods. In addition, the voids inside the powder compact that occur in the area where the additive has been removed can be easily eliminated by isotropic compression of the compact, so even if the amount added is small, the plasticity will be reduced when kneaded with the powder. Easy to display and heating/
Another advantage is that there is no need to use expensive polystyrene, which has been developed as an additive that easily scatters. Furthermore, since the resin thin film coated on the powder compact also has the role of reinforcing the powder compact, it is also effective in preventing cracks and cracks that occur during the process of transferring the powder compact after degreasing to the sintering process. be. In addition, in the present invention, since it is possible to use a substance with a lower boiling point than polystyrene or polyethylene as an additive, it is not necessarily necessary to degrease at a high temperature of about 600°C as in the case of using polystyrene or polyethylene. In some cases it is much lower than this, for example 250 as shown in the example below.
It can even be carried out at temperatures below ℃,
It is also extremely advantageous in terms of heat energy consumption. In addition, the implementation temperature is preferably in the range of about 300 to 50°C. Since the present invention has such advantageous effects,
It is particularly effective when manufacturing ceramic sintered bodies with relatively complex shapes that require methods such as injection molding or slurry casting, and also require reliability in mechanical strength. It can be applied to [Examples and Comparative Examples] The present invention will be specifically described below with reference to Examples and Comparative Examples. Example 1 As raw material powders, 100 parts by weight of silicon nitride powder with a specific surface area of 15 m 2 /g and an average particle diameter as determined by an electron microscope image of 0.3 μm and a specific surface area of 12 m 2 /g and an average particle diameter determined as an electron microscope image were used. Using 5 parts by weight of 0.35 μm magnesium oxide, 25 parts by weight of ethanol and 5 parts by weight of lauric acid were added as additives, and the resulting mixture was then injection molded at an injection pressure of 500 Kg/cm 2 to form a mold with a diameter of 15 mm. A cylindrical silicon nitride powder compact with a length of 50 mm was obtained. The volume occupied by the raw material powder with respect to the apparent volume of the obtained powder compact (hereinafter referred to as "powder filling ratio") was 57%. As shown in Fig. 4, an alumina porous body 8 (diameter 15 mm, length 10 mm, average pore diameter 10 μm) is superimposed on one end of this powder compact 3, and a hollow pressure-resistant tube is fixed to a pressure-resistant container. When connected to 5,
These surfaces were coated with a resin thin film 2 having a thickness of 120 μm. The exposed area was 6% of the total surface area. The coating method is to apply liquid styrene-butadiene latex (a copolymer of 60% styrene and 40% butadiene) to the powder compact by dipping and pulling up, and then drying the water in the latex to form a thin resin film on the surface. This was done by forming a Next, the pressure container is filled with boric acid water with a concentration of 30% by weight, and this boric acid water is compressed with a pump to 1500%
The powder compact was degreased by heating it with a heater under pressure of Kg/cm 2 to raise the temperature. The heating method for the boric acid water was as follows. That is, increase the temperature from room temperature to 75℃ at a rate of 30℃/h, hold at 75℃ for 3 hours, and increase the temperature from 75℃ to 174℃ at a rate of 30℃/h.
Increase temperature at a rate of ℃/h, hold at 174℃ for 2 hours, 174℃
Temperature rises at a rate of 30°C/h from to 210°C, 1 at 210°C
Hold for a while and then cool to room temperature by natural cooling. The total time from the start of temperature rise until cooling to room temperature was 19 hours. During this time, the boric acid solution was maintained at a pressure of 1500 kg/cm 2 . Note that the ethanol and lauric acid contained in the powder compact were scattered to the outside of the pressure container through the alumina porous body 8 and the hollow pressure tube 5 from the exposed surface not covered with the resin thin film. , this external pressure was atmospheric pressure. The powder compact 3 taken out from the pressure container showed no changes in appearance such as cracks or damage to the resin thin film, and ethanol and lauric acid were not present.
