JPS5819637B2 - Silicon doped gallium tank - Google Patents
Silicon doped gallium tankInfo
- Publication number
- JPS5819637B2 JPS5819637B2 JP9099174A JP9099174A JPS5819637B2 JP S5819637 B2 JPS5819637 B2 JP S5819637B2 JP 9099174 A JP9099174 A JP 9099174A JP 9099174 A JP9099174 A JP 9099174A JP S5819637 B2 JPS5819637 B2 JP S5819637B2
- Authority
- JP
- Japan
- Prior art keywords
- heating section
- dislocation density
- temperature heating
- crystal
- gallium arsenide
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 title claims description 18
- 229910052710 silicon Inorganic materials 0.000 title claims description 18
- 239000010703 silicon Substances 0.000 title claims description 18
- GYHNNYVSQQEPJS-UHFFFAOYSA-N Gallium Chemical compound [Ga] GYHNNYVSQQEPJS-UHFFFAOYSA-N 0.000 title description 2
- 229910052733 gallium Inorganic materials 0.000 title description 2
- 239000013078 crystal Substances 0.000 claims description 67
- JBRZTFJDHDCESZ-UHFFFAOYSA-N AsGa Chemical compound [As]#[Ga] JBRZTFJDHDCESZ-UHFFFAOYSA-N 0.000 claims description 37
- 229910001218 Gallium arsenide Inorganic materials 0.000 claims description 37
- 238000010438 heat treatment Methods 0.000 claims description 32
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 19
- 229910052785 arsenic Inorganic materials 0.000 claims description 18
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 claims description 18
- 238000000034 method Methods 0.000 claims description 17
- 239000010453 quartz Substances 0.000 claims description 16
- 238000004519 manufacturing process Methods 0.000 claims description 9
- 239000011148 porous material Substances 0.000 claims description 6
- 238000009792 diffusion process Methods 0.000 claims description 3
- AJNVQOSZGJRYEI-UHFFFAOYSA-N digallium;oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Ga+3].[Ga+3] AJNVQOSZGJRYEI-UHFFFAOYSA-N 0.000 claims description 3
- 229910001195 gallium oxide Inorganic materials 0.000 claims description 3
- 229910052814 silicon oxide Inorganic materials 0.000 claims description 3
- KWLSQQRRSAWBOQ-UHFFFAOYSA-N dipotassioarsanylpotassium Chemical compound [K][As]([K])[K] KWLSQQRRSAWBOQ-UHFFFAOYSA-N 0.000 claims description 2
- 238000003860 storage Methods 0.000 claims description 2
- 238000010586 diagram Methods 0.000 description 11
- LIVNPJMFVYWSIS-UHFFFAOYSA-N silicon monoxide Chemical compound [Si-]#[O+] LIVNPJMFVYWSIS-UHFFFAOYSA-N 0.000 description 10
- 230000000694 effects Effects 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- 230000007423 decrease Effects 0.000 description 4
- 238000009826 distribution Methods 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 238000007711 solidification Methods 0.000 description 3
- 230000008023 solidification Effects 0.000 description 3
- 238000009736 wetting Methods 0.000 description 3
- HJTAZXHBEBIQQX-UHFFFAOYSA-N 1,5-bis(chloromethyl)naphthalene Chemical compound C1=CC=C2C(CCl)=CC=CC2=C1CCl HJTAZXHBEBIQQX-UHFFFAOYSA-N 0.000 description 2
- GOLCXWYRSKYTSP-UHFFFAOYSA-N arsenic trioxide Inorganic materials O1[As]2O[As]1O2 GOLCXWYRSKYTSP-UHFFFAOYSA-N 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 206010011732 Cyst Diseases 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 208000031513 cyst Diseases 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000005518 electrochemistry Effects 0.000 description 1
- 238000005530 etching Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000002932 luster Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 235000011149 sulphuric acid Nutrition 0.000 description 1
Landscapes
- Crystals, And After-Treatments Of Crystals (AREA)
- Liquid Deposition Of Substances Of Which Semiconductor Devices Are Composed (AREA)
Description
【発明の詳細な説明】
本発明はボート成長法によるひ化ガリウム単結晶の製造
方法に関するもので、シリコンを高濃度ドープでき、か
つ転位密度の小さい単結晶を製造することができる有用
な方法を提供するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a gallium arsenide single crystal using a boat growth method, and is a useful method capable of producing a single crystal that can be highly doped with silicon and has a low dislocation density. This is what we provide.
先ずひ化ガリウムの従来の製造方法の代表的な例を挙げ
、その問題点を述べる。First, we will give a typical example of the conventional manufacturing method of gallium arsenide and discuss its problems.
