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JPH0735318B2 - <II>-<VI> Group compound single crystal growth boat - Google Patents
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JPH0735318B2 - <II>-<VI> Group compound single crystal growth boat - Google Patents

<II>-<VI> Group compound single crystal growth boat

Info

Publication number
JPH0735318B2
JPH0735318B2 JP61132983A JP13298386A JPH0735318B2 JP H0735318 B2 JPH0735318 B2 JP H0735318B2 JP 61132983 A JP61132983 A JP 61132983A JP 13298386 A JP13298386 A JP 13298386A JP H0735318 B2 JPH0735318 B2 JP H0735318B2
Authority
JP
Japan
Prior art keywords
boat
single crystal
opening
compound single
crystal growth
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 - Fee Related
Application number
JP61132983A
Other languages
Japanese (ja)
Other versions
JPS62292690A (en
Inventor
勝美 望月
剛 増本
健史 宮崎
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sumitomo Electric Industries Ltd
Original Assignee
Sumitomo Electric Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sumitomo Electric Industries Ltd filed Critical Sumitomo Electric Industries Ltd
Priority to JP61132983A priority Critical patent/JPH0735318B2/en
Publication of JPS62292690A publication Critical patent/JPS62292690A/en
Publication of JPH0735318B2 publication Critical patent/JPH0735318B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • 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】 〈産業上の利用分野〉 この発明は、II−VI族化合物単結晶成長用ボートに関す
る。さらに詳細には、この発明は原料の損失を防止し収
率の向上が図れるII−VI族化合物単結晶成長用ボートに
関する。
TECHNICAL FIELD The present invention relates to a boat for growing a II-VI compound single crystal. More specifically, the present invention relates to a boat for growing a II-VI compound single crystal capable of preventing the loss of raw materials and improving the yield.

〈従来の技術〉 従来、II−VI族化合物単結晶の製造方法として、種々の
方法が用いられているが、そのような方法の一つとし
て、第3図に示されるような単結晶成長用のボートを用
いた水平ブリッジマン法を挙げることができる。この装
置を用いてII−VI族化合物単結晶、例えば、CdTe化合物
単結晶を製造する一例を説明すると、反応部(4)とリ
ザーバー部(5)とがキャピラリーで連通された反応容
器(6)を使用し、リザーバー部(5)に適量のCdを加
えるとともに反応部(4)に設けられた単結晶成長用ボ
ート(7)内にCdTe化合物原料を仕込んだ後、反応容器
(6)を減圧し真空とする。そして、反応容器(6)を
炉(8)により外部から加熱すると、CdTe化合物原料は
しだいにCdを吸収し、最終的には化学量論的組成の融液
(9)となった後、単結晶成長用ボート(7)の一端に
設けられた棚部に保持されたCdTe化合物単結晶(種子結
晶)を該融液(9)に接触させ、結晶成長を開始させ
る。その後、炉(8)の温度分布を移動(装置によって
は、炉またはボートの移動)させて結晶を成長させ、Cd
Te化合物単結晶(10)が製造される。上記の製造方法に
おいて、該炉(8)の温度分布は、反応容器(6)内部
の蒸気圧の制御を行ないつつ単結晶の成長を行うため、
通常、第4図に示されるように、T1(CdTe化合物の融
点)以上の温度領域、前記T1と後記T3との間の温度であ
るT2の温度領域、および反応系内を化学量論的な化合物
を得るに適した蒸気圧に保持するために、蒸気圧制御物
質(上記の例ではCd)を蒸発させるに必要な加熱温度で
あるT3の温度領域の3つの定温度帯となされている。
<Prior Art> Conventionally, various methods have been used as a method for producing a II-VI group compound single crystal. One of such methods is for growing a single crystal as shown in FIG. The horizontal Bridgman method using a boat can be mentioned. An example of producing a II-VI group compound single crystal, for example, a CdTe compound single crystal using this apparatus will be described. A reaction vessel (6) in which a reaction section (4) and a reservoir section (5) are connected by a capillary. After adding an appropriate amount of Cd to the reservoir part (5) and charging the CdTe compound raw material into the single crystal growth boat (7) provided in the reaction part (4), the reaction vessel (6) is depressurized. And make a vacuum. Then, when the reaction vessel (6) is externally heated by the furnace (8), the CdTe compound raw material gradually absorbs Cd, and finally becomes a melt (9) having a stoichiometric composition. A CdTe compound single crystal (seed crystal) held on a shelf provided at one end of the crystal growth boat (7) is brought into contact with the melt (9) to start crystal growth. After that, the temperature distribution of the furnace (8) is moved (the furnace or boat is moved depending on the device) to grow a crystal, and Cd
A Te compound single crystal (10) is produced. In the above-mentioned manufacturing method, the temperature distribution of the furnace (8) is such that the single crystal is grown while controlling the vapor pressure inside the reaction vessel (6).
Usually, as shown in FIG. 4, a stoichiometric range is set in a temperature range equal to or higher than T1 (melting point of CdTe compound), a temperature range of T2 which is a temperature between T1 and T3 described later, and a reaction system. In order to maintain the vapor pressure suitable for obtaining the compound, there are three constant temperature zones in the temperature region of T3 which is the heating temperature required for vaporizing the vapor pressure control substance (Cd in the above example).