More than 99% of the particles were scattered. Also, the powder filling rate is 62%
and increased compared to before degreasing. Next, this powder compact was heated at 1800°C for 2 hours in a nitrogen gas atmosphere at a pressure of 5 kg/cm 2 G to obtain a ceramic sintered body. The density of the obtained sintered body is 3.14
g/cm 3 , which corresponds to 99% of the theoretical density of silicon nitride. Cut out 20 test pieces from this sintered body,
As a result of measuring the bending strength according to the regulations of JISR-1601, the average strength was 82Kg/mm 2 and the standard deviation was 3.1Kg/mm2.
It was warm in mm2 . Comparative Example 1 A cylindrical silicon nitride powder molded body obtained by injection molding in exactly the same manner as in Example 1 was heated in the same manner as in Example 1 in air at normal pressure without being coated with a resin thin film. It was then heated and degreased. After degreasing, the powder compact had many cracks in the range of 2 to 4 mm, and peeling with a thickness of 1 to 2 mm had occurred on about 40% of the surface. Comparative Example 2 Raw material powder consisting of 100 parts by weight of the same silicon nitride powder and 5 parts by weight of magnesium oxide used in Example 1 was added with 19 parts by weight of polypropylene and 10 parts by weight of polyethylene.
parts by weight, and 1 part by weight of stearic acid were added, and the mixture obtained by kneading these was injection molded in exactly the same manner as in Example 1 to obtain a powder compact with a powder filling rate of 59%. Next, this powder compact was degreased by the following conventional heating method at high temperature and for a long time.
In other words, the temperature is raised from room temperature to 100℃ at a rate of 30℃/h, 100℃
The temperature was raised from ℃ to 600℃ at a rate of 2℃/h, held at 600℃ for 2 hours, and then cooled to room temperature by natural cooling. At the stage where the temperature was maintained at 600°C for 2 hours, the atmosphere was set to air in order to oxidize and decompose the additives, and at other stages, the atmosphere was set to nitrogen gas and the pressure was set to atmospheric pressure. The total time from the start of temperature rise until cooling to room temperature is 260 minutes.
It took a long time. No changes in appearance such as cracking or surface peeling were observed in the powder compact taken out from the container, more than 99.5% of additives such as polypropylene were scattered, and the powder filling rate was the same as before degreasing. It was the same 59%. Next, this powder compact was heated and sintered at 1800° C. for 2 hours in exactly the same manner as in Example 1. The density of the sintered body was 3.10 g/cm 3 . A test piece was cut out from the obtained sintered body in exactly the same manner as in Example 1, and the bending strength was measured. As a result, the average strength was 68 Kg/mm 2 and the standard deviation was 6.6 Kg/mm 2 . A comparison between Example 1 and Comparative Example 1 shows that coating a powder compact with a thin film and degreasing the coated surface while applying hydrostatic pressure has a remarkable effect on preventing cracks and surface peeling. I understand. Furthermore, a comparison between Example 1 and Comparative Example 2, which is a conventional degreasing method, shows that although the powder compacts degreased by the present invention were degreased at a much lower temperature and in a shorter time, this powder filling rate was lower than that of the conventional technique. It can be seen that the bending strength of the sintered body of the present invention is higher than that of , and that the bending strength of the sintered body is increased and the variation thereof is also much smaller. Examples 2 to 4 The same silicon nitride powder and magnesium oxide powder as in Example 1 were used as raw material powders, and the additives shown in Table 1 were added to 100 parts by weight and 5 parts by weight of these powders. The resulting mixture was injection molded in exactly the same manner as in Example 1 to obtain silicon nitride powder compacts having the powder filling percentages shown in Table 1. Next, in the same manner as in Example 1, these powder compacts were joined to a hollow pressure tube via an alumina porous body as shown in Fig. 4, and their surfaces were coated with a resin thin film. did. As for the coating method, in Example 2, acrylic emulsion was applied in the same manner and the water was dried, and in Examples 3 and 4, chlorprene resin using ethyl acetate as a solvent was applied and the solvent was dried. I went there. The thickness of the resin thin film was 120 μm in Example 2, and 230 μm in Examples 3 and 4. Next, the coated surface of these powder compacts was hydrostatically pressurized to a pressure of 1500 kg/cm 2 with boric acid water with a concentration of 30% by weight in the same manner as in Example 1, and the boric acid water was applied with a heater. Degreasing was performed by heating and raising the temperature. Here, the heating mode in Example 2 was exactly the same as in Example 1, and in Examples 3 and 4, it was as follows.