第1図はいわゆる二湿度形水平式ブリッジマン法の結晶
成長炉の構成図、炉内温度分布図および結晶成長用容器
を示す図である。FIG. 1 is a diagram showing the configuration of a so-called dual-humidity horizontal Bridgman method crystal growth furnace, a temperature distribution diagram in the furnace, and a crystal growth container.
横軸はこの成長炉の内部の位置を示し、縦軸は炉内湿度
を示している。The horizontal axis shows the position inside the growth furnace, and the vertical axis shows the humidity inside the furnace.
温度T1.T3はそれぞれT1=1250’−1275
℃。Temperature T1. T3 is T1=1250'-1275 respectively
℃.
T3−605°−620℃である。T3-605°-620°C.
又Tmはひ化ガリウムの融点でおおよそTm=1238
℃ である。Also, Tm is the melting point of gallium arsenide, approximately Tm = 1238
It is ℃.
第1図において、1はひ化ガリウムの融液2を保持する
高純度石英製ボート6を収容した高純度石英製容器で、
3は成長した少量のひ化ガリウム単結晶又は高純度ひ化
ガリウムの種結晶、4はひ素(As)の蒸気圧を制御す
るための過剰ひ素である。In FIG. 1, 1 is a high-purity quartz container containing a high-purity quartz boat 6 that holds a gallium arsenide melt 2;
3 is a small amount of grown gallium arsenide single crystal or a high purity gallium arsenide seed crystal, and 4 is excess arsenic for controlling the vapor pressure of arsenic (As).
7,9は高温加熱部Aと低湿加熱部Cに分けられた電気
炉を模式的に示したものである。7 and 9 schematically show an electric furnace divided into a high temperature heating section A and a low humidity heating section C.
容器1は予め10 ” mHg以下の高真空(こ封入
されるが、容器1を炉内【こ挿入後定常状態に達すると
過剰のひ素4によって容器内にはひ素の蒸気が充満し約
1気圧に保たれる。The container 1 is sealed in advance under a high vacuum of 10" mHg or less, but when the container 1 reaches a steady state after being inserted into the furnace, the excess arsenic 4 fills the container with arsenic vapor, creating a pressure of approximately 1 atm. is maintained.
この状態で電気炉7゜9を容器1(こ対して相対的に左
に向って5〜50mm/時の速度で移動させることによ
ってひ化カリウムの単結晶化ができる。In this state, the electric furnace 7°9 is moved to the left relative to the container 1 at a speed of 5 to 50 mm/hour, thereby single crystallizing potassium arsenide.
ここで高温加熱部(温度T1)と低温加熱部(温度T3
)間の温度勾配Gは10°〜50′C/Cmと太きい。Here, a high temperature heating section (temperature T1) and a low temperature heating section (temperature T3)
) is as large as 10° to 50'C/Cm.
そのため凝固後の冷却過程において、結晶内の長手方向
に大きな畠度差が生ずる。Therefore, during the cooling process after solidification, a large difference in graininess occurs in the longitudinal direction within the crystal.
温度差が生ずると熱膨張の差(格子定数の差)により歪
が生じ、この歪量が結晶の弾性限を越えると塑性変形し
、転位が発生又は増殖される。When a temperature difference occurs, strain occurs due to the difference in thermal expansion (difference in lattice constant), and when this amount of strain exceeds the elastic limit of the crystal, plastic deformation occurs and dislocations are generated or multiplied.
特にひ化ガリウムの融点直下では塑性変形を起しやすい
ので、融点直下の部分での温度勾配Gが大きいこの方法
では、転位密度が大きくなり小断面積(5cm以下)の
結晶でも通常2X 103cm −2以上となってしま
う。In particular, plastic deformation is likely to occur just below the melting point of gallium arsenide, so in this method where the temperature gradient G is large just below the melting point, the dislocation density increases and even crystals with a small cross-sectional area (5 cm or less) are usually 2X 103 cm - It ends up being 2 or more.
断面積が10crA以上では1×104crn−2を越
えてしまう。If the cross-sectional area is 10 crA or more, it exceeds 1×10 4 crn-2.
又ひ化ガリウム融液(ドープされたシリコンも含む)と
石英ボートとは次のような反応をひき起すことが知られ
ている。It is also known that the following reaction occurs between gallium arsenide melt (including doped silicon) and quartz boats.
4Ga(Ga As融液中)−1−8iO□(固体)=
2Ga20(気体) +S i ・
・・・・・・・・ (1)Si+5iO3(固体)=2
SiO(気体)・・・・・・・・・ (2)3Ga20
(気体)+A s 4(気体)−〇a203(固体)+
4GaAs(固体) ・・・・・・・・
・ (3)SiO(気体)=SiO(固体) ・・
・・・・・・・ (4)高濃度のシリコンをドープする
場合には主として(2)式と(4)式が反応に寄与して
くる。4Ga (in GaAs melt) -1-8iO□ (solid) =
2Ga20 (gas) +S i ・
・・・・・・・・・ (1) Si + 5iO3 (solid) = 2
SiO (gas)・・・・・・・・・(2)3Ga20
(Gas) +A s 4 (Gas) -〇a203 (Solid) +
4GaAs (solid) ・・・・・・・・・
・ (3) SiO (gas) = SiO (solid) ・・
(4) When doping silicon at a high concentration, equations (2) and (4) mainly contribute to the reaction.