このように融液(9)から解離して逃散しようとするCd
蒸気の圧力と、リザーバー部(5)内のCdの蒸気圧とが
等しくなるように制御することにより、融液(9)の組
成が変化するのを防止している。
Cd that dissociates from the melt (9) and tries to escape
The composition of the melt (9) is prevented from changing by controlling the vapor pressure and the vapor pressure of Cd in the reservoir (5) to be equal.

〈発明が解決しようとする問題点〉 しかしながら、CdTe化合物は融点における解離圧が大き
く、またCdおよびTeは共に高い蒸気圧を示す。特にCdは
蒸気圧が高いので、上記方法のような化学量論的組成制
御のCd圧においても単結晶成長用ボート(7)内の融液
(9)の表面からリザーバー部(5)への蒸発が生じ、
原料の損失が大きいという問題がある。このとき、上述
した蒸気圧制御によってCdの融液(9)からの蒸発は抑
制されているのに対して、CdとTeの蒸気圧が共に高い場
合には制御できない。特に、大型の単結晶を製造する際
には、成長用ボートも大型となり、表面積も広くなるの
で、蒸発による損失は大きなものとなる。
<Problems to be Solved by the Invention> However, CdTe compounds have a large dissociation pressure at the melting point, and both Cd and Te show high vapor pressures. In particular, since Cd has a high vapor pressure, even when the Cd pressure is controlled by stoichiometric composition as in the above method, the surface of the melt (9) in the single crystal growth boat (7) flows into the reservoir section (5). Evaporation occurs,
There is a problem that the loss of raw materials is large. At this time, evaporation of Cd from the melt (9) is suppressed by the vapor pressure control described above, but cannot be controlled when both vapor pressures of Cd and Te are high. In particular, when a large single crystal is manufactured, the growth boat also becomes large and the surface area becomes large, so that the loss due to evaporation becomes large.

〈目的〉 この発明は上記問題点に鑑みてなされたものであり、成
長用ボート表面からの蒸発を制御し、原料の損失を防止
できるII−VI族化合物単結晶成長用ボートを提供するこ
とを目的とする。
<Object> The present invention has been made in view of the above problems, and provides a boat for growing II-VI compound single crystals capable of controlling evaporation from the surface of the boat for growth and preventing loss of raw materials. To aim.

〈構成〉 上記目的を達成するためになされた、この発明のII−VI
族化合物単結晶成長用ボートは、開口部を有する有蓋の
単結晶成長用ボートであることを特徴とし、該開口部は
小面積であることが好ましい。
<Structure> II-VI of the present invention made to achieve the above object
The group compound single crystal growth boat is characterized by being a capped single crystal growth boat having an opening, and the opening preferably has a small area.