In other words, the temperature is raised from room temperature to 98°C at a rate of 30°C/h, 98
Hold at ℃ for 5 hours, raise temperature from 98℃ to 110℃ at 10℃/h, hold at 110℃ for 2 hours, then cool to room temperature by natural cooling. The total time from the start of temperature rise until cooling to room temperature was 15 hours. There were no visible changes in the powder compacts taken out from the pressure container, such as cracks or thin film damage, and more than 99% of the additives had been scattered. In addition, as shown in Table 1, the powder filling rate increased in all cases compared to before degreasing. Next, these powder compacts were heated in exactly the same manner as in Example 1 at 1800°C for 2 hours to obtain sintered bodies having the densities shown in Table 1.
【表】
** カルボキシメチルセルロース
得られた焼結体より実施例1と全く同様にして
試験片を切り出し、曲げ強度を測定した結果、平
均値及び標準偏差は表−1に示した値であつた。
実施例 5〜7
静水圧加圧する圧力の効果をみる目的で次の実
験を行つた。原料粉末として、比表面積が17m2/
gで電子顕微鏡像による平均粒子が0.25μmの炭
化ケイ素粉末と、比表面積が10m2/gで同じく平
均粒子が0.4μmの単体ホウ素と、比表面積が90
m2/gで同じく平均粒子が0.03μmのカーボンブ
ラツクとを用い、これらのそれぞれ100重量部、
1重量部、2重量部と、添加剤としてイソプロパ
ノールを30重量部とミリスチン酸3重量部と加え
混練して得た混合物を実施例1と全く同様にして
射出成形した粉末充填率が57%の粉末成形体3個
を得た。
これらの炭化ケイ素質の粉末成形体をそれぞれ
実施例1と全く同様にして、アルミナ製多孔質体
8を介して中空の耐圧管5に接合した状態でこれ
らの表面にスチレン−ブタジエンラテツクスを塗
布し、水を乾燥させて厚さ120μmの樹脂薄膜を
被覆した。
次に、これらをそれぞれ表−2に示した圧力で
静水圧加圧の状態を保持しておいて、実施例1と
全く同様な加熱様式で加熱し、脱脂した。脱脂後
の粉末充填率はそれぞれ表−2に示した値であつ
た。次にこれらの粉末成形体を真空中(1mmHg
以下)で2050℃に1時間加熱して、炭化ケイ素質
の焼結体を得た。得られた焼結体の密度はそれぞ
れ表−2に示した値であつた。[Table] ** Carboxymethyl cellulose A test piece was cut out from the obtained sintered body in exactly the same manner as in Example 1, and the bending strength was measured. As a result, the average value and standard deviation were the values shown in Table 1. . Examples 5 to 7 The following experiments were conducted for the purpose of examining the effect of hydrostatic pressurization. As a raw material powder, the specific surface area is 17m 2 /
A silicon carbide powder with an average particle size of 0.25 μm as determined by an electron microscope image in g, a single boron powder with a specific surface area of 10 m 2 /g and an average particle size of 0.4 μm, and a specific surface area of 90 μm.
m 2 /g and carbon black with an average particle size of 0.03 μm, 100 parts by weight of each of these,
A mixture obtained by adding 1 part by weight, 2 parts by weight, 30 parts by weight of isopropanol and 3 parts by weight of myristic acid as additives and kneading was injection molded in exactly the same manner as in Example 1, and the powder filling rate was 57%. Three powder compacts were obtained. Each of these silicon carbide powder compacts was bonded to a hollow pressure tube 5 via an alumina porous body 8 in exactly the same manner as in Example 1, and styrene-butadiene latex was applied to their surfaces. Then, the water was dried and a resin thin film with a thickness of 120 μm was coated. Next, these were heated in the same heating manner as in Example 1 to degrease them while maintaining the state of hydrostatic pressurization at the pressures shown in Table 2. The powder filling rates after degreasing were the values shown in Table 2. Next, these powder compacts were placed in a vacuum (1 mmHg
(below) for 1 hour at 2050°C to obtain a silicon carbide sintered body. The densities of the obtained sintered bodies were as shown in Table 2.