最初(2)式の反応が右側に進み一酸化シリコン(Si
n)の蒸気を発生させる。At first, the reaction of equation (2) proceeds to the right and silicon monoxide (Si
n) generating steam;
この蒸気は高温加熱部から低温加熱部へ拡散して行って
(4)式の反応により凝縮し、psio が低下する
。This vapor diffuses from the high-temperature heating section to the low-temperature heating section and is condensed by the reaction of equation (4), resulting in a decrease in psio.
こ\で(1)式および(2)式の平衡定数を各々に1(
T1)、に2(T1)とするとCPGa2o 、Ps
io ] 2=に1 (TI) −に2(TI )とな
る。Here, the equilibrium constants of equations (1) and (2) are each set to 1 (
T1), 2(T1), CPGa2o, Ps
io ] 2 = 1 (TI) - 2 (TI ).
但し、Gaの活量とSiの活量はそれぞれに1(T1)
、に2(T1)に含めた(、Psioが低下するとPG
a20が増さねばならないので、(1)式が右側へ進行
することになり、融液と石英ボートとが反応する、いわ
ゆる「ぬれ」が進行する。However, the activity of Ga and the activity of Si are each 1 (T1)
, included in 2 (T1) (, When Psio decreases, PG
Since a20 must increase, equation (1) will proceed to the right, and so-called "wetting" in which the melt and the quartz boat react will proceed.
その結果良質な単結晶は得られない。As a result, a high quality single crystal cannot be obtained.
本発明は以上の難点を解消し、成長したひ化ガリウム単
結晶の残留シリコン濃度を広い範囲にわたって制御でき
、特に約5 X 1017〜5X101f′cm−3ま
での範囲で高濃度ドーピング制御でき、かつ転位密度を
約2×103Crrl−2以下にすることを可能とする
ひ化ガリウム単結晶の製造方法を提供するものである。The present invention solves the above-mentioned difficulties, makes it possible to control the residual silicon concentration in the grown gallium arsenide single crystal over a wide range, and in particular, to control high concentration doping in the range of about 5 x 1017 to 5 x 101 f'cm-3, and The present invention provides a method for producing a gallium arsenide single crystal that allows the dislocation density to be approximately 2 x 103 Crrl-2 or less.
本発明の第1の発明は上記二基i形水平式ブリッジマン
法の改良方法である所の本出願人が先に提案した三温度
形水平式ブリッジマン法(特公昭48−35861号参
照)すなわち、
(a)結晶成長炉は、約1245°−1270℃の高温
加熱部と約1080’−1220℃の中間温度加熱部と
ひ素の蒸気圧がほぼ1気圧(こなる程度の加熱を行う低
湿加熱部を具備し、
(b) ひ化ガリウムを収容するボートとして石英ボ
ートを用い、上記石英ボートを収容する密封容器は、該
ボートを収容する室とひ素を収容する室とそれらの室の
間に設けられたひ素の蒸気の流通は認められるが、ガリ
ウムの酸化物やシリコンの酸化物の蒸気の拡散を阻害す
る細孔部とより成り、
(c)上記細孔部の上記ひ素収容室との境界線と上記中
間湿度加熱部の最低湿度位置との距離(L2)を、上記
ボートの全長(Ll)Iこほぼ等しくするか又はより長
く構成して製造する方法において、上記中間湿度加熱部
の温度を特に11000−1200’Cとし、上記高温
加熱部と中間温度加熱部との間の温度勾配G(第2図)
を約2〜10C/cmとし、かつ結晶の成長速度を約2
〜10rIrIrL/時とすること(こより、転位密度
を約2X10”Cr11−2以下にすることを特徴とす
るシリコンがドープされた転位密度の小さいひ化ガリウ
ム単結晶の製造方法である。The first invention of the present invention is an improved method of the above-mentioned two-temperature horizontal Bridgman method, which was previously proposed by the present applicant (see Japanese Patent Publication No. 35861/1986). (a) The crystal growth furnace consists of a high-temperature heating section of about 1245°-1270°C, an intermediate-temperature heating section of about 1080'-1220°C, and a low-humidity heating section where the vapor pressure of arsenic is approximately 1 atm (approximately 1 atm). (b) A quartz boat is used as the boat for accommodating the gallium arsenide, and the sealed container for accommodating the quartz boat is located between a chamber for accommodating the boat, a chamber for accommodating the arsenic, and those chambers. Although it is recognized that the arsenic vapor can flow through the pores provided in the pores that inhibit the diffusion of gallium oxide and silicon oxide vapors, (c) the arsenic storage chamber in the pores and the In the manufacturing method, the distance (L2) between the boundary line of In particular, the temperature is 11000-1200'C, and the temperature gradient G between the high temperature heating section and the intermediate temperature heating section (Fig.
