JP4390872B2 - Semiconductor manufacturing apparatus member and method for manufacturing semiconductor manufacturing apparatus member - Google Patents
Semiconductor manufacturing apparatus member and method for manufacturing semiconductor manufacturing apparatus member Download PDFInfo
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- JP4390872B2 JP4390872B2 JP15966898A JP15966898A JP4390872B2 JP 4390872 B2 JP4390872 B2 JP 4390872B2 JP 15966898 A JP15966898 A JP 15966898A JP 15966898 A JP15966898 A JP 15966898A JP 4390872 B2 JP4390872 B2 JP 4390872B2
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- 238000000034 method Methods 0.000 title claims description 41
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 claims description 91
- 238000005245 sintering Methods 0.000 claims description 54
- 229910010271 silicon carbide Inorganic materials 0.000 claims description 50
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- 238000010438 heat treatment Methods 0.000 claims description 44
- 229910052799 carbon Inorganic materials 0.000 claims description 38
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Description
【0001】
【発明の属する技術分野】
本発明は、半導体製造装置用部材及びその製造方法に関し、詳しくは、優れた特性を有する炭化ケイ素焼結体を用いた、耐久性に優れ、高い特性を有する半導体製造装置用部材及びその製造方法に関するものである。
【0002】
【従来の技術】
半導体を製造するために用いる均熱管(ライナーチューブ)、反応ガスを流す反応管(プロセスチューブ)、半導体ウエハを乗せる治具(ウエーハボート)等の半導体製造装置用部材は、緻密性、耐熱性、剛性等の高い特性を要求されることから、炭化ケイ素の使用が増加する傾向にある。従来、炭化ケイ素により半導体製造装置用部材を作製する場合、原料粉末に結合剤を添加して成形した後、焼成、焼結後、金属シリコンを溶融含浸するの工程に付する方法が汎用されている。
【0003】
従来の炭化ケイ素を用いた半導体製造装置用部材は、高温処理時に炭化ケイ素内部の金属不純物が部材中に拡散移動するため、製造される半導体ウェハを汚染するという問題があった。この炭化ケイ素の不純物に起因するウェハの汚染を防止する方法として、部材を高純度の原料で作製する方法、部材表面にCVD(化学的気相析出)処理による高純度の炭化ケイ素被膜を形成する方法等が行われて
いる。
【0004】
しかしながら、含有不純金属が数ppm以下のオーダーの高純度の炭化ケイ素を用いても金属シリコン含浸前の多孔体焼結体の純化は必要であり、また、金属シリコン含浸後の焼結体は酸洗いや酸処理工程で金属シリコンの溶出の問題があった。そこで、更なる高純度化や耐久性向上のため、部材表面を炭化ケイ素膜で被覆するCVD処理を行っているが、このCVD処理は設備に多額の費用が必要で、生産コストが高くなり、また、このCVD被膜は急熱、急冷のサイクルを繰り返すうちに、基材から剥離したり、ピンホールや亀裂が生じたりして汚染防止効果の耐久性に欠ける問題点があった。
【0005】
また、このCVD処理を施すための基材は、鋳込み成形などの手段により反応焼結法によって予め治具の形状に成形されるが、近年のウエハサイズの大型化や反応管の形状の変化に伴って、基材の形状も多様なものが求められ、各部材ごとに鋳型が必要となり、これも製造コストを引き上げる要因となっていた。
【0006】
【発明が解決しようとする課題】
本発明は上記の各問題点を考慮してなされたものであり、その目的は、高密度且つ高純度の良質な炭化ケイ素焼結体を用いて、ウエハ等の金属不純物による汚染を防止することができ、生産性が良好で製造コストが低く、且つ、耐久性、耐溶剤性に優れた半導体製造装置用部材及びその製造方法を提供することにある。
【0007】
【課題を解決するための手段】
本発明者らは、上述の如き焼結法開発の経緯を鋭意検討した結果、予め炭化ケイ素粉体の表面に炭素を代表とする、加熱により炭素を生成する有機化合物である非金属系焼結助剤を適量適度に配置し、特定条件でのホットプレスを組み合わせることにより得られた高密度かつ、高純度の炭化ケイ素焼結体を用いることにより、優れた特性の半導体製造装置用部材を得られることを見出し、本発明を完成した。
【0008】
即ち、本発明の半導体製造装置用部材は、炭化ケイ素粉末と加熱により炭素を生成する有機化合物である非金属系焼結助剤との混合物を、700℃まで加熱して保持する第1の昇温と、更に1500℃まで加熱して保持する第2の昇温と、を行った後、温度2000〜2400℃、圧力300〜700kgf/cm2、非酸化性雰囲気下でホットプレスを行い焼結して得られた焼結体であって、密度が2.9g/cm3 以上、不純物元素の総含有量が1ppm未満、である炭化ケイ素焼結体を用いることを特徴とする。
また、本発明の半導体製造装置用部材の製造方法は、炭化ケイ素粉末と加熱により炭素を生成する有機化合物である非金属系焼結助剤との混合物を準備する工程と、前記混合物を700℃まで加熱して保持する第1の昇温工程と、更に1500℃まで加熱して保持する第2の昇温工程と、更にその後温度2000〜2400℃、圧力300〜700kgf/cm2、非酸化性雰囲気下でホットプレスする工程と、を有することを特徴とする。
【0009】
ここで用いられる炭化ケイ素焼結体は、比抵抗が1Ω・cm以下であり、熱伝導率が200W/m・k以上であることが好ましい。
【0010】
本発明の半導体製造装置用部材は、高純度で、且つ、高密度の炭化ケイ素焼結体を用いているため、金属ケイ素を含有せず、ケイ素の融点である1500℃を超える加熱によっても強度の低下が見られず、酸処理にも安定である。また、この部材は放電加工を容易になし得るので、組立式とすることもでき、これによって、半導体製造装置用部材の設計の自由度が上がり、大型の部材を作製する場合においても、従来の規模の焼結体製造装置で対応することができる。
【0011】
【発明の実施の形態】
以下に、本発明をさらに詳細に説明する。まず、本発明の半導体製造装置用部材を構成する炭化ケイ素焼結体について説明する。
【0012】
本発明の半導体製造装置用部材の基材として用いられる炭化ケイ素焼結体は、原料として、α型、β型、非晶質或いはこれらの混合物等である炭化ケイ素粉末が使用されており、特に、β型炭化ケイ素粉末が好適に使用される。このβ型炭化ケイ素粉末のグレードには特に制限はなく、例えば、一般に市販されているβ型炭化ケイ素粉末を用いることができる。この炭化ケイ素粉末の粒径は、高密度化の観点からは小さいことが好ましく、0.01〜10μm程度、さらには、0.05〜1μm程度であることが好ましい。粒径が0.01μm未満であると、計量、混合などの処理工程における取扱が困難となり、10μmを超えると比表面積が小さく、即ち、隣接する粉体との接触面積が小さくなり、高密度化が困難となるため、好ましくない。
【0013】
好適な炭化ケイ素原料粉体の態様としては、粒径が0.05〜1μm、比表面積が5m2 /g以上、遊離炭素1%以下、酸素含有量1%以下のものが好適に用いられる。また、用いられる炭化ケイ素粉末の粒度分布は特に制限されず、炭化ケイ素焼結体の製造時において、粉体の充填密度を向上させること及び炭化ケイ素の反応性の観点から、2つ以上の極大値を有するものも使用しうる。
【0014】
なお、高純度の炭化ケイ素焼結体を得るためには、原料の炭化ケイ素粉末として、高純度の炭化ケイ素粉体を用いればよい。
【0015】
高純度の炭化ケイ素粉末は、例えば、少なくとも1種以上の液状のケイ素化合物を含むケイ素源と、加熱により炭素を生成する少なくとも1種以上の液状の有機化合物を含む炭素源と、重合又は架橋触媒と、を均質に混合して得られた固形物を非酸化性雰囲気下で焼成する焼成工程とを含む製造方法により得ることができる。
【0016】
高純度の炭化ケイ素粉末の製造に用いられるケイ素化合物(以下、適宜、ケイ素源と称する)としては、液状のものと固体のものとを併用することができるが、少なくとも一種は液状のものから選ばれなくてはならない。液状のものとしては、アルコキシシラン(モノ−、ジ−、トリ−、テトラ−)及びテトラアルコキシシランの重合体が用いられる。アルコキシシランの中ではテトラアルコキシシランが好適に用いられ、具体的には、メトキシシラン、エトキシシラン、プロポキシシラン、ブトキシシラン等が挙げられるが、ハンドリングの点からはエトキシシランが好ましい。また、テトラアルコキシシランの重合体としては、重合度が2〜15程度の低分子量重合体(オリゴマー)及びさらに重合度が高いケイ酸ポリマーで液状のものが挙げられる。これらと併用可能な固体状のものとしては、酸化ケイ素が挙げられる。本発明において酸化ケイ素とは、SiOの他、シリカゾル(コロイド状超微細シリカ含有液、内部にOH基やアルコキシル基を含む)、二酸化ケイ素(シリカゲル、微細シリカ、石英粉体)等を含む。
【0017】
これらケイ素源のなかでも、均質性やハンドリング性が良好な観点から、テトラエトキシシランのオリゴマー及びテトラエトキシシランのオリゴマーと微粉体シリカとの混合物等が好適である。また、これらのケイ素源は高純度の物質が用いられ、初期の不純物含有量が20ppm以下であることが好ましく、5ppm以下であることがさらに好ましい。
【0018】
また、高純度炭化ケイ素粉末の製造に使用される加熱により炭素を生成する有機化合物としては、液状のものの他、液状のものと固体のものとを併用することができ、残炭率が高く、且つ触媒若しくは加熱により重合又は架橋する有機化合物、具体的には例えば、フェノール樹脂、フラン樹脂、ポリイミド、ポリウレタン、ポリビニルアルコール等の樹脂のモノマーやプレポリマーが好ましく、その他、セルロース、蔗糖、ピッチ、タール等の液状物も用いられ、特にレゾール型フェノール樹脂が好ましい。また、その純度は目的により適宜制御選択が可能であるが、特に高純度の炭化ケイ素粉末が必要な場合には、各金属を5ppm以上含有していない有機化合物を用いることが望ましい。