〈作用〉 この発明は、上記の構成よりなり、成長用ボート内の融
液は、開口部を有する蓋で覆われるので、該蓋が融液表
面からの蒸発の抵抗体となり、原料の損失を減少させる
ことができる。特に、開口部が小面積であれば、この効
果は一層大きくなる。
<Operation> The present invention has the above-described configuration, and since the melt in the growth boat is covered with the lid having the opening, the lid serves as a resistance against evaporation from the surface of the melt, thereby reducing the loss of the raw material. Can be reduced. In particular, if the opening has a small area, this effect becomes even greater.

ここで、開口部を設けているのは、以下の理由による。
例えばCdTe化合物単結晶を製造する水平ブリッジマン法
では、前述のように、反応容器内のボート外に置いたCd
を加熱して、Cd蒸気をボート内の融液に徐々に吸収させ
て、最終的に化学当量的組成のCdTe融液とする。従っ
て、前記開口部はCd蒸気の進入口として機能する。
Here, the reason why the opening is provided is as follows.
For example, in the horizontal Bridgman method for producing a CdTe compound single crystal, as described above, Cd placed outside the boat inside the reaction vessel
Is heated to gradually absorb the Cd vapor into the melt in the boat, and finally form a CdTe melt having a stoichiometric composition. Therefore, the opening functions as an entrance for Cd vapor.

〈実施例〉 以下、実施例を示す添附図面に基づいて詳細に説明す
る。
<Example> Hereinafter, a detailed description will be given based on the accompanying drawings showing an example.

第1図は、この発明のII−VI族化合物単結晶成長用ボー
トの一実施例を示す斜視図で、ボート底部(1)、蓋
(2)および開口部(3)で構成されている。ボート底
部(1)は従来から使用されている単結晶成長用ボート
と実質的に同一のものである。該ボート底部(1)の上
方開口面は蓋(2)で覆われ、蓋(2)にはスリット状
の開口部(3)が該蓋(2)の幅方向に沿って設けられ
ている。ボート底部(1)と蓋(2)とは融着等により
封着してもよいが、封着しなくとも、この発明の効果は
充分に達成することができる。開口部(3)の形状は、
特に限定されず、上記のようにスリット状としてもよい
し、小穴状等でもよい。また、蓋(2)を2つに分け、
その二分された蓋(2)をボート底部(1)上に小間隔
をおいて覆設することによって開口部(3)を形成して
もよい。さらに、開口部(3)は上記実施例とは異な
り、該蓋(2)の長さ方向に沿って設けられていてもよ
い。
FIG. 1 is a perspective view showing an embodiment of a boat for growing a II-VI group compound single crystal according to the present invention, which comprises a boat bottom portion (1), a lid (2) and an opening portion (3). The bottom part (1) of the boat is substantially the same as the conventional single crystal growth boat. The upper opening surface of the boat bottom (1) is covered with a lid (2), and the lid (2) is provided with a slit-shaped opening (3) along the width direction of the lid (2). The boat bottom (1) and the lid (2) may be sealed by fusion or the like, but the effects of the present invention can be sufficiently achieved without sealing. The shape of the opening (3) is
The shape is not particularly limited, and may be a slit shape as described above, a small hole shape, or the like. Also, divide the lid (2) into two,
The opening (3) may be formed by covering the divided bottom (2) on the boat bottom (1) at a small interval. Further, the opening (3) may be provided along the length direction of the lid (2), unlike the above embodiment.

この発明にあっては、開口部(3)の形状等よりもその
面積が重要な意味を有し、開口部(3)の面積を10mm2
以下とするのが制御性の面から好ましい。
In the present invention, the area is more important than the shape of the opening (3), and the area of the opening (3) is 10 mm 2
The following is preferable from the viewpoint of controllability.