is about 2 to 10 C/cm, and the crystal growth rate is about 2
~10 rIrIrL/hour (thereby, the dislocation density is about 2X10''Cr11-2 or less).This is a method for producing a silicon-doped gallium arsenide single crystal with a low dislocation density.
本発明によれば、単結晶の断面積が5c4(直径35r
ItM)以上において、シリコンがドープされた転位密
度の小さいひ化ガリウム単結晶を製造しうる0
上述のように従来の方法では断面積5c4(直径35m
の半円)以下の小断面G a A s 結晶でも転位
密度は2×1O−3Crrl−2以上、又断面積が10
cm(直径50閣の半円)以上では1×104cm−2
以上の転位密度のGaAs結晶しか得られていない。According to the present invention, the cross-sectional area of the single crystal is 5c4 (diameter 35r
ItM), it is possible to produce a silicon-doped gallium arsenide single crystal with a low dislocation density.
Even if the crystal has a small cross-section of less than 2×1O-3Crrl-2, and the cross-sectional area is 10
cm (diameter of 50 semicircles) or more: 1 x 104 cm-2
Only GaAs crystals with dislocation densities above the above have been obtained.
後述のよう【こGaAs結晶は一般に〈111>方向に
成長させられるので、断面積5c77fは(100)断
面積で約9 cli、又断面積1octAは(100)
Ii部面積約15c77fに相当する。As will be explained later, [Since GaAs crystals are generally grown in the <111> direction, the cross-sectional area 5c77f is a (100) cross-sectional area of about 9 cli, and the cross-sectional area 1 octA is a (100)
The area of part Ii corresponds to approximately 15c77f.
又、T、S、 Plaskett et al、T
he Eff−ect of Growth 0r
ientation onthe Crystal
Perfection of Ho−rizon
tal Bridgman GrownGaAs″
。Also, T.S., Plaskett et al., T.S.
he Effect of Growth 0r
ientation on the Crystal
Perfection of Ho-rizon
tal Bridgman GrownGaAs''
.
Journal of Electrochemic
alSoci ety 、Jan、(1971)PP、
115〜l 17、(こよれば、直径約15mの半円
(断面積0.9 crrt )の小結晶でも<013>
方向(こ成長した結晶のみが転位密度約1000Cr/
に一2以下になったという。Journal of Electrochemistry
alSoci ity, Jan, (1971) PP,
115~l 17, (according to this, even a small crystal of a semicircle with a diameter of about 15 m (cross-sectional area 0.9 crrt) <013>
direction (only this grown crystal has a dislocation density of about 1000Cr/
It is said that the number of children decreased to less than 12.
これに対し、本発明【こよれば断面積5c7n−2(直
径35mmの半円)以上の大面積G aA s結晶でも
再現性よく転位密度が2X 10” cm−2以下のも
のが得られるのである。In contrast, according to the present invention, a large-area GaAs crystal with a cross-sectional area of 5c7n-2 (a semicircle with a diameter of 35 mm) or more can have a dislocation density of 2X 10'' cm-2 or less with good reproducibility. be.
又本発明においては、単結晶が成長し終って単結晶全体
が上記中間温度加熱部に位置せしめられた後、結晶成長
炉を停止し、該炉を降温させて徐冷することが適尚であ
る。Further, in the present invention, after the single crystal has finished growing and the entire single crystal has been placed in the intermediate temperature heating section, it is appropriate to stop the crystal growth furnace and lower the temperature of the furnace to slowly cool it. be.
次に本発明の第2の発明は、第1の発明による方法にお
いて、単結晶中のシリコン濃度を特に高濃度、すナワチ
約5×1017CrrL−3〜5×1018Crrl−
3の範囲に制御することを特徴としている。Next, the second invention of the present invention provides a method according to the first invention in which the silicon concentration in the single crystal is set to a particularly high concentration, approximately 5×10 17 CrrL−3 to 5×10 18 Crrl−
It is characterized by being controlled within a range of 3.
一般的には不純物を高濃度ドープすると転位密度は急激
に増加する傾向があるにも拘わらず、本発明の方法によ
れば、逆にむしろ転位密度は減少する傾向がある。Generally speaking, when impurities are doped at a high concentration, the dislocation density tends to increase rapidly, but according to the method of the present invention, on the contrary, the dislocation density tends to decrease.