【0019】
本発明に使用される原料粉体である高純度炭化ケイ素粉体を製造するにあたっての、炭素とケイ素のモル比(以下、C/Si比と略記)は、混合物を1000℃にて炭化して得られる炭化物中間体を、元素分析することにより定義される。化学量論的には、C/Si比が3.0の時に生成炭化ケイ素中の遊離炭素が0%となるはずであるが、実際には同時に生成するSiOガスの揮散により低C/Si比において遊離炭素が発生する。この生成炭化ケイ素粉体中の遊離炭素量が焼結体等の製造用途に適当でない量にならないように予め配合を決定することが重要である。通常、1気圧近傍で1600℃以上での焼成では、C/Si比を2.0〜2.5にすると遊離炭素を抑制することができ、この範囲を好適に用いることができる。C/Si比を2.5以上にすると遊離炭素が顕著に増加するが、この遊離炭素は粒成長を抑制する効果を持つため、粒子形成の目的に応じて適宜選択しても良い。但し、雰囲気の圧力を低圧又は高圧で焼成する場合は、純粋な炭化ケイ素を得るためのC/Si比は変動するので、この場合は必ずしも前記C/Si比の範囲に限定するものではない。
【0020】
なお、遊離炭素の焼結の際の作用は、本発明で用いられる炭化ケイ素粉体の表面に被覆された非金属系焼結助剤に由来する炭素によるものに比較して非常に弱いため、基本的には無視することができる。
【0021】
また、本発明においてケイ素源と加熱により炭素を生成する有機化合物とを均質に混合した固形物を得るために、ケイ素源と該有機化合物の混合物を硬化させて固形物とすることも必要に応じて行われる。硬化の方法としては、加熱により架橋する方法、硬化触媒により硬化する方法、電子線や放射線による方法が挙げられる。硬化触媒としては、炭素源に応じて適宜選択できるが、フェノール樹脂やフラン樹脂の場合には、トルエンスルホン酸、トルエンカルボン酸、酢酸、しゅう酸、塩酸、硫酸等の酸類、ヘキサミン等のアミン類等を用いる。
【0022】
この原料混合固形物は必要に応じ加熱炭化される。これは窒素又はアルゴン等の非酸化性雰囲気中800℃〜1000℃にて30分〜120分間該固形物を加熱することにより行われる。
【0023】
さらに、この炭化物をアルゴン等の非酸化性雰囲気中1350℃以上2000℃以下で加熱することにより炭化ケイ素が生成する。焼成温度と時間は希望する粒径等の特性に応じて適宜選択できるが、より効率的な生成のためには1600℃〜1900℃での焼成が望ましい。
【0024】
また、より高純度の粉体を必要とする時には、前述の焼成時に2000〜2100℃にて5〜20分間加熱処理を施すことにより不純物をさらに除去できる。
【0025】
以上より、特に高純度の炭化ケイ素粉末を得る方法としては、特開平9−78605号公報「単結晶の製造方法」に記載された原料粉体の製造方法を利用できる。単結晶の製造方法に記載された原料粉体の製造方法、即ち、高純度のテトラアルコキシシラン、テトラアルコキシシラン重合体から選択される1種以上をケイ素源とし、加熱により炭素を生成する高純度有機化合物を炭素源とし、これらを均質に混合して得られた混合物を非酸化性雰囲気下において加熱焼成して炭化ケイ素粉体を得る炭化ケイ素生成工程と、得られた炭化ケイ素粉体を、1700℃以上2000℃未満の温度に保持し、該温度の保持中に、2000℃〜2100℃の温度において5〜20分間にわたり加熱する処理を少なくとも1回行う後処理工程とを含み、前記2工程を行うことにより、各不純物元素の含有量が0.5ppm以下である炭化ケイ素粉体を得ること、を特徴とする高純度炭化ケイ素粉末の製造方法等を利用することができる。
【0026】
また、本発明の半導体製造装置用部材に好適に使用し得る炭化ケイ素焼結体を製造するにあたって、前記炭化ケイ素粉末と混合されて用いられる非金属系焼結助剤としては、加熱により炭素を生成する、所謂炭素源と称される物質が用いられ、加熱により炭素を生成する有機化合物又はこれらで表面を被覆された炭化ケイ素粉末(粒径:0.01〜1μm程度)が挙げられ、効果の観点からは前者が好ましい。
【0027】
加熱により炭素を生成する有機化合物としては、具体的には、残炭率の高いコールタールピッチ、ピッチタール、フェノール樹脂、フラン樹脂、エポキシ樹脂、フェノキシ樹脂やグルコース等の単糖類、蔗糖等の少糖類、セルロース、デンプン等の多糖類などの等の各種糖類が挙げられる。これらは炭化ケイ素粉末と均質に混合するという目的から、常温で液状のもの、溶媒に溶解するもの、熱可塑性或いは熱融解性のように加熱することにより軟化するもの或いは液状となるものが好適に用いられるが、なかでも、得られる成形体の強度が高いフェノール樹脂、特に、レゾール型フェノール樹脂が好適である。
【0028】
この有機化合物は加熱されると系中でカーボンブラックやグラファイトの如き無機炭素系化合物を生成し、これが焼結助剤として有効に作用すると考えられる。なお、カーボンブラックやグラファイト粉末を焼結助剤として添加しても本発明の効果を得ることはできない。
【0029】
本発明において、炭化ケイ素粉末と非金属系焼結助剤との混合物を得る際に、非金属系焼結助剤を溶媒に溶解又は分散させて混合することが好ましい。溶媒は、非金属系焼結助剤として使用する化合物に対して好適なもの、具体的には、好適な加熱により炭素を生成する有機化合物であるフェノール樹脂に対しては、エチルアルコール等の低級アルコール類やエチルエーテル、アセトン等を選択することができる。また、この非金属系焼結助剤及び溶媒についても不純物の含有量が低いものを使用することが好ましい。
【0030】
炭化ケイ素粉末と混合される非金属系焼結助剤の添加量は少なすぎると焼結体の密度が上がらず、多過ぎると焼結体に含まれる遊離炭素が増加するため高密度化を阻害する虞があるため、使用する非金属系焼結助剤の種類にもよるが、一般的には、10重量%以下、好ましくは2〜5重量%となるように添加量を調整することが好ましい。この量は、予め炭化ケイ素粉末の表面のシリカ(酸化ケイ素)量をフッ酸を用いて定量し、化学量論的にその還元に充分な量を計算することにより決定することができる。
【0031】
なお、ここでいう炭素としての添加量とは、上記の方法により定量されたシリカが非金属系焼結助剤に由来する炭素で、下記の化学反応式により還元されるものとし、非金属系焼結助剤の熱分解後の残炭率(非金属系焼結助剤中で炭素を生成する割合)などを考慮して得られる値である。
【0032】
【化1】
SiO2 + 3C → SiC + 2CO
また、本発明に係る炭化ケイ素焼結体においては、炭化ケイ素焼結体中に含まれる炭化ケイ素に由来する炭素原子及び非金属系焼結助剤に由来する炭素原子の合計が30重量%を超え、40重量%以下であることが好ましい。含有量が30重量%以下であると、焼結体中に含まれる不純物の割合が多くなり、40重量%を超えると炭素含有量が多くなり得られる焼結体の密度が低下し、焼結体の強度、耐酸化性等の諸特性が悪化するため好ましくない。
【0033】
本発明に係わる炭化ケイ素焼結体を製造するにあたって、まず、炭化ケイ素粉末と、非金属系焼結助剤とを均質に混合するが、前述の如く、非金属系焼結助剤であるフェノール樹脂をエチルアルコールなどの溶媒に溶解し、炭化ケイ素粉末と十分に混合する。混合は公知の混合手段、例えば、ミキサー、遊星ボールミルなどによって行うことができる。混合は、10〜30時間、特に、16〜24時間にわたって行うことが好ましい。十分に混合した後は、溶媒の物性に適合する温度、例えば、先に挙げたエチルアルコールの場合には50〜60℃の温度、で溶媒を除去し、混合物を蒸発乾固させたのち、篩にかけて混合物の原料粉体を得る。なお、高純度化の観点からは、ボールミル容器及びボールの材質を金属をなるべく含まない合成樹脂にする必要がある。また、乾燥にあたっては、スプレードライヤーなどの造粒装置を用いてもよい。
【0034】
本発明の半導体製造装置用部材原料に適する焼結体を製造する製造方法において必須の工程である焼結工程は、粉体の混合物又は後記の成形工程により得られた粉体の混合物の成形体を、温度2000〜2400℃、圧力300〜700kgf/cm2 、非酸化性雰囲気下で成形金型中に配置し、ホットプレスする工程である。
【0035】
ここで使用する成形金型は、得られる焼結体の純度の観点から、成形体と金型の金属部とが直接接触しないように、型の一部又は全部に黒鉛製の材料を使用するか、金型内にテフロンシート等を介在させることが好ましい。
【0036】
本発明においてホットプレスの圧力は300〜700kgf/cm2 の条件で加圧することができるが、特に、400kgf/cm2 以上の加圧した場合には、ここで使用するホットプレス部品、例えば、ダイス、パンチ等は耐圧性の良好なものを選択する必要がある。
【0037】
ここで、焼結工程を詳細に説明するが、焼結体を製造するためのホットプレス工程の前に以下の条件で加熱、昇温を行って不純物を十分に除去し、非金属系焼結助剤の炭化を完全に行わせしめた後、前記条件のホットプレス加工を行うことが必要である。
【0038】
即ち、以下の2段階の昇温工程を行うことが必要である。まず、炉内を真空下、室温から700℃に至るまで、緩やかに加熱する。ここで、高温炉の温度制御が困難な場合には、700℃まで昇温を連続的に行ってもよいが、好ましくは、炉内を10-4torrにして、室温から200℃まで緩やかに昇温し、該温度において一定時間保持する。その後、さらに緩やかに昇温を続け、700℃まで加熱する。さらに700℃前後の温度にて一定時間保持する。この第1の昇温工程において、吸着水分や有機溶媒の脱離が行われ、さらに、非金属系焼結助剤の熱分解による炭化が行われる。200℃前後或いは700℃前後の温度に保持する時間は焼結体のサイズによって好適な範囲が選択される。保持時間が十分であるか否かは真空度の低下がある程度少なくなる時点をめやすにすることができる。この段階で急激な加熱を行うと、不純物の除去や非金属系焼結助剤の炭化が十分に行われず、成形体に亀裂や空孔を生じさせる虞があるため好ましくない。
【0039】
一例を挙げれば、5〜10g程度の試料に関しては、10-4torrにして、室温から200℃まで緩やかに昇温し、該温度において約30分間保持し、その後、さらに緩やかに昇温を続け、700℃まで加熱するが、室温から700℃に至るまでの時間は6〜10時間程度、好ましくは8時間前後である。さらに700℃前後の温度にて2〜5時間程度保持することが好ましい。
【0040】
真空中で、さらに700℃から1500℃に至るまで、前記の条件であれば6〜9時間ほどかけて昇温し、1500℃の温度で1〜5時間ほど保持する。この工程では二酸化ケイ素、酸化ケイ素の還元反応が行われると考えられる。ケイ素と結合した酸素を除去するため、この還元反応を十分に完結させることが重要であり、1500℃の温度における保持時間は、この還元反応による副生物である一酸化炭素の発生が完了するまで、即ち、真空度の低下が少なくなり、還元反応開始前の温度である1300℃付近における真空度に回復するまで、行うことが必要である。この第2の昇温工程における還元反応により、炭化ケイ素粉体表面に付着して緻密化を阻害し、大粒成長の原因となる二酸化ケイ素が除去される。この還元反応中に発生するSiO、COを含む気体は不純物元素を伴っているが、真空ポンプによりこれらの発生気体が反応炉へ絶えず排出され、除去されるため、高純度化の観点からもこの温度保持を十分に行うことが好ましい。