上記ボート底部(1)および蓋(2)の材質としては、
外部より結晶の成長状態を観察できる点から透明石英が
好ましいが、予め設定された条件で製造を行うように観
察が不用の場合には、セラミックス、BN、SiC、Al2O3
の材質でもよい。
As the material of the boat bottom (1) and the lid (2),
Transparent quartz is preferable from the viewpoint of observing the crystal growth state from the outside, but when observation is unnecessary so that the production is carried out under preset conditions, ceramics, BN, SiC, Al 2 O 3 etc. Good.

次に、この発明にかかる単結晶成長用ボートの使用法の
一例を説明すると、まずボート底部(1)の内部にII−
VI族化合物単結晶原料を充填し、開口部(3)を有する
蓋(2)で覆った後、第3図で示される装置の反応部
(4)の所定位置に設置し、反応容器(6)を減圧し真
空とする。以下、従来の水平ブリッジマン法に準じて、
II−VI族化合物単結晶を成長させる。上記の製造方法
中、開口部(3)は結晶の成長方向に向かって後ろ側に
設ける方が蒸気圧の制御を行うには好ましい。従って、
蓋(2)に開口部(3)を設ける際にも、蓋(2)の長
さ方向の一端に寄った部分に開口部(3)を設けること
が好ましい。
Next, an example of the method of using the single crystal growth boat according to the present invention will be described. First, inside the boat bottom portion (1) II-
After filling the group VI compound single crystal raw material and covering it with a lid (2) having an opening (3), it was placed at a predetermined position of the reaction section (4) of the apparatus shown in FIG. ) Is depressurized to vacuum. Hereafter, according to the conventional horizontal Bridgman method,
A II-VI compound single crystal is grown. In the above manufacturing method, it is preferable to provide the opening (3) on the rear side in the crystal growth direction in order to control the vapor pressure. Therefore,
Also when providing the opening (3) in the lid (2), it is preferable to provide the opening (3) at a portion near one end in the length direction of the lid (2).

以下、実験例をもって、この発明をより詳細に説明す
る。
Hereinafter, the present invention will be described in more detail with reference to experimental examples.

実験例 スリット面積を変化させた、第1図に示される単結晶成
長用ボート(長さ170mm、幅20mm、深さ10mm)を作製
し、該ボート内にCdTe化合物原料を一定量仕込んだ後、
第3図に示される装置の反応部の所定位置に設置し、T1
=1170℃、T2−1050℃およびT3=820℃の温度条件で加
熱し、原料のロス量を測定した。ロス量の測定は、CdTe
化合物を含むボートの加熱前後の重量の差により求め
た。その結果を第2図に示す。
Experimental Example A single crystal growth boat (length 170 mm, width 20 mm, depth 10 mm) shown in FIG. 1 having different slit areas was prepared, and after a certain amount of a CdTe compound raw material was charged in the boat,
Installed at the specified position of the reaction part of the device shown in FIG.
It was heated under the temperature conditions of = 1170 ° C, T2-1050 ° C and T3 = 820 ° C, and the loss amount of the raw material was measured. The amount of loss is measured by CdTe
It was determined by the difference in weight of the boat containing the compound before and after heating. The results are shown in FIG.

第2図から明らかなように、ロス量は、ある開口面積
(S0)までは開口面積に比例して増加するが、S0を越え
るとロス量の変化はなくなり、Cd分圧や融液温度の影響
が強くなる。種々の実験の結果、クリティカルポイント
S0は、Cd分圧や融液条件により若干の変化が見られる
が、おおよそ2〜10mm2の範囲に存在する。従って、開
口部の面積は10mm2以下とするのが好ましい。
As is clear from FIG. 2, the loss amount increases in proportion to the opening area up to a certain opening area (S0), but when it exceeds S0, the loss amount does not change, and the Cd partial pressure and the melt temperature The impact will be stronger. Results of various experiments, critical points
S0 slightly changes depending on the Cd partial pressure and the melt conditions, but exists in the range of approximately 2 to 10 mm 2 . Therefore, the area of the opening is preferably 10 mm 2 or less.