以下、本発明を実施例により詳細に説明する。Hereinafter, the present invention will be explained in detail with reference to Examples.
実施例 1
第2図は本発明の実施例によりひ化ガリウム単結晶を製
造する場合の三湿度形水平式ブリッジ77法の結晶成長
炉の構成図、炉内湿度分布図および結晶成長用容器を示
す図である。Example 1 FIG. 2 shows a configuration diagram of a crystal growth furnace using a three-humidity type horizontal bridge 77 method, a humidity distribution diagram in the furnace, and a crystal growth container for manufacturing gallium arsenide single crystals according to an example of the present invention. FIG.
横軸はこの成長炉の内部の位置を示し、縦軸は炉内温度
を示している。The horizontal axis shows the position inside the growth furnace, and the vertical axis shows the temperature inside the furnace.
温度T1.T2.T3 はそれぞれT1=1245°〜
1270℃、T2=1100’−1,200℃、T3=
605°−620℃、特に610℃である。Temperature T1. T2. T3 is T1=1245°~
1270℃, T2=1100'-1,200℃, T3=
605°-620°C, especially 610°C.
但し過剰ひ素4の量が極めて少なければT3はT2 と
ほぼ同じ位まで加熱することができるので、Crは省略
することも可能である。However, if the amount of excess arsenic 4 is extremely small, T3 can be heated to almost the same level as T2, so Cr can be omitted.
第2図において、1はひ化ガリウムの融液2を保持する
高純度石英製ボートOを収容した高純度石英製容器で、
3は成長した少量のひ化ガリウム単結晶および高純度又
はシリコンをドープしたひ化ガリウムの種結晶、4はひ
素(As )の蒸気圧を制御するための過剰ひ素である
。In FIG. 2, 1 is a high-purity quartz container containing a high-purity quartz boat O that holds a gallium arsenide melt 2;
3 is a small amount of grown gallium arsenide single crystal and a high purity or silicon-doped gallium arsenide seed crystal; 4 is excess arsenic for controlling the vapor pressure of arsenic (As).
石英ボート6は最も簡単な形のものを示しであるが、種
結晶を用いて、いわゆるシーディングを行なう場合には
、1鈴木隆、「化合物半導体の製造と問題点ハ日本エコ
ノミストセンター主催講演会資料、10月20日〜10
月21日(1970)PP、1〜16に発表されて以来
採用されるようになった、いわゆる棚つきボートの棚上
に細い種結晶を置くこと、ができる。The quartz boat 6 is shown in its simplest form, but when so-called seeding is performed using a seed crystal, 1 Takashi Suzuki, ``Manufacturing of compound semiconductors and problems'', lecture sponsored by the Japan Economist Center. Materials, October 20th-10th
It is possible to place a thin seed crystal on the shelf of a so-called shelf boat, which has been adopted since it was published in May 21, 1970, PP, 1-16.
5は細孔部で、ひ素の蒸気の流通は認めるがガリウムの
酸化物およびシリコンの酸化物の蒸気の拡散を阻害する
役目をする。Reference numeral 5 denotes a pore, which allows the flow of arsenic vapor but serves to inhibit the diffusion of gallium oxide and silicon oxide vapor.
?、8.9は各々高温加熱部A1中間湛度加熱部Bおよ
び低温加熱部;Cに分けられた電気炉を模式的に示して
いる。? , 8.9 schematically show an electric furnace divided into a high temperature heating section A, an intermediate heating section B, and a low temperature heating section C.
又Gは高濡加熱部Aと中間温度加熱部Bとの間の湿度勾
配で、約2〜10℃1cmであった。Further, G is the humidity gradient between the high wetness heating section A and the intermediate temperature heating section B, which was approximately 2 to 10° C. 1 cm.
ボート6内には最初ガリウム(純度99.9999%)
の約500grと高純度Siの200mgrが収容され
、石英容器1内の低湿部にはひ素(純度99.9999
%)の約550grと高純度三酸化ひ素(AS203)
の50mgr が収容された。Inside boat 6, there is initially gallium (99.9999% purity).
Approximately 500gr of Si and 200mgr of high purity Si are stored, and arsenic (purity 99.9999
%) of about 550gr and high purity arsenic trioxide (AS203)
of 50mgr was accommodated.
かくしてボート6内に生成された溶融ひ化ガリウムと、
ボート6の長手方向に(111)A s方向を有するシ
リコンドープひ化ガリウム種結晶とを接続した後、電気
炉I、8゜9を石英容器1に対して相対的に左に向って
2〜10y+tm/時の速度で移動させた。The molten gallium arsenide thus generated in the boat 6,
After connecting the silicon-doped gallium arsenide seed crystal having the (111)A s direction in the longitudinal direction of the boat 6, the electric furnace I, 8°9 is turned to the left relative to the quartz container 1, and the It was moved at a speed of 10y+tm/hour.