【0041】
これらの昇温工程が終了した後に、高圧ホットプレスを行う。温度が1500℃より高温に上昇すると焼結が開始するが、その際、異常粒成長を押さえるために300〜700kgf/cm2 程度までをめやすとして加圧を開始する。その後、炉内を非酸化性雰囲気とするために不活性ガスを導入する。この不活性ガスとしては、窒素あるいは、アルゴンなどを用いるが、高温においても非反応性であることから、アルゴンガスを用いることが望ましい。
【0042】
炉内を非酸化性雰囲気とした後、温度を2000〜2400℃、圧力300〜700kgf/cm2 となるように加熱、加圧をおこなう。プレス時の圧力は原料粉体の粒径によって選択することができ、原料粉体の粒径が小さいものは加圧時の圧力が比較的小さくても好適な焼結体が得られる。また、ここで1500℃から最高温度である2000〜2400℃までへの昇温は2〜4時間かけて行うが、焼結は1850〜1900℃で急速に進行する。さらに、この最高温度で1〜3時間保持し、焼結を完了する。
【0043】
ここで最高温度が2000℃未満であると高密度化が不十分となり、2400℃を超えると粉体若しくは成形体原料が昇華(分解)する虞があるため好ましくない。また、加圧条件が300kgf/cm2 未満であると高密度化が不十分となり、700kgf/cm2 を超えると黒鉛型などの成形型の破損の原因となり、製造の効率から好ましくない。
【0044】
この焼結工程においても、得られる焼結体の純度保持の観点から、ここで用いられる黒鉛型や加熱炉の断熱材等は、高純度の黒鉛原料を用いることが好ましく、黒鉛原料は高純度処理されたものが用いられるが、具体的には、2500℃以上の温度で予め十分ベーキングされ、焼結温度で不純物の発生がないものが望ましい。さらに、使用する不活性ガスについても、不純物が少ない高純度品を使用することが好ましい。
【0045】
本発明では、前記焼結工程を行うことにより半導体製造装置用部材の基材として優れた特性を有する炭化ケイ素焼結体が得られるが、最終的に得られる焼結体の高密度化の観点から、この焼結工程に先立って以下に述べる成形工程を実施してもよい。以下にこの焼結工程に先立って行うことができる成形工程について説明する。ここで、成形工程とは、炭化ケイ素粉末と、非金属系焼結助剤とを均質に混合して得られた原料粉体を成形金型内に配置し、80〜300℃の温度範囲で、5〜60分間にわたり加熱、加圧して予め成形体を調整する工程である。ここで、原料粉体の金型への充填は極力密に行うことが、最終的な焼結体の高密度化の観点から好ましい。この成形工程を行うと、ホットプレスのために試料を充填する際に嵩のある粉体を予めコンパクトになしうるので、この成形工程を繰り返すことにより厚みの大きい成形体を製造し易くなる。
【0046】
加熱温度は、非金属系焼結助剤の特性に応じて、80〜300℃、好ましくは120〜140℃の範囲、圧力60〜100kgf/cm2 の範囲で、充填された原料粉体の密度を1.5g/cm3 以上、好ましくは、1.9g/cm3 以上とするようにプレスして、加圧状態で5〜60分間、好ましくは20〜40分間保持して原料粉体からなる成形体を得る。ここで成形体の密度は、粉体の平均粒径が小さくなる程高密度にしにくくなり、高密度化するためには成形金型内に配置する際に振動充填等の方法をとることが好ましい。具体的には、平均粒径が1μm程度の粉体では密度が1.8g/cm3 以上、平均粒径が0.5μm程度の粉体では密度が1.5g/cm3 以上であることがより好ましい。それぞれの粒径において密度が1.5g/cm3 又は1.8g/cm3 未満であると、最終的に得られる焼結体の高密度化が困難となる。
【0047】
この成形体は、次の焼結工程に付す前に、予め用いるホットプレス型に適合するように切削加工を行うことができる。この成形体を前記の温度2000〜2400℃、圧力300〜700kgf/cm2 、非酸化性雰囲気下で成形金型中に配置し、ホットプレスする工程即ち焼結工程に付して、高密度、高純度の炭化ケイ素焼結体を得るものである。
【0048】
以上により生成した炭化ケイ素焼結体は、十分に高密度化されており、密度は2.9g/cm3 以上である。得られた焼結体の密度が2.9g/cm3 未満であると、曲げ強度、破壊強度などの力学的特性や電気的な物性が低下し、さらに、パーティクルが増大し、汚染性が悪化するため好ましくない。炭化ケイ素焼結体の密度は、3.0g/cm3 以上であることがより好ましい。
【0049】
また、得られた焼結体が多孔質体であると、耐熱性、耐酸化性、耐薬品性や機械強度に劣る、洗浄が困難である、微小割れが生じて微小片が汚染物質となる、ガス透過性を有する等の物性的に劣る点を有することになり、用途が限定されるなどの問題点も生じてくる。
【0050】
本発明に用い得る炭化ケイ素焼結体の不純物の総含有量は1ppm未満であるが、半導体工業分野への適用の観点からは、これらの化学的な分析による不純物含有量は参考値としての意味を有するに過ぎない。実用的には、不純物が均一に分布しているか、局所的に偏在しているかによっても、評価が異なってくる。従って、当業者は一般的に実用装置を用いて所定の加熱条件のもとで不純物がどの程度ウェハを汚染するかを種々の手段により評価している。なお、液状のケイ素化合物と、非金属系焼結助剤と、重合又は架橋触媒と、を均質に混合して得られた固形物を非酸化性雰囲気下で加熱炭化した後、さらに、非酸化性雰囲気下で焼成する焼成工程とを含む製造方法によれば、炭化ケイ素焼結体に含まれる不純物元素の総含有量を1ppm未満にすることができる。ここで不純物元素とは、1989年IUPAC無機化学命名法改訂版の周期律表における1族から16族元素に属し、且つ、原子番号3以上であり、原子番号6〜8及び同14〜16の元素を除く元素をいう。
【0051】
その他、本発明に係る炭化ケイ素焼結体の好ましい物性について検討するに、例えば、室温における曲げ強度は50〜65kgf/mm2 、1500℃における曲げ強度は55〜80kgf/mm2 、ヤング率は3.5×104 〜4.5×104 、ビッカース硬度は2000kgf/mm2 以上、ポアソン比は0.14〜0.21、熱膨張係数は3.8×10-6〜4.2×10-6(℃-1)、熱伝導率は150W/m・k以上、比熱は0.15〜0.18cal/g・℃、耐熱衝撃性は500〜700ΔT℃、比抵抗は1Ω・cm以下であることが好ましい。
【0052】
上記の製造方法により得られた炭化ケイ素焼結体を、使用目的に応じて、加工、研磨、洗浄等の処理を行い、半導体製造装置用部材を作製する。所望の形状への加工方法としては導電性を利用した放電加工が好適に用いられる。
【0053】
ここで加工して得られる部材や加工方法について具体的に述べれば、素材からの部材の切り出しとして、ワイヤー放電加工機やダイヤモンドブレードのカッターによる直線切り出し、ワイヤー放電加工機による曲線切り出しが挙げられる。穴あけには、放電ボール盤やダイヤモンド砥石研削加工機による丸穴開け、研削加工機や型彫放電加工機による底付穴・段付穴開け、ワイヤー放電加工機や型彫放電加工機による異形穴あけ、型彫放電加工機やダイヤモンドタップ機によるネジ穴加工、円筒研削盤やダイヤモンド電着チップ使用旋盤によるオスネジ加工、ダイヤモンド砥石平面研削盤やラップ盤による平面加工、型彫放電加工機や形状研削盤による溝付け加工等が挙げられる。本発明の半導体製造装置用部材の原料である炭化ケイ素焼結体は導電性を有するため、加工範囲が広い放電加工が適用できるという利点を有する。
【0054】
放電加工機、例えば、型彫放電加工機、ワイヤー放電加工機、放電ボール盤等としては、一般の金属加工用放電加工機が使用できるが、本発明の部材に係る素材の加工には電源が高出力のほうが加工が行い易く、加工時間も短縮できる。電源回路は安定回路内蔵型、瞬間最大加工電流50アンペア以上、最大ワイヤー送り速度15m/min.以上、使用ワイヤー径0.3mm程度のコンピードワイヤー使用を目安とすることができる。また、吹き付け型ではなく、加工液浸漬型とする。
【0055】
ここで用いる焼結体によって、治具を一体的に形成することもできるが、焼結体が均質で高純度であるため、いくつかの部品を作製し、それを組み立てて治具を形成することもできる。CVD処理を行う場合には、均一な被膜を形成させるためには、治具は一体成形されたものが好ましく、複雑な形状を得る場合には、先に述べたように複雑な、そして、様々な形状の鋳型を必要としており、さらに、部材の一部が破損すると全体が使用できなくなるのが現状であったが、本発明に係る高純度の焼結体を用いれば、種々の部品の加工も公知の放電加工等により簡単に行うことができ、さらに、部品の一部が破損してもその部品のみを交換し得るという利点や面精度を向上させること(鏡面化)か容易であるという利点をも有するものである。部材を所望の形状にするための加工は、部品の切り出し、穴あけ、ネジたて、ボルト、ナットなどのファスナー製造及び鏡面加工など、公知の機械加工の手順で行うことができる。かくして得られた半導体製造装置用部材は、半導体製造装置の部品、半導体安全部品等の使用に供される。
【0056】
ここで、本発明の半導体製造装置用部材が使用される主な半導体製造装置としては、露光装置、レジスト処理装置、ドライエッチング装置、洗浄装置、熱処理装置、イオン注入装置、CVD装置、PVD装置、ダイシング装置等を挙げることができ、部品の一例としては、ドライエッチング装置用のプラズマ電極、防護リング(フォーカスリング)、イオン注入装置用のスリット部品(アパーチャー)、イオン発生部や質量分析部用の防護板、熱処理装置やCVD装置におけるウェハ処理時に用いられるダミーウェハ、また、熱処理装置やCVD装置における発熱ヒーター、特にウェハをその下部において直接加熱するヒーター等が挙げられる。
【0057】
本発明に係る素材となる炭化ケイ素焼結体の製造においては、前記加熱条件を満たしうるものであれば、特に製造装置等に制限はなく、焼結用の型の耐圧性を考慮すれば、公知の加熱炉内や反応装置を使用することができる。
【0058】
本発明に係る炭化ケイ素焼結体の原料粉体である炭化ケイ素粉体及び原料粉体を製造するためのケイ素源と非金属系焼結助剤、さらに、非酸化性雰囲気とするために用いられる不活性ガス、それぞれの純度は、各不純物元素含有量1ppm以下であることが好ましいが、加熱、焼結工程における純化の許容範囲内であれば必ずしもこれに限定するものではない。また、ここで不純物元素とは、先に述べたのと同様に、1989年IUPAC無機化学命名法改訂版の周期律表における1族から16族元素に属し、且つ、原子番号3以上であり、原子番号6〜8及び同14〜16の元素を除く元素をいう。
【0059】
【実施例】
以下に実施例を挙げて本発明を具体的に説明するが、本発明の主旨を超えない限り本実施例に限定されるものではない。
【0060】
(実施例1)
成形体の製造