【表】
この焼結体を使用し実施例1と同様にして試験
片を切り出し、曲げ強度を測定した結果、平均値
及び標準偏差は表−2に示した値であつた。[Table] Using this sintered body, test pieces were cut out in the same manner as in Example 1, and the bending strength was measured. As a result, the average value and standard deviation were the values shown in Table-2.
第1図および第2図は、本発明において用いる
粉末成形体の形状の例を示す斜視図である。第3
図および第4図は、本発明において用いる粉末成
形体が加圧容器に設置された状態を示す断面図で
ある。
図面において、1……露出面、2……樹脂薄
膜、3……粉末成形体、4……耐圧容器壁、5…
…中空の耐圧管、6……加圧液、7……大気、8
……アルミナ製多孔質体を示す。
FIGS. 1 and 2 are perspective views showing examples of shapes of powder compacts used in the present invention. Third
4 and 4 are cross-sectional views showing a state in which the powder compact used in the present invention is placed in a pressurized container. In the drawings, 1...exposed surface, 2...resin thin film, 3...powder compact, 4...pressure container wall, 5...
...Hollow pressure tube, 6 ... Pressurized liquid, 7 ... Atmosphere, 8
...Indicates a porous body made of alumina.
Claims (1)
り該添加剤を加熱・飛散させて除去する方法であ
つて、予め該粉末成形体の表面の少なくとも一部
を露出面として残すほかは、残余を気密性のある
樹脂薄膜で被覆し、該被覆した面を静水圧加圧し
た状態で該粉末成形体を加熱し、該添加剤を該露
出面を通して飛散せしめることを特徴とする粉末
成形体中の添加剤の除去方法。 2 粉末がセラミツクス粉末である特許請求の範
囲第1項記載の方法。 3 粉末成形体が射出成形法により成形されたも
のである特許請求の範囲第1項記載の方法。 4 粉末成形体が泥漿鋳込み成形法により成形さ
れたものである特許請求の範囲第1項記載の方
法。 5 添加剤が除去された粉末成形体を引き続き強
熱して成形セラミツクス焼結体とする特許請求の
範囲第1項ないし第4項の何れかに記載の方法。[Scope of Claims] 1. A method for removing additives from a powder compact formed by adding additives to powder by heating and scattering the additives, the method comprising: removing at least a part of the surface of the powder compact from an exposed surface in advance; In addition to leaving it as a powder, the remaining part is covered with an airtight resin thin film, and the powder compact is heated while the coated surface is subjected to hydrostatic pressure, and the additive is dispersed through the exposed surface. A method for removing additives from a powder compact. 2. The method according to claim 1, wherein the powder is a ceramic powder. 3. The method according to claim 1, wherein the powder compact is molded by an injection molding method. 4. The method according to claim 1, wherein the powder compact is formed by a slurry casting method. 5. The method according to any one of claims 1 to 4, wherein the powder compact from which additives have been removed is subsequently ignited to produce a shaped ceramic sintered body.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61-152807 | 1986-07-01 | ||
| JP15280786 | 1986-07-01 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63147869A JPS63147869A (en) | 1988-06-20 |
| JPH0415191B2 true JPH0415191B2 (en) | 1992-03-17 |
Family
ID=15548584
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62162240A Granted JPS63147869A (en) | 1986-07-01 | 1987-07-01 | Method of removing additive from powder formed body |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63147869A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2777674B2 (en) * | 1990-09-28 | 1998-07-23 | 日本特殊陶業株式会社 | Manufacturing method of ceramic sintered body |
-
1987
- 1987-07-01 JP JP62162240A patent/JPS63147869A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63147869A (en) | 1988-06-20 |
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