〈効果〉 以上のように、この発明のII−VI族化合物単結晶成長用
ボートによれば、開口部を有する蓋が融液表面からの蒸
発を抑制するので、原料の損失を防止でき、生産性の向
上に寄与できるという特有の効果を奏する。
<Effect> As described above, according to the boat for growing II-VI compound single crystal of the present invention, the lid having the opening suppresses evaporation from the melt surface, so that loss of raw material can be prevented and production It has a unique effect that it can contribute to the improvement of sex.

【図面の簡単な説明】[Brief description of drawings]

第1図は、この発明にかかるII−VI族化合物単結晶成長
用ボートの一実施例を示す斜視図、 第2図は、実験例における開口面積とロス量の関係を示
す図、 第3図および第4図は、それぞれ水平ブリッジマン法に
用いられる装置の概略図および温度制御例の概略図であ
る。 (1)……ボート底部、(2)……蓋 (3)……開口部
FIG. 1 is a perspective view showing an embodiment of a boat for growing a II-VI group compound single crystal according to the present invention, FIG. 2 is a view showing a relationship between an opening area and a loss amount in an experimental example, FIG. FIG. 4 and FIG. 4 are a schematic diagram of an apparatus used in the horizontal Bridgman method and a schematic diagram of an example of temperature control, respectively. (1) …… bottom of boat, (2) …… cover (3) …… opening

フロントページの続き (72)発明者 宮崎 健史 大阪府大阪市此花区島屋1丁目1番3号 住友電気工業株式会社大阪製作所内 (56)参考文献 特開 昭59−83914(JP,A) 特開 昭57−47795(JP,A) 実開 昭58−129634(JP,U)Front Page Continuation (72) Inventor Kenji Miyazaki 1-3-3 Shimaya, Konohana-ku, Osaka City, Osaka Prefecture Sumitomo Electric Industries, Ltd. (56) Reference JP-A-59-83914 (JP, A) Showa 57-47795 (JP, A) Actually opened Showa 58-129634 (JP, U)

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】水平ブリッジマン法によるII−VI族化合物
単結晶の製造に使用される単結晶成長用ボートにおい
て、該ボートが開口部を有する有蓋ボートであることを
特徴とするII−VI族化合物単結晶成長用ボート。
1. A boat for growing a single crystal used for producing a II-VI compound single crystal by the horizontal Bridgman method, wherein the boat is a covered boat having an opening. Compound single crystal growth boat.
【請求項2】開口部の面積が、10mm2以下である上記特
許請求の範囲第1項記載のII−VI族化合物単結晶成長用
ボート。
2. The boat for growing a II-VI group compound single crystal according to claim 1, wherein the area of the opening is 10 mm 2 or less.
JP61132983A 1986-06-09 1986-06-09 <II>-<VI> Group compound single crystal growth boat Expired - Fee Related JPH0735318B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61132983A JPH0735318B2 (en) 1986-06-09 1986-06-09 <II>-<VI> Group compound single crystal growth boat

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61132983A JPH0735318B2 (en) 1986-06-09 1986-06-09 <II>-<VI> Group compound single crystal growth boat

Publications (2)

Publication Number Publication Date
JPS62292690A JPS62292690A (en) 1987-12-19
JPH0735318B2 true JPH0735318B2 (en) 1995-04-19

Family

ID=15094042

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61132983A Expired - Fee Related JPH0735318B2 (en) 1986-06-09 1986-06-09 <II>-<VI> Group compound single crystal growth boat

Country Status (1)

Country Link
JP (1) JPH0735318B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH026330A (en) * 1988-03-07 1990-01-10 Sanyo Electric Co Ltd Production of superconducting material and superconducting single crystal

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5747795A (en) * 1980-08-09 1982-03-18 Hitachi Cable Ltd Manufacture of mixed single crystal
JPS58129634U (en) * 1982-02-25 1983-09-02 富士通株式会社 Ampoule for manufacturing semiconductor crystals
JPS5983914A (en) * 1982-10-29 1984-05-15 Fujitsu Ltd Method for forming alloy containing easily evaporable component

Also Published As

Publication number Publication date
JPS62292690A (en) 1987-12-19

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