高純度炭化ケイ素粉末(平均粒径1.1μm:前記特開平9−78605号公報に記載された製造方法に準じて製造された不純物含有量5ppm以下の炭化ケイ素粉末:1.5重量%のシリカを含有)90gと含水率20%の高純度液体レゾール型フェノール樹脂(熱分解後の残炭率50%)10gをエタノール150gに溶解したものとを、遊星ボールミルで18時間攪拌し、十分に混合した。その後、50〜60℃に加温してエタノールを蒸発乾固させ、500μmの篩にかけて均質な炭化ケイ素原料粉体を得た。この原料粉体8.5gを30mmφの金型に充填し130℃で20分間プレスして、密度2.1g/cm3 の成形体を得た。
【0061】
焼結体の製造
この成形体を黒鉛製型に入れ、以下の条件でホットプレスを行った。ホットプレス装置としては、高周波誘導加熱式10tホットプレスを用いた。
(焼結工程の条件)
10-5〜10-4torrの真空条件下で、室温から700℃まで6時間かけて昇温し、5時間その温度に保持した。(第1の昇温工程)
真空条件下で、700℃〜1200℃まで3時間で昇温し、さらに、1200℃〜1500℃まで3時間で昇温し、1時間その温度に保持した。(第2の昇温工程)
さらに500kgf/cm2 の圧力で加圧し、アルゴン雰囲気下にて1500℃〜2200℃まで3時間で昇温し、1時間その温度に保持した。
【0062】
(ホットプレス工程)
得られた焼結体の密度は3.15g/cm3 、ビッカース硬度は2300kgf/mm2 、電気比抵抗は0.02Ω・cmであった。この焼結体の金属不純物はいずれも0.1ppm未満であった。
【0063】
また、実施例1により得られた焼結体について物性を詳細に測定した結果、前記以外の特性として、室温における曲げ強度は57kgf/mm2 、1500℃における曲げ強度は60kgf/mm2 、ヤング率は4.1×104 、ポアソン比は0.15、熱膨張係数は3.9×10-6℃-1、熱伝導率は200W/m・k以上、比熱は0.16cal/g・℃、耐熱衝撃性は530ΔT℃であり、前記の好ましい物性を全て満たしていることが確認された。
【0064】
半導体製造装置用部材の作製
得られた焼結体を放電加工し、図1(A)、(B)、(C)及び図2(A)、(B)、(C)、(D)に示す如き部材を作製して、それらを組み合わせて図3に示す如き横形ウエハボートを作製した。図1(A)は横形ウエハボートに用いる側板10の斜視図を示し、図1(B)は両端にネジ切り部を有する外径6mm、長さ600mmの横形ウエハボートに用いる受け棒12の斜視図を示し、図1(C)は、受け棒12を支持するために複数箇所に取り付けられる支柱14の斜視図を示す。図2(A)はブラケット18に取り付けるハンドル16の斜視図を示し、図2(B)は図1(A)に示された側板10に取り付けるブラケット18の斜視図を示し、図2(C)は側板10と受け棒12との結合や、ハンドル16等の取り付けに使用するナット20、図2(D)はブラケット18を側板10に取り付けるボルト22のそれぞれ斜視図を示す。また、図3は横形ウエハボート24の概略斜視図を示す。
【0065】
半導体製造装置用部材の評価
(汚染性)
ウエハ(8インチ)をこのウエハボートに配置し、1050℃の拡散炉中で、ウエハの表面に酸化被膜を形成した。この酸化被膜中の表面より1μm以内の鉄の原子数を確認したところ、3.0×1012atoms/(1μm×1cm2 )であった。このことから、ウエハはほとんど汚染されていない、即ち、このウエハボートの汚染性は無視できるほど小さいことがわかった。
【0066】
(耐久性)
得られた部材を拡散炉に挿入し、空気の存在下1250℃まで20℃/minの速度で昇温し、1250℃に30分間保持した後、800℃まで15℃/minで冷却し、この昇温、冷却のサイクルを10回繰り返した。その後、部材表面について、クラック、ピンホール等の発生状態を目視で観察したところ、表面におけるクラック、ピンホール等の発生は認められず、昇温、冷却の繰り返しによる表面の劣化は見られなかった。
【0067】
(耐溶剤性)
得られた部材の重量を測定した後、フッ酸で30回洗浄し、洗浄後の重量を測定して重量の減少量を測定した。洗浄の前後で重量の減少は認められず、耐溶剤性に優れていることがわかった。
【0068】
(実施例2)
焼結体の製造
実施例1と同様にして得た炭化ケイ素原料粉体を8.5gとり、実施例1で行った金型に充填してプレスし、成形体を得る工程を行わずに、直接黒鉛製型に粉体を充填し、実施例1と同様の条件でホットプレスを行った。ホットプレス装置としては、実施例1と同じものを用いた。
(ホットプレス条件)
10-5〜10-4torrの真空条件下で、室温から700℃まで8時間かけて昇温し、1時間その温度に保持した。(第1の昇温工程)
真空条件下で、700℃〜1200℃まで3時間で昇温し、さらに、1200℃〜1500℃まで3時間で昇温し、4時間その温度に保持した。(第2の昇温工程)
さらに500kgf/cm2 の圧力で加圧し、アルゴン雰囲気下にて1500℃〜2200℃まで4時間で昇温し、1時間その温度に保持した。(ホットプレス工程)
得られた焼結体の密度は3.05g/cm3 、ビッカース硬度は2500kgf/mm2 、電気比抵抗は0.03Ω・cmであった。
【0069】
半導体製造装置用部材の作製と評価
得られた焼結体を用いて、実施例1と同様にして半導体製造装置用部材(ウエハボート)を作製し、実施例1と同様に評価を行ったところ、汚染性の評価結果は、8.3×1012atoms/(1μm×cm2 )であり、ウエハーボートの汚染性は無視できるほど小さいことがわかった。また、耐久性、耐溶剤性ともに実施例1と同様に優れていることが確認された。
【0070】
(比較例1)
市販の炭化ケイ素粉末85重量%、炭素粉末15重量%を混合して実施例1と同様の部材を成形した後、仮焼炉に入れて窒素ガス雰囲気下で900℃まで加熱して仮焼結体を得た。次に、これを焼結炉にセットして1550℃に加熱して金属ケイ素を含浸し、焼結を完了した。このようにして得られた焼結体を鋳込み成形してウエハボートを得た。
【0071】
得られた焼結体の密度は3.02g/cm3 、ビッカース硬度は2000kgf/mm2 、電気比抵抗は1.0×10-3Ω・cmであった。
【0072】
半導体製造装置用部材の評価
得られた半導体製造装置用部材(ウエハボート)について、実施例1と同様に評価を行ったところ、汚染性の評価結果は、1.1×1016atoms/(1μm×cm2 )であり汚染性が著しいことがわかった。また、耐久性については、8回目の昇温時に接合部に亀裂が生じ、耐溶剤性については、15%の重量減少が見られ、ウエハ投入部に欠損が観察され、耐久性、耐溶剤性ともに不充分であった。
【0073】
(比較例2)
比較例1で鋳込み成形により得られたウエハボートの表面に、1000℃で、メチルトリクロロシランを原料ガスとして炭化ケイ素被膜をCVD処理により形成した。被膜の厚みは10〜100μmであった。
【0074】
半導体製造装置用部材の評価
得られた半導体製造装置用部材(ウエハボート)について、実施例1と同様に評価を行ったところ、汚染性の評価結果は、4.6×1012atoms/(1μm×cm2 )であり汚染性は、無視できるほど小さいことがわかった。また、耐久性については、7回目の昇温時に表面に亀裂が観察され、8回目には接合部に亀裂が生じ、耐久性が不充分であった。耐溶剤性については、フッ酸洗浄後も重量減少は観察されず、耐溶剤性には優れることがわかった。
【0075】
前記の各実施例並びに比較例に明らかなように、本発明の方法により得られた実施例1、2の半導体製造装置用部材は、放電加工及び研削加工による部品を組み合わせることにより簡単に製造し得るとともに、耐久性、耐溶剤性に優れ、汚染性は無視できるほど小さいことがわかった。一方、従来法により得られた比較例1の半導体製造装置用部材は、耐久性、耐溶剤性ともに不充分で、汚染性は顕著であった。また、この表面にCVD処理による被膜を形成した比較例2の半導体製造装置用部材は、汚染性、耐溶剤性に優れていたが、製造が煩雑であり、また、被膜強度の問題から耐久性に問題があることがわかった。
【0076】
このように、本発明の半導体製造装置用部材は組立式の部材としても優れた特性を示すため、近年の半導体製造装置用の大型化に伴う大型部材への要求に対しても、焼結体製造装置を大型化することなく対応し得るという利点をも示すものである。
【0077】
【発明の効果】
本発明の半導体製造装置用部材は、高密度性、高純度性、高導電性、高熱伝導率を兼ね備えた高品位の炭化ケイ素焼結体よりなるため、製造、加工が簡単であり、金属元素による半導体の汚染がなく、優れた耐久性、耐溶剤性を有していた。
【図面の簡単な説明】
【図1】(A)は炭化ケイ素焼結体を放電加工して得られた横形ウエハボートに用いる側板、(B)は同じく受け棒、(C)は支柱の側面図を示す。
【図2】(A)は炭化ケイ素焼結体を放電加工して得られた横形ウエハボートに用いるブラケットのハンドル、(B)は図1(A)に示す側板に取り付けるブラケットの側面図を示す。(C)はナット、(D)はボルトの側面図を示す。
【図3】実施例1の横形ウエハボートの概略斜視図を示す。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a member for a semiconductor manufacturing apparatus.And its manufacturing methodIn particular, a semiconductor manufacturing apparatus member having excellent durability and high characteristics using a silicon carbide sintered body having excellent characteristicsAnd its manufacturing methodIt is about.
[0002]
[Prior art]
Semiconductor manufacturing equipment members such as soaking tubes (liner tubes) used to manufacture semiconductors, reaction tubes (process tubes) through which reaction gases flow, jigs (wafer boats) on which semiconductor wafers are placed are dense, heat resistant, Since high characteristics such as rigidity are required, the use of silicon carbide tends to increase. Conventionally, when a member for a semiconductor manufacturing apparatus is produced using silicon carbide, a method in which a binder is added to a raw material powder, and after molding, firing, sintering, and a process of melting and impregnating metal silicon has been widely used. Yes.