溶融ひ化ガリウム結晶が全部凝固した後、30〜b 例えば約り0℃/時の速度で冷却した。After all the molten gallium arsenide crystals have solidified, 30~b For example, it was cooled at a rate of about 0° C./hour.
この様にして断面積6〜10c4(100)断面積にし
て9〜15cm、長さ約30〜40cmもの大面積かつ
長尺のひ化ガリウム単結晶が得られ、この結晶のボート
側の光沢は非常によく、ボートと融液との「ぬれ」の痕
跡をも認めることができなかった。In this way, a large and long gallium arsenide single crystal with a cross-sectional area of 6-10c4 (100 cm), a cross-sectional area of 9-15 cm, and a length of about 30-40 cm was obtained, and the luster on the boat side of this crystal was Very well, no trace of "wetting" between the boat and the melt could be observed.
尚結晶の全長(こわたって良質の結晶とするには、第2
図でL2≧L1とすることが必要であった。The total length of the crystal (to obtain a high quality crystal over the entire length, the second
In the figure, it was necessary to set L2≧L1.
又温度勾配G(2〜10″C/cm)と結晶の成長速度
R(2〜10B/時)の比、いわゆるG/Rは10℃、
時/cystより大きいことが望まし(z)□ G51
0℃10n、R510m+++7時、G/R≦10℃、
時/crtlの場合には、断面5cd以上の低転位密度
G aA s結晶は得られ難い。Also, the ratio of the temperature gradient G (2 to 10"C/cm) to the crystal growth rate R (2 to 10B/hour), so-called G/R, is 10C,
It is desirable that it be larger than time/cyst (z) □ G51
0℃10n, R510m+++7 o'clock, G/R≦10℃,
In the case of 1/crtl, it is difficult to obtain a low dislocation density GaAs crystal with a cross section of 5 cd or more.
この結晶の長手方向に垂直7.C(111)Ga面を3
H2SO4:lH2O□:lH2Oを用いて室湿で約1
0分間エツチングしてエッチピット密度を測定した結果
、転位密度が結晶の先端部で約500cm−2、後端部
で約5ooCrrl−である事が分った。7. Perpendicular to the longitudinal direction of this crystal. C(111)Ga plane 3
About 1 at room humidity using H2SO4:lH2O□:lH2O
As a result of measuring the etch pit density after etching for 0 minutes, it was found that the dislocation density was approximately 500 cm@-2 at the leading end of the crystal and approximately 5oo Crrl@- at the trailing end.
又この結晶の(100)面を溶融KOHで約8分間エツ
チングしてエッチピット密度を測定した結果、はぼ同じ
結果が得られた。Furthermore, when the (100) plane of this crystal was etched with molten KOH for about 8 minutes and the etch pit density was measured, almost the same results were obtained.
さらにこの結晶をファンデルパラ法によってホール係数
を測定した結果、295°にでのキャリヤー濃度が先端
部で2X1018m−3、後端部で5×1018Crr
l−3である事が分、つた。Furthermore, as a result of measuring the Hall coefficient of this crystal by the van der Para method, the carrier concentration at 295° was 2 x 1018 m-3 at the tip and 5 x 1018 Crr at the rear end.
I knew it was l-3.
実施例1の効果は次のように説明される。The effects of Example 1 are explained as follows.
■ 高温加熱部と低湿加熱部間の温度勾配Gが2〜b
凝固後の冷却過程において結晶内の長手方向の温度差が
小さく、又成長速度が2〜10mm/時と小さいため、
結晶内の半径方向の温度差も小さくなるので、熱歪が少
なく、転位が発生又は増殖しない。■ The temperature gradient G between the high-temperature heating section and the low-humidity heating section is 2-b.During the cooling process after solidification, the temperature difference in the longitudinal direction within the crystal is small, and the growth rate is small at 2-10 mm/hour.
Since the temperature difference in the radial direction within the crystal is also reduced, thermal strain is small and dislocations do not occur or multiply.
■ 凝固完了後の冷却速度が約り0℃/時と小さいため
、結晶の内、外部の湿度差が小さくなるので、熱歪が少
すく、転位が発生又は増殖しない。(2) Since the cooling rate after completion of solidification is as low as approximately 0° C./hour, the difference in humidity between the inside and outside of the crystal is small, so thermal distortion is small and dislocations do not occur or multiply.
■ ひ化ガリウム融液中のシリコンと石英ボートとの反
応(前述の(2成)によって発生した一酸化シリコンの
蒸気は中間温度加熱部の温度T2が1100°−120
0℃と高いため凝縮しない。■ The silicon monoxide vapor generated by the reaction between the silicon in the gallium arsenide melt and the quartz boat (the above-mentioned (2)) has a temperature T2 of the intermediate temperature heating section of 1100°-120°.