[0003]
A conventional member for a semiconductor manufacturing apparatus using silicon carbide has a problem of contaminating a semiconductor wafer to be manufactured because metal impurities inside silicon carbide diffuse and move in the member during high temperature processing. As a method of preventing contamination of the wafer due to the impurities of silicon carbide, a method of producing a member with a high-purity raw material, and forming a high-purity silicon carbide film on the surface of the member by CVD (chemical vapor deposition) treatment Method etc.
Yes.
[0004]
However, even if high-purity silicon carbide with an impure metal content on the order of several ppm or less is used, it is necessary to purify the porous sintered body before impregnation with metal silicon. There was a problem of metal silicon elution in the washing and acid treatment processes. Therefore, in order to further increase the purity and improve the durability, a CVD process is performed to coat the surface of the member with a silicon carbide film. However, this CVD process requires a large amount of equipment and increases the production cost. Further, this CVD film has a problem that the durability of the anti-contamination effect is lacking due to peeling from the base material or pinholes or cracks during repeated rapid heating and rapid cooling cycles.
[0005]
In addition, the base material for performing this CVD process is formed in the shape of a jig in advance by a reaction sintering method by means such as casting, but in recent years the wafer size has increased and the shape of the reaction tube has changed. Along with this, various shapes of the base material are required, and a mold is required for each member, which also increases the manufacturing cost.
[0006]
[Problems to be solved by the invention]
The present invention has been made in consideration of the above-mentioned problems, and its object is to prevent contamination by metal impurities such as wafers using a high-density and high-purity silicon carbide sintered body. Can be manufactured, has low productivity, has low durability, and has excellent durability and solvent resistance.And its manufacturing methodIs to provide.
[0007]
[Means for Solving the Problems]
As a result of intensive studies on the development of the sintering method as described above, the present inventors represented carbon on the surface of the silicon carbide powder in advance.It is an organic compound that produces carbon by heating.Producing semiconductors with excellent characteristics by using high-density and high-purity sintered silicon carbide obtained by combining appropriate amounts of non-metallic sintering aids and combining hot pressing under specific conditions It discovered that the member for apparatuses was obtained and completed this invention.
[0008]
That is, the member for a semiconductor manufacturing apparatus of the present invention comprises a mixture of silicon carbide powder and a nonmetallic sintering aid that is an organic compound that generates carbon by heating.After performing a first temperature rise to be heated to 700 ° C. and held and a second temperature rise to be further heated to 1500 ° C. and held,Temperature 2000-2400 ° C, pressure 300-700kgf / cm2A sintered body obtained by sintering by hot pressing in a non-oxidizing atmosphere and having a density of 2.9 g / cmThreeAs described above, a silicon carbide sintered body having a total content of impurity elements of less than 1 ppm is used.
Moreover, the method for producing a member for a semiconductor manufacturing apparatus according to the present invention comprises a step of preparing a mixture of silicon carbide powder and a nonmetallic sintering aid that is an organic compound that generates carbon by heating, and the mixtureA first temperature raising step of heating and holding up to 700 ° C., a second temperature raising step of heating and holding up to 1500 ° C., and thenTemperature 2000-2400 ° C, pressure 300-700kgf / cm2And hot pressing in a non-oxidizing atmosphere.
[0009]
The silicon carbide sintered body used here preferably has a specific resistance of 1 Ω · cm or less and a thermal conductivity of 200 W / m · k or more.New.
[0010]
Since the semiconductor manufacturing apparatus member of the present invention uses a high-purity and high-density silicon carbide sintered body, it does not contain metallic silicon, and is strong even by heating exceeding 1500 ° C., which is the melting point of silicon. Is not stable and is stable to acid treatment. Further, since this member can be easily subjected to electric discharge machining, it can also be made as an assembly type, thereby increasing the degree of freedom in designing the semiconductor manufacturing apparatus member, and even when manufacturing a large member, This can be handled by a large-scale sintered body manufacturing apparatus.
[0011]
DETAILED DESCRIPTION OF THE INVENTION
The present invention is described in further detail below. First, the silicon carbide sintered body constituting the member for a semiconductor manufacturing apparatus of the present invention will be described.
[0012]
The silicon carbide sintered body used as the base material of the member for a semiconductor manufacturing apparatus of the present invention uses, as a raw material, silicon carbide powder that is α-type, β-type, amorphous, or a mixture thereof. Β-type silicon carbide powder is preferably used. The grade of this β-type silicon carbide powder is not particularly limited, and for example, commercially available β-type silicon carbide powder can be used. The particle size of the silicon carbide powder is preferably small from the viewpoint of densification, and is preferably about 0.01 to 10 μm, and more preferably about 0.05 to 1 μm. If the particle size is less than 0.01 μm, handling in processing steps such as weighing and mixing becomes difficult, and if it exceeds 10 μm, the specific surface area is small, that is, the contact area with the adjacent powder becomes small, and the density increases. Is not preferable because it becomes difficult.
[0013]
As a preferred embodiment of the silicon carbide raw material powder, the particle diameter is 0.05 to 1 μm and the specific surface area is 5 m.2/ G or more, free carbon 1% or less, oxygen content 1% or less is preferably used. Further, the particle size distribution of the silicon carbide powder to be used is not particularly limited, and at the time of producing a silicon carbide sintered body, two or more maximums are obtained from the viewpoint of improving the packing density of the powder and the reactivity of the silicon carbide. Those having a value can also be used.
[0014]
In order to obtain a high-purity silicon carbide sintered body, a high-purity silicon carbide powder may be used as the raw material silicon carbide powder.
[0015]
High purity silicon carbide powder includes, for example, a silicon source containing at least one or more liquid silicon compounds, a carbon source containing at least one or more liquid organic compounds that generate carbon by heating, and a polymerization or crosslinking catalyst. And a baking step of baking a solid material obtained by homogeneous mixing in a non-oxidizing atmosphere.
[0016]
As a silicon compound (hereinafter, appropriately referred to as a silicon source) used for production of high-purity silicon carbide powder, a liquid and a solid can be used in combination, but at least one is selected from a liquid It must be done. As the liquid, a polymer of alkoxysilane (mono-, di-, tri-, tetra-) and tetraalkoxysilane is used. Among the alkoxysilanes, tetraalkoxysilane is preferably used, and specific examples include methoxysilane, ethoxysilane, propoxysilane, butoxysilane, and the like. From the viewpoint of handling, ethoxysilane is preferable. Examples of the tetraalkoxysilane polymer include a low molecular weight polymer (oligomer) having a degree of polymerization of about 2 to 15 and a silicate polymer having a higher degree of polymerization, which are liquid. Examples of solid materials that can be used in combination with these include silicon oxide. In the present invention, silicon oxide includes silica sol (a colloidal ultrafine silica-containing liquid containing OH groups and alkoxyl groups inside), silicon dioxide (silica gel, fine silica, quartz powder) and the like in addition to SiO.
[0017]
Among these silicon sources, from the viewpoint of good homogeneity and handling properties, an oligomer of tetraethoxysilane and a mixture of an oligomer of tetraethoxysilane and fine powder silica are preferable. These silicon sources are high-purity substances, and the initial impurity content is preferably 20 ppm or less, more preferably 5 ppm or less.
[0018]
Moreover, as an organic compound which produces | generates carbon by the heating used for manufacture of a high purity silicon carbide powder, in addition to a liquid thing, a liquid thing and a solid thing can be used together, and a residual carbon ratio is high, In addition, an organic compound that is polymerized or cross-linked by a catalyst or heating, specifically, a monomer or prepolymer of a resin such as phenol resin, furan resin, polyimide, polyurethane, and polyvinyl alcohol is preferable. In addition, cellulose, sucrose, pitch, and tar Etc., and a resol type phenol resin is particularly preferable. In addition, the purity can be appropriately controlled and selected depending on the purpose, but when a high-purity silicon carbide powder is required, it is desirable to use an organic compound that does not contain 5 ppm or more of each metal.
[0019]
The molar ratio of carbon to silicon (hereinafter abbreviated as C / Si ratio) in producing high-purity silicon carbide powder that is a raw material powder used in the present invention is obtained by carbonizing the mixture at 1000 ° C. The resulting carbide intermediate is defined by elemental analysis. Stoichiometrically, when the C / Si ratio is 3.0, the free carbon in the generated silicon carbide should be 0%. However, in practice, the low C / Si ratio is caused by volatilization of the SiO gas generated at the same time. Free carbon is generated in It is important to determine the formulation in advance so that the amount of free carbon in the generated silicon carbide powder does not become an amount that is not suitable for the purpose of manufacturing a sintered body or the like. Usually, in firing at 1600 ° C. or more near 1 atm, free carbon can be suppressed when the C / Si ratio is set to 2.0 to 2.5, and this range can be suitably used. When the C / Si ratio is 2.5 or more, free carbon significantly increases. However, since this free carbon has an effect of suppressing grain growth, it may be appropriately selected according to the purpose of grain formation. However, when the atmosphere is fired at a low pressure or a high pressure, the C / Si ratio for obtaining pure silicon carbide varies, and in this case, it is not necessarily limited to the range of the C / Si ratio.
[0020]
In addition, since the action at the time of sintering free carbon is very weak compared to that due to carbon derived from the nonmetallic sintering aid coated on the surface of the silicon carbide powder used in the present invention, Basically it can be ignored.
[0021]
Further, in the present invention, in order to obtain a solid material in which the silicon source and the organic compound that generates carbon by heating are homogeneously mixed, the mixture of the silicon source and the organic compound is cured to form a solid material as necessary. Done. Examples of the curing method include a method of crosslinking by heating, a method of curing with a curing catalyst, and a method of electron beam or radiation. The curing catalyst can be appropriately selected according to the carbon source, but in the case of phenol resin or furan resin, acids such as toluenesulfonic acid, toluenecarboxylic acid, acetic acid, oxalic acid, hydrochloric acid, sulfuric acid, and amines such as hexamine Etc. are used.
[0022]
This raw material mixed solid is heated and carbonized as necessary. This is done by heating the solid for 30 minutes to 120 minutes at 800 ° C. to 1000 ° C. in a non-oxidizing atmosphere such as nitrogen or argon.
[0023]
Furthermore, silicon carbide is produced by heating this carbide at 1350 ° C. or more and 2000 ° C. or less in a non-oxidizing atmosphere such as argon. The firing temperature and time can be appropriately selected according to the desired properties such as particle size, but firing at 1600 ° C. to 1900 ° C. is desirable for more efficient production.
[0024]
In addition, when a powder with higher purity is required, impurities can be further removed by performing a heat treatment at 2000 to 2100 ° C. for 5 to 20 minutes during the aforementioned baking.
[0025]
From the above, as a method for obtaining a particularly high-purity silicon carbide powder, the raw material powder production method described in JP-A-9-78605 “Production method of single crystal” can be used. The raw material powder manufacturing method described in the method for manufacturing a single crystal, that is, high purity in which carbon is generated by heating using one or more selected from high-purity tetraalkoxysilane and tetraalkoxysilane polymer as a silicon source A silicon carbide production step of obtaining a silicon carbide powder by heating and firing a mixture obtained by uniformly mixing an organic compound as a carbon source in a non-oxidizing atmosphere, and the obtained silicon carbide powder, A post-treatment step of holding at a temperature of 1700 ° C. or higher and lower than 2000 ° C., and performing the heating at a temperature of 2000 ° C. to 2100 ° C. for 5 to 20 minutes at least once during the holding of the temperature. To obtain a silicon carbide powder having a content of each impurity element of 0.5 ppm or less by performing a method of producing high-purity silicon carbide powder, etc. Rukoto can.
[0026]
Further, in the production of a silicon carbide sintered body that can be suitably used for a member for a semiconductor manufacturing apparatus of the present invention, the non-metallic sintering aid used by mixing with the silicon carbide powder is carbon by heating. The so-called carbon source that is generated is used, and includes organic compounds that generate carbon by heating, or silicon carbide powder (particle size: about 0.01 to 1 μm) whose surface is coated with these compounds. From the viewpoint of the above, the former is preferable.
[0027]
Specific examples of organic compounds that generate carbon by heating include coal tar pitch, pitch tar, phenol resin, furan resin, epoxy resin, phenoxy resin, monosaccharides such as glucose, sucrose, and the like with a high residual carbon ratio. Various saccharides, such as saccharides, polysaccharides, such as a cellulose and starch, are mentioned. For the purpose of being homogeneously mixed with silicon carbide powder, those that are liquid at room temperature, those that dissolve in a solvent, those that soften by heating such as thermoplasticity or heat melting, or those that become liquid are suitable. Among them, a phenol resin, particularly a resol type phenol resin, having high strength of the obtained molded body is preferable.
[0028]
When this organic compound is heated, it produces inorganic carbon compounds such as carbon black and graphite in the system, which are considered to act effectively as a sintering aid. Even if carbon black or graphite powder is added as a sintering aid, the effect of the present invention cannot be obtained.
[0029]
In the present invention, when obtaining a mixture of the silicon carbide powder and the nonmetallic sintering aid, it is preferable to mix the nonmetallic sintering aid dissolved or dispersed in a solvent. The solvent is suitable for a compound used as a non-metallic sintering aid, specifically, for a phenol resin that is an organic compound that generates carbon by suitable heating, a lower solvent such as ethyl alcohol. Alcohols, ethyl ether, acetone and the like can be selected. Also, it is preferable to use a non-metallic sintering aid and a solvent having a low impurity content.
[0030]
If the amount of the non-metallic sintering aid mixed with the silicon carbide powder is too small, the density of the sintered body will not increase, and if it is too large, the free carbon contained in the sintered body will increase, which will hinder densification. Depending on the type of non-metallic sintering aid used, the amount of addition may be adjusted to generally 10% by weight or less, preferably 2 to 5% by weight. preferable. This amount can be determined by previously quantifying the amount of silica (silicon oxide) on the surface of the silicon carbide powder using hydrofluoric acid and calculating the amount stoichiometrically sufficient for the reduction.
[0031]
The amount added as carbon here means that the silica quantified by the above method is carbon derived from a non-metallic sintering aid and is reduced by the following chemical reaction formula, This is a value obtained in consideration of the residual carbon ratio after pyrolysis of the sintering aid (ratio of generating carbon in the nonmetallic sintering aid).
[0032]
[Chemical 1]
SiO2 + 3C → SiC + 2CO
In the silicon carbide sintered body according to the present invention, the total of carbon atoms derived from silicon carbide and nonmetallic sintering aids contained in the silicon carbide sintered body is 30% by weight. It is preferably 40% by weight or less. When the content is 30% by weight or less, the proportion of impurities contained in the sintered body increases, and when it exceeds 40% by weight, the carbon content increases and the density of the resulting sintered body decreases, and the sintered body is sintered. It is not preferable because various properties such as strength and oxidation resistance of the body deteriorate.
[0033]
In producing the silicon carbide sintered body according to the present invention, first, silicon carbide powder and a nonmetallic sintering aid are mixed homogeneously. As described above, phenol which is a nonmetallic sintering aid is used. The resin is dissolved in a solvent such as ethyl alcohol and mixed well with the silicon carbide powder. Mixing can be performed by a known mixing means such as a mixer or a planetary ball mill. The mixing is preferably performed for 10 to 30 hours, particularly 16 to 24 hours. After thorough mixing, the solvent is removed at a temperature compatible with the physical properties of the solvent, such as 50-60 ° C. in the case of ethyl alcohol, and the mixture is evaporated to dryness. To obtain a raw material powder of the mixture. From the viewpoint of high purity, it is necessary to use a synthetic resin that contains as little metal as possible for the material of the ball mill container and the ball. In drying, a granulator such as a spray dryer may be used.
[0034]
The sintering step, which is an essential step in the production method for producing a sintered body suitable for a raw material for a semiconductor manufacturing apparatus according to the present invention, is a powder mixture or a molded body of a powder mixture obtained by a molding step described later. , Temperature 2000-2400 ° C., pressure 300-700 kgf / cm2This is a step of placing in a molding die in a non-oxidizing atmosphere and hot pressing.
[0035]
From the viewpoint of the purity of the obtained sintered body, the molding die used here uses a graphite material for part or all of the mold so that the molded body and the metal part of the mold do not come into direct contact with each other. Alternatively, it is preferable to interpose a Teflon sheet or the like in the mold.
[0036]
In the present invention, the pressure of the hot press is 300 to 700 kgf / cm.2The pressure can be applied under the conditions of 400 kgf / cm.2When the pressure is applied as described above, it is necessary to select a hot-pressed part used here, for example, a die, a punch or the like having good pressure resistance.
[0037]
Here, the sintering process will be described in detail. Before the hot pressing process for producing a sintered body, heating and heating are performed under the following conditions to sufficiently remove impurities, and non-metallic sintering. After the auxiliary agent is completely carbonized, hot pressing under the above conditions may be performed.is necessary.
[0038]
That is, the following two-step temperature raising process can be performed.is necessary. First, the inside of the furnace is gently heated from room temperature to 700 ° C. under vacuum. Here, when it is difficult to control the temperature of the high-temperature furnace, the temperature may be continuously increased up to 700 ° C.-FourTorr, the temperature is gradually raised from room temperature to 200 ° C., and the temperature is maintained for a certain period of time. Thereafter, the temperature is further gradually raised and heated to 700 ° C. Further, it is held for a certain time at a temperature of around 700 ° C. In this first temperature raising step, adsorbed moisture and organic solvent are desorbed, and further, carbonization by thermal decomposition of the nonmetallic sintering aid is performed. A suitable range of the time for maintaining the temperature at around 200 ° C. or around 700 ° C. is selected depending on the size of the sintered body. Whether or not the holding time is sufficient can make it easy to identify the time when the decrease in the degree of vacuum is reduced to some extent. If rapid heating is performed at this stage, impurities are not sufficiently removed and carbonization of the nonmetallic sintering aid is not sufficiently performed, which may cause cracks and voids in the molded body, which is not preferable.
[0039]
As an example, for a sample of about 5-10 g, 10-FourTorr is gradually raised from room temperature to 200 ° C., held at that temperature for about 30 minutes, and then further gently raised and heated to 700 ° C. The time from room temperature to 700 ° C. Is about 6 to 10 hours, preferably about 8 hours. Furthermore, it is preferable to hold at about 700 ° C. for about 2 to 5 hours.
[0040]
In vacuum, from 700 ° C. to 1500 ° C., the temperature is increased over 6 to 9 hours under the above conditions, and the temperature is maintained at 1500 ° C. for 1 to 5 hours. In this step, it is considered that a reduction reaction of silicon dioxide and silicon oxide is performed. In order to remove oxygen bonded to silicon, it is important to complete the reduction reaction sufficiently. The holding time at a temperature of 1500 ° C. is sufficient until generation of carbon monoxide as a by-product by the reduction reaction is completed. That is, it is necessary to carry out the process until the degree of vacuum decreases and the degree of vacuum is restored to around 1300 ° C., which is the temperature before the start of the reduction reaction. By the reduction reaction in the second temperature raising step, silicon dioxide that adheres to the surface of the silicon carbide powder and inhibits densification and causes large grain growth is removed. Gases containing SiO and CO generated during this reduction reaction are accompanied by impurity elements, but these generated gases are constantly discharged and removed by the vacuum pump to the reaction furnace. It is preferable to sufficiently maintain the temperature.
[0041]
After these heating steps are completed, high-pressure hot pressing is performed.Yeah.Sintering starts when the temperature rises above 1500 ° C., but at that time, 300 to 700 kgf / cm in order to suppress abnormal grain growth.2Pressurization is started as an indication of the degree. Thereafter, an inert gas is introduced to make the inside of the furnace a non-oxidizing atmosphere. Nitrogen or argon is used as this inert gas, but it is desirable to use argon gas because it is non-reactive even at high temperatures.
[0042]
After making the inside of the furnace a non-oxidizing atmosphere, the temperature is 2000-2400 ° C., the pressure 300-700 kgf / cm.2Heat and pressurize so that The pressure at the time of pressing can be selected according to the particle size of the raw material powder, and those having a small particle size of the raw material powder can obtain a suitable sintered body even when the pressure at the time of pressurization is relatively small. In addition, the temperature rise from 1500 ° C. to the maximum temperature of 2000 to 2400 ° C. is performed over 2 to 4 hours, but the sintering proceeds rapidly at 1850 to 1900 ° C. Further, the sintering is completed at this maximum temperature for 1 to 3 hours.
[0043]
Here, if the maximum temperature is less than 2000 ° C., the densification is insufficient, and if it exceeds 2400 ° C., the powder or the raw material of the molded body may be sublimated (decomposed). Also, pressurization condition is300kgf / cm2If it is less than 700, the densification is insufficient, and 700 kgf / cm.2Exceeding this may cause damage to a mold such as a graphite mold, which is not preferable from the viewpoint of production efficiency.
[0044]
Also in this sintering step, from the viewpoint of maintaining the purity of the sintered body to be obtained, it is preferable to use a high-purity graphite raw material for the graphite mold and the heat insulating material used in the heating furnace, and the graphite raw material has a high purity. Although what was processed is used, specifically, what is sufficiently baked at a temperature of 2500 ° C. or higher and does not generate impurities at the sintering temperature is desirable. Furthermore, it is preferable to use a high-purity product with few impurities for the inert gas to be used.
[0045]
In the present invention, by performing the sintering step, a silicon carbide sintered body having excellent characteristics as a base material for a member for a semiconductor manufacturing apparatus can be obtained. From the viewpoint of increasing the density of the finally obtained sintered body. Therefore, a molding process described below may be performed prior to this sintering process. The molding process that can be performed prior to this sintering process will be described below. Here, the molding step is a process in which raw material powder obtained by homogeneously mixing silicon carbide powder and a nonmetallic sintering aid is placed in a molding die, and the temperature ranges from 80 to 300 ° C. In this step, the molded body is preliminarily adjusted by heating and pressurizing for 5 to 60 minutes. Here, the filling of the raw material powder into the mold is preferably performed as densely as possible from the viewpoint of increasing the density of the final sintered body. When this molding step is performed, a bulky powder can be made compact in advance when the sample is filled for hot pressing, and thus it becomes easy to produce a molded body having a large thickness by repeating this molding step.