Because it is as high as 0°C, it does not condense.
すなわち(4)式は右側へ進行しないためPsioの低
下は起らない。In other words, since equation (4) does not proceed to the right, Psio does not decrease.
その結果(1)式は右側へ進行しないので「ぬれ」は起
らないと考えられる。As a result, equation (1) does not proceed to the right, so it is considered that "wetting" does not occur.
この中間温度加熱帯の役割を示したのが第3図である。FIG. 3 shows the role of this intermediate temperature heating zone.
第3図は本発明によってひ化ガリウム中の残留シリコン
の濃度をコントロールできる範囲を説明する図で、横軸
は中間湿度加熱部の温度T2の逆数を示し、左の縦軸は
ひ化ガリウム融液中のシリコンの活量(asi)を示し
、右の縦軸は得られた結晶中の残留シリコンの濃度Ns
i を示している。FIG. 3 is a diagram explaining the range in which the concentration of residual silicon in gallium arsenide can be controlled by the present invention. The activity (asi) of silicon in the liquid is shown, and the vertical axis on the right is the concentration Ns of residual silicon in the obtained crystal.
i is shown.
図の直線10−aは(4)式の直線1o−bは(3)式
の平衡関係を示している。The straight line 10-a in the figure represents the equation (4), and the straight line 1o-b represents the equilibrium relationship of the equation (3).
残留シリコン濃度が制御される【こはT2は1045℃
〈T2〈m、p、の範囲であることが必要であるが、実
験的に良質な単結晶を得るには、1050℃〈T2〈1
200℃である事が必要であった。Residual silicon concentration is controlled (T2 is 1045℃)
It is necessary that 〈T2〈m, p is within the range of 1050℃〈T2〈1
The temperature needed to be 200°C.
特に本発明により結晶中の残留シリコン濃度Nsiが5
X 10”cm ” (Nsl〈5×1018Crr
l−3である良質な単結晶を得るには、T2 の温度が
1100℃〈T2〈1200℃でなければならないこと
がわかる。In particular, according to the present invention, the residual silicon concentration Nsi in the crystal can be reduced to 5
X 10”cm” (Nsl〈5×1018Crr
It can be seen that in order to obtain a high quality single crystal of l-3, the temperature of T2 must be 1100°C<T2<1200°C.
又シリコン濃度が約1013Crrl−3〜5×101
7cm−3の範囲で制御される為には、1050℃ぐ1
<1200℃であれば充分であるが、断面積5crA以
上で転位密度が2×103Crrv2 以下になる為
(こは、やはり1100℃〈T2〈1200℃でなけれ
ばならないのである。Also, the silicon concentration is about 1013 Crrl-3 to 5×101
In order to be controlled within the range of 7cm-3, the temperature must be 1050℃1.
<1200°C is sufficient, but if the cross-sectional area is 5 crA or more, the dislocation density will be 2×103 Crrv2 or less (this also requires 1100°C<T2<1200°C).
なおシリコン濃度を約1013cm−3〜5×1018
cm−3に制御するとともにSi以椙の不純物をドープ
しても有効と考えられる。In addition, the silicon concentration is approximately 1013 cm-3 ~ 5 x 1018
It is considered to be effective to control the impurity to cm-3 and dope with an impurity other than Si.
以上詳述した如く、本発明の方法は、シリコンドープひ
化ガリウム単結晶、特にシリコン高濃度ドープひ化ガリ
ウム単結晶の製造において、結晶中の残留シリコン濃度
を制御でき、かつ転位密度を2×103Crrl−2以
下にできる方法を提供するものである。As detailed above, the method of the present invention can control the residual silicon concentration in the crystal and reduce the dislocation density by The purpose is to provide a method that can reduce the amount to 103Crrl-2 or less.
第1図はひ化ガリウム結晶を従来の方法によって製造す
る場合の結晶成長炉の構成図、炉内湿度分布図および結
晶成長用容器を示す図である。
第2図は本発明の実施例によりひ化ガリウム結晶を製造
する場合の結晶成長炉の構成図、炉内湿度分布図および
結晶成長用容器を示す図である。
第3図は本発明によってひ化ガリウム中の残留シリコ7
の濃Wをコントロールできる範囲を説明する図である。
図において1は石英製容器、2はひ化ガリウム融液、3
は結晶したひ化ガリウム又はひ化ガリウム種結晶、4は
過剰ひ素、5は細孔部、6は石英ボート、7は高温加熱
部、8は中間温度加熱部、′ 9は低温加熱部である。FIG. 1 is a diagram showing the configuration of a crystal growth furnace, a humidity distribution diagram in the furnace, and a crystal growth container in the case of producing gallium arsenide crystals by a conventional method. FIG. 2 is a diagram showing a configuration diagram of a crystal growth furnace, a humidity distribution diagram in the furnace, and a container for crystal growth when producing gallium arsenide crystals according to an embodiment of the present invention. Figure 3 shows the residual silicon 7 in gallium arsenide according to the present invention.