[0046]
The heating temperature is 80 to 300 ° C., preferably in the range of 120 to 140 ° C., and the pressure is 60 to 100 kgf / cm, depending on the characteristics of the nonmetallic sintering aid.2In the range of 1.5 to 1.5 g / cmThreeOr more, preferably 1.9 g / cmThreeIt presses as mentioned above, and it hold | maintains for 5 to 60 minutes in a pressurized state, Preferably it is 20 to 40 minutes, and the molded object which consists of raw material powder is obtained. Here, the density of the molded body becomes difficult to increase as the average particle diameter of the powder decreases, and in order to increase the density, it is preferable to take a method such as vibration filling when placing in the molding die. . Specifically, a powder having an average particle diameter of about 1 μm has a density of 1.8 g / cm.ThreeAs described above, the density of the powder having an average particle diameter of about 0.5 μm is 1.5 g / cm.ThreeMore preferably. The density is 1.5 g / cm at each particle size.ThreeOr 1.8 g / cmThreeIf it is less than this, it will be difficult to increase the density of the finally obtained sintered body.
[0047]
This molded body can be cut so as to be compatible with a hot press die used in advance before being subjected to the next sintering step. This molded body was subjected to the above-mentioned temperature 2000-2400 ° C., pressure 300-700 kgf / cm.2A step of placing in a mold in a non-oxidizing atmosphere and hot pressing;SinteringA high-density, high-purity silicon carbide sintered body is obtained through the process.
[0048]
The silicon carbide sintered body produced as described above is sufficiently densified, and the density is 2.9 g / cm.ThreeThat's it. The density of the obtained sintered body is 2.9 g / cm.ThreeIf it is less than the range, the mechanical properties such as bending strength and fracture strength and the electrical physical properties are lowered, and further, the number of particles is increased and the contamination is deteriorated. The density of the silicon carbide sintered body is 3.0 g / cm.ThreeMore preferably.
[0049]
In addition, if the obtained sintered body is a porous body, it is inferior in heat resistance, oxidation resistance, chemical resistance and mechanical strength, is difficult to clean, microcracks occur, and microscopic pieces become contaminants. In other words, it has inferior physical properties such as gas permeability and has problems such as limited use.
[0050]
The total content of impurities in the sintered silicon carbide that can be used in the present invention isLess than 1ppmHowever, from the viewpoint of application to the semiconductor industry field, the impurity content by these chemical analyzes has only a meaning as a reference value. Practically, the evaluation differs depending on whether the impurities are uniformly distributed or locally distributed. Therefore, those skilled in the art generally use various means to evaluate how much impurities contaminate the wafer under a predetermined heating condition using a practical apparatus. A solid material obtained by homogeneously mixing a liquid silicon compound, a nonmetallic sintering aid, and a polymerization or crosslinking catalyst is heated and carbonized in a nonoxidizing atmosphere, and then further nonoxidized. According to the manufacturing method including the firing step of firing in a neutral atmosphere, the total content of impurity elements contained in the silicon carbide sintered body is 1 ppm.Less thanCan be. Here, the impurity element belongs to the group 1 to
[0051]
In addition, when examining preferable physical properties of the silicon carbide sintered body according to the present invention, for example, the bending strength at room temperature is 50 to 65 kgf / mm.2Flexural strength at 1500 ° C is 55-80 kgf / mm2Young's modulus is 3.5 × 10Four~ 4.5 × 10Four, Vickers hardness is 2000kgf / mm2As described above, the Poisson's ratio is 0.14 to 0.21, and the thermal expansion coefficient is 3.8 × 10-6~ 4.2 × 10-6(℃-1The thermal conductivity is preferably 150 W / m · k or more, the specific heat is 0.15 to 0.18 cal / g · ° C., the thermal shock resistance is 500 to 700 ΔT ° C., and the specific resistance is preferably 1 Ω · cm or less.
[0052]
The silicon carbide sintered body obtained by the above manufacturing method is subjected to processing such as processing, polishing, and washing according to the purpose of use, and a member for a semiconductor manufacturing apparatus is manufactured. As a processing method to a desired shape, electrical discharge machining utilizing conductivity is preferably used.
[0053]
The members and processing methods obtained by processing here will be specifically described. Examples of cutting out members from the material include straight line cutting with a wire electric discharge machine or diamond blade cutter, and curve cutting with a wire electric discharge machine. For drilling, round drilling with an electric discharge drilling machine or diamond grinding wheel grinding machine, bottomed hole / stepped drilling with a grinding machine or die-cutting electric discharge machine, irregular drilling with a wire electric discharge machine or die-sinking electric discharge machine, Screw hole drilling with a die-sinking electrical discharge machine or diamond tap machine, male thread machining with a cylindrical grinder or lathe using diamond electrodeposition tips, surface machining with a diamond grinding wheel surface grinder or lapping machine, with an electric discharge machine or shape grinder A grooving process etc. are mentioned. Since the silicon carbide sintered body which is a raw material of the member for a semiconductor manufacturing apparatus of the present invention has conductivity, it has an advantage that electric discharge machining with a wide machining range can be applied.
[0054]
As an electric discharge machine, for example, a die-sinking electric discharge machine, a wire electric discharge machine, an electric discharge drilling machine, etc., a general electric discharge machine for metal working can be used, but a power source is high for processing a material related to the member of the present invention. The output is easier to process and the processing time can be shortened. The power circuit has a built-in stable circuit, instantaneous maximum machining current of 50 amperes or more, maximum wire feed speed of 15 m / min. As described above, the use of a composite wire having a wire diameter of about 0.3 mm can be used as a guide. Moreover, it is not a spray type but a machining liquid immersion type.
[0055]
Depending on the sintered body used here, the jig can be formed integrally, but since the sintered body is homogeneous and highly pure, several parts are produced and assembled to form the jig. You can also. In the case of performing CVD processing, in order to form a uniform film, the jig is preferably integrally formed. When obtaining a complicated shape, as described above, the jig is complicated and various. However, if a part of the member is broken, the whole cannot be used. However, if the high-purity sintered body according to the present invention is used, various parts can be processed. Can be easily performed by known electric discharge machining, etc., and even if part of the part is damaged, it is easy to improve the advantage and surface accuracy (mirroring) that only the part can be replaced It also has advantages. The processing for forming the member into a desired shape can be performed by known machining procedures such as part cutting, drilling, screwing, manufacturing of fasteners such as bolts and nuts, and mirror finishing. The member for a semiconductor manufacturing apparatus thus obtained is used for parts of a semiconductor manufacturing apparatus, semiconductor safety parts, and the like.
[0056]
Here, as the main semiconductor manufacturing apparatus in which the semiconductor manufacturing apparatus member of the present invention is used, an exposure apparatus, a resist processing apparatus, a dry etching apparatus, a cleaning apparatus, a heat treatment apparatus, an ion implantation apparatus, a CVD apparatus, a PVD apparatus, Examples of parts include a plasma electrode for a dry etching apparatus, a protective ring (focus ring), a slit part (aperture) for an ion implantation apparatus, an ion generation unit, and a mass analysis unit. Examples include a protective plate, a dummy wafer used during wafer processing in a heat treatment apparatus or a CVD apparatus, and a heat generating heater in the heat treatment apparatus or the CVD apparatus, particularly a heater that directly heats the wafer in the lower portion thereof.
[0057]
In the production of a silicon carbide sintered body that is a material according to the present invention, as long as the heating conditions can be satisfied, the production apparatus is not particularly limited, and considering the pressure resistance of the sintering mold, A known heating furnace or a reaction apparatus can be used.
[0058]
Silicon carbide powder that is a raw material powder of the silicon carbide sintered body according to the present invention, a silicon source for producing the raw material powder, a non-metallic sintering aid, and further used for a non-oxidizing atmosphere The purity of each inert gas to be produced is preferably 1 ppm or less for each impurity element, but is not necessarily limited to this as long as it is within the allowable range of purification in the heating and sintering processes. Further, the impurity element here belongs to the group 1 to
[0059]
【Example】
Hereinafter, the present invention will be specifically described with reference to examples. However, the present invention is not limited to these examples as long as the gist of the present invention is not exceeded.
[0060]
Example 1
Manufacturing of compacts
High-purity silicon carbide powder (average particle size 1.1 μm: silicon carbide powder produced according to the production method described in JP-A-9-78605 and having an impurity content of 5 ppm or less: 1.5 wt% silica 90 g) and 10 g of high-purity liquid resol type phenolic resin with a water content of 20% (residual carbon ratio after thermal decomposition of 50%) dissolved in 150 g of ethanol are stirred for 18 hours with a planetary ball mill and mixed thoroughly. did. Thereafter, the mixture was heated to 50 to 60 ° C. to evaporate ethanol to dryness, and passed through a 500 μm sieve to obtain a homogeneous silicon carbide raw material powder. 8.5 g of this raw material powder was filled in a 30 mmφ mold and pressed at 130 ° C. for 20 minutes to obtain a density of 2.1 g / cm 2.ThreeA molded body of was obtained.
[0061]
Production of sintered body
This compact was put into a graphite mold and hot pressed under the following conditions. As a hot press apparatus, a high-frequency induction heating type 10t hot press was used.
(Conditions for sintering process)
10-Five-10-FourUnder a torr vacuum condition, the temperature was raised from room temperature to 700 ° C. over 6 hours and held at that temperature for 5 hours. (First temperature raising step)
Under vacuum conditions, the temperature was raised from 700 ° C. to 1200 ° C. over 3 hours, further raised from 1200 ° C. to 1500 ° C. over 3 hours, and held at that temperature for 1 hour. (Second temperature raising step)
500 kgf / cm2Then, the temperature was increased from 1500 ° C. to 2200 ° C. in 3 hours under an argon atmosphere, and the temperature was maintained for 1 hour.
[0062]
(Hot press process)
The density of the obtained sintered body is 3.15 g / cm.ThreeVickers hardness is 2300kgf / mm2The electrical resistivity was 0.02 Ω · cm. The metal impurities in this sintered body were all less than 0.1 ppm.
[0063]
Moreover, as a result of measuring the physical properties of the sintered body obtained in Example 1 in detail, as a property other than the above, the bending strength at room temperature was 57 kgf / mm.2Flexural strength at 1500 ° C is 60kgf / mm2Young's modulus is 4.1 × 10FourPoisson's ratio is 0.15 and thermal expansion coefficient is 3.9 × 10-6℃-1The thermal conductivity was 200 W / m · k or more, the specific heat was 0.16 cal / g · ° C., and the thermal shock resistance was 530ΔT ° C., confirming that all of the above preferred physical properties were satisfied.