FIG. 3 is a diagram illustrating a range in which the darkness W of the image can be controlled. In the figure, 1 is a quartz container, 2 is a gallium arsenide melt, and 3 is a quartz container.
is crystallized gallium arsenide or gallium arsenide seed crystal, 4 is excess arsenic, 5 is pore section, 6 is quartz boat, 7 is high temperature heating section, 8 is intermediate temperature heating section, ' 9 is low temperature heating section .
Claims (1)
法、すなわち (a)結晶成長炉は、約1245°−1270℃の高温
加熱部と約1080’−1220℃の中間温度加熱部と
ひ素の蒸気圧がほぼ1気圧になる程度の加熱を行う低湿
加熱部を具備し、 (b) ひ化ガリウムを収容するボートとして石英ボ
ートを用い、上記石英ボートを収容する密封容器は、該
ボートを収容する室とひ素を収容する室とそれらの室の
間に設けられたひ素の蒸気の流通は認められるがガリウ
ムの酸化物やシリコンの酸化物の蒸気の拡散を阻害する
細孔部とより成り、 (c)上記細孔部の上記ひ素収容室との境界線と上記中
間温度加熱部の最低温度位置との距離(L2)を、上記
ボートの全長(Ll)にほぼ等しくするか又はより長く
構成して製造する方法において、上記中間温度加熱部の
湿度を特に1100℃〜1200℃とし、上記高温加熱
部と中間温度加熱部との間の温度勾配G(第2図)を約
2〜10C/cmとし、かつ結晶の成長速度を約2〜1
0閣/時とすることにより、転位密度を約2X103c
Wl−2以下にすることを特徴とするシリコンがドープ
された転位密度の小さいひ化ガリウム単結晶の製造方法
。 2、特許請求の範囲第1項記載の方法において、単結晶
中のシリコン濃度を約5×1017crrl−3〜5×
1018Crrl−3の範囲に制御することを特徴とす
るシリコンが高濃度ドープされた転位密度の小さいひ化
カリウム単結晶の製造方法。[Claims] 1. Gallium arsenide single crystal is grown using the three-temperature horizontal Bridgman method, that is, (a) the crystal growth furnace has a high-temperature heating section of about 1245°-1270°C and an intermediate heating section of about 1080°-1220°C. It is equipped with a temperature heating section and a low humidity heating section that heats the vapor pressure of arsenic to approximately 1 atmosphere, (b) a quartz boat is used as a boat for containing gallium arsenide, and a sealed container for containing the quartz boat. The chamber housing the boat, the chamber housing the arsenic, and the chambers installed between these chambers allow the flow of arsenic vapor, but there are no restrictions that prevent the diffusion of gallium oxide or silicon oxide vapor. (c) the distance (L2) between the boundary line of the pores with the arsenic storage chamber and the lowest temperature position of the intermediate temperature heating section is approximately equal to the total length (Ll) of the boat; In the manufacturing method, the humidity of the intermediate temperature heating section is set to 1100° C. to 1200° C., and the temperature gradient G between the high temperature heating section and the intermediate temperature heating section is set (FIG. 2). is about 2 to 10 C/cm, and the crystal growth rate is about 2 to 1
By setting the rate to 0 kaku/hour, the dislocation density is approximately 2×103c.
A method for producing a silicon-doped gallium arsenide single crystal having a low dislocation density, characterized in that the dislocation density is Wl-2 or less. 2. In the method according to claim 1, the silicon concentration in the single crystal is approximately 5×10 17 crrl-3 to 5×
A method for producing a potassium arsenide single crystal doped with a high concentration of silicon and having a low dislocation density, the method comprising controlling the dislocation density to a range of 1018 Crrl-3.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9099174A JPS5819637B2 (en) | 1974-08-07 | 1974-08-07 | Silicon doped gallium tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9099174A JPS5819637B2 (en) | 1974-08-07 | 1974-08-07 | Silicon doped gallium tank |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5118471A JPS5118471A (en) | 1976-02-14 |
| JPS5819637B2 true JPS5819637B2 (en) | 1983-04-19 |
Family
ID=14013969
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9099174A Expired JPS5819637B2 (en) | 1974-08-07 | 1974-08-07 | Silicon doped gallium tank |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5819637B2 (en) |
-
1974
- 1974-08-07 JP JP9099174A patent/JPS5819637B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5118471A (en) | 1976-02-14 |
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