[0064]
Fabrication of components for semiconductor manufacturing equipment
The obtained sintered body was subjected to electric discharge machining to produce a member as shown in FIGS. 1 (A), (B), (C) and FIGS. 2 (A), (B), (C), (D). These were combined to produce a horizontal wafer boat as shown in FIG. FIG. 1A is a perspective view of a
[0065]
Evaluation of components for semiconductor manufacturing equipment
(Contamination)
A wafer (8 inches) was placed in this wafer boat, and an oxide film was formed on the surface of the wafer in a diffusion furnace at 1050 ° C. When the number of iron atoms within 1 μm from the surface in the oxide film was confirmed, 3.0 × 1012atoms / (1 μm × 1 cm2)Met. This indicates that the wafers are hardly contaminated, that is, the contamination of the wafer boat is negligibly small.
[0066]
(durability)
The obtained member was inserted into a diffusion furnace, heated to 1250 ° C. at a rate of 20 ° C./min in the presence of air, held at 1250 ° C. for 30 minutes, and then cooled to 800 ° C. at 15 ° C./min. The temperature raising and cooling cycle was repeated 10 times. Then, when the occurrence state of cracks, pinholes, etc. was visually observed on the surface of the member, occurrence of cracks, pinholes, etc. on the surface was not observed, and surface deterioration due to repeated heating and cooling was not seen. .
[0067]
(Solvent resistance)
After the weight of the obtained member was measured, it was washed 30 times with hydrofluoric acid, and the weight after washing was measured to determine the weight reduction. No decrease in weight was observed before and after washing, indicating that the solvent resistance was excellent.
[0068]
(Example 2)
Production of sintered body
8.5 g of silicon carbide raw material powder obtained in the same manner as in Example 1 was filled, pressed into the mold performed in Example 1, and pressed directly into a graphite mold without performing the step of obtaining a molded body. The powder was filled and hot pressed under the same conditions as in Example 1. As the hot press apparatus, the same one as in Example 1 was used.
(Hot press conditions)
10-Five-10-FourUnder a torr vacuum condition, the temperature was raised from room temperature to 700 ° C. over 8 hours and held at that temperature for 1 hour. (First temperature raising step)
Under vacuum conditions, the temperature was raised from 700 ° C. to 1200 ° C. over 3 hours, further raised from 1200 ° C. to 1500 ° C. over 3 hours, and maintained at that temperature for 4 hours. (Second temperature raising step)
500 kgf / cm2Then, the temperature was increased from 1500 ° C. to 2200 ° C. in 4 hours under an argon atmosphere, and the temperature was maintained for 1 hour. (Hot press process)
The density of the obtained sintered body is 3.05 g / cm.ThreeVickers hardness is 2500kgf / mm2The electrical resistivity was 0.03 Ω · cm.
[0069]
Fabrication and evaluation of semiconductor manufacturing equipment components
Using the obtained sintered body, a member for a semiconductor manufacturing apparatus (wafer boat) was produced in the same manner as in Example 1 and evaluated in the same manner as in Example 1. As a result, the evaluation result of the contamination was 8 .3x1012atoms / (1 μm × cm2The contamination of the wafer boat was found to be negligibly small. Further, it was confirmed that the durability and solvent resistance were excellent as in Example 1.
[0070]
(Comparative Example 1)
After mixing 85% by weight of commercially available silicon carbide powder and 15% by weight of carbon powder to form the same member as in Example 1, it was placed in a calcining furnace and heated to 900 ° C. in a nitrogen gas atmosphere to be temporarily sintered. Got the body. Next, this was set in a sintering furnace, heated to 1550 ° C. and impregnated with metallic silicon, and sintering was completed. The sintered body thus obtained was cast and molded to obtain a wafer boat.
[0071]
The density of the obtained sintered body is 3.02 g / cm.Three, Vickers hardness is 2000kgf / mm2The electrical resistivity is 1.0 × 10-3It was Ω · cm.
[0072]
Evaluation of components for semiconductor manufacturing equipment
When the obtained semiconductor manufacturing apparatus member (wafer boat) was evaluated in the same manner as in Example 1, the contamination evaluation result was 1.1 × 10.16atoms / (1 μm × cm2It was found that the contamination was remarkable. As for durability, cracks occurred in the joint at the eighth temperature rise, and regarding solvent resistance, a 15% weight reduction was observed, and defects were observed in the wafer insertion part, resulting in durability and solvent resistance. Both were insufficient.
[0073]
(Comparative Example 2)
A silicon carbide film was formed on the surface of the wafer boat obtained by casting in Comparative Example 1 at 1000 ° C. using methyltrichlorosilane as a source gas by a CVD process. The thickness of the coating was 10 to 100 μm.
[0074]
Evaluation of components for semiconductor manufacturing equipment
The obtained semiconductor manufacturing apparatus member (wafer boat) was evaluated in the same manner as in Example 1. As a result, the contamination evaluation result was 4.6 × 10 6.12atoms / (1 μm × cm2) And the contamination was found to be negligibly small. As for durability, cracks were observed on the surface when the temperature was increased for the seventh time, and cracks were generated at the joint portion for the eighth time, resulting in insufficient durability. Regarding solvent resistance, no weight loss was observed even after washing with hydrofluoric acid, indicating that the solvent resistance was excellent.
[0075]
As is clear from the above-described examples and comparative examples, the semiconductor manufacturing apparatus members of Examples 1 and 2 obtained by the method of the present invention can be easily manufactured by combining parts by electric discharge machining and grinding. As a result, it was found that the durability and solvent resistance were excellent, and the contamination was negligibly small. On the other hand, the semiconductor manufacturing apparatus member of Comparative Example 1 obtained by the conventional method was insufficient in durability and solvent resistance, and the contamination was remarkable. In addition, the semiconductor manufacturing apparatus member of Comparative Example 2 in which a coating film was formed on the surface by CVD treatment was excellent in contamination and solvent resistance, but it was complicated to manufacture and was durable due to film strength problems. I found that there was a problem.
[0076]
Thus, since the member for a semiconductor manufacturing apparatus of the present invention exhibits excellent characteristics as an assembly-type member, the sintered body can meet the demand for a large-sized member accompanying the recent increase in size for a semiconductor manufacturing apparatus. It also shows the advantage that the manufacturing apparatus can be handled without increasing the size.
[0077]
【The invention's effect】
The semiconductor manufacturing apparatus member of the present invention is made of a high-quality silicon carbide sintered body having high density, high purity, high conductivity, and high thermal conductivity. There was no contamination of the semiconductor due to, and it had excellent durability and solvent resistance.
[Brief description of the drawings]
1A is a side plate used in a horizontal wafer boat obtained by electric discharge machining of a silicon carbide sintered body, FIG. 1B is a receiving rod, and FIG.
2A is a bracket handle used in a horizontal wafer boat obtained by electric discharge machining of a silicon carbide sintered body, and FIG. 2B is a side view of the bracket attached to the side plate shown in FIG. . (C) is a nut, and (D) is a side view of the bolt.
FIG. 3 is a schematic perspective view of a horizontal wafer boat of Example 1. FIG.
Claims (8)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15966898A JP4390872B2 (en) | 1997-06-20 | 1998-06-08 | Semiconductor manufacturing apparatus member and method for manufacturing semiconductor manufacturing apparatus member |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16478397 | 1997-06-20 | ||
| JP9-164783 | 1997-06-20 | ||
| JP15966898A JP4390872B2 (en) | 1997-06-20 | 1998-06-08 | Semiconductor manufacturing apparatus member and method for manufacturing semiconductor manufacturing apparatus member |
Publications (2)
| Publication Number | Publication Date |
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| JPH1171181A JPH1171181A (en) | 1999-03-16 |
| JP4390872B2 true JP4390872B2 (en) | 2009-12-24 |
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| JP15966898A Expired - Lifetime JP4390872B2 (en) | 1997-06-20 | 1998-06-08 | Semiconductor manufacturing apparatus member and method for manufacturing semiconductor manufacturing apparatus member |
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Families Citing this family (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001076902A (en) * | 1999-09-03 | 2001-03-23 | Sumitomo Osaka Cement Co Ltd | Snubber resistor and manufacture thereof |
| JP4925152B2 (en) * | 2000-01-21 | 2012-04-25 | イビデン株式会社 | Semiconductor manufacturing equipment parts and semiconductor manufacturing equipment |
| JP3980262B2 (en) * | 2000-10-31 | 2007-09-26 | 日本碍子株式会社 | SiC heat treatment jig |
| JP2002231649A (en) * | 2001-01-30 | 2002-08-16 | Tokyo Electron Ltd | Heat treatment equipment and wafer support ring |
| WO2003040059A1 (en) * | 2001-11-08 | 2003-05-15 | Bridgestone Corporation | Process for producing silicon carbide sinter jig for use in semiconductor production and silicon carbide sinter jig obtained by the process |
| US7226561B2 (en) | 2002-03-11 | 2007-06-05 | Bridgestone Corporation | Method of producing silicon carbide sintered body jig |
| JP2005219937A (en) * | 2004-02-03 | 2005-08-18 | Bridgestone Corp | Silicon carbide sintered compact containing phosphorus, silicon carbide powder to be raw material of the same, and method of manufacturing these |
| US20070089836A1 (en) * | 2005-10-24 | 2007-04-26 | Applied Materials, Inc. | Semiconductor process chamber |
| JP5519389B2 (en) * | 2010-04-23 | 2014-06-11 | 株式会社ブリヂストン | Support pin |
| CN108777252B (en) * | 2018-05-29 | 2024-06-21 | 上海科发电子产品有限公司 | A sintering mold for hybrid integrated circuit housing |
| TWI770810B (en) * | 2020-02-07 | 2022-07-11 | 日商京瓷股份有限公司 | Wafer boat |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
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| JPS61261267A (en) * | 1985-05-15 | 1986-11-19 | 株式会社日立製作所 | Manufacture of silicon carbide sintered body |
| JPS63123867A (en) * | 1986-11-10 | 1988-05-27 | 三井東圧化学株式会社 | Manufacture of silicon carbide formed body for sintering |
| JPH0788255B2 (en) * | 1987-09-30 | 1995-09-27 | 新日本製鐵株式会社 | Silicon carbide sintered body and method for producing the same |
| JP2726693B2 (en) * | 1989-01-30 | 1998-03-11 | 弌倫 木島 | High thermal conductive silicon carbide sintered body and method for producing the same |
| JP3174622B2 (en) * | 1992-06-08 | 2001-06-11 | 株式会社ブリヂストン | Method for producing high-purity β-type silicon carbide sintered body |
| JPH06128036A (en) * | 1992-10-16 | 1994-05-10 | Shin Etsu Chem Co Ltd | Silicon carbide material for semiconductors |
| JP3483920B2 (en) * | 1993-12-07 | 2004-01-06 | 株式会社ブリヂストン | Method for producing high-purity β-type silicon carbide sintered body for semiconductor production equipment |
| JP3934695B2 (en) * | 1995-05-31 | 2007-06-20 | 株式会社ブリヂストン | Method for producing high-purity silicon carbide powder for producing silicon carbide single crystal |
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1998
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