JPH07133182A - Hydrothermal synthesis and growth vessel for hydrothermal synthesis - Google Patents

Hydrothermal synthesis and growth vessel for hydrothermal synthesis

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Publication number
JPH07133182A
JPH07133182A JP27445093A JP27445093A JPH07133182A JP H07133182 A JPH07133182 A JP H07133182A JP 27445093 A JP27445093 A JP 27445093A JP 27445093 A JP27445093 A JP 27445093A JP H07133182 A JPH07133182 A JP H07133182A
Authority
JP
Japan
Prior art keywords
hydrothermal synthesis
temp
growth container
solute
zno
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.)
Withdrawn
Application number
JP27445093A
Other languages
Japanese (ja)
Inventor
Yuji Asai
裕次 浅井
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.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP27445093A priority Critical patent/JPH07133182A/en
Publication of JPH07133182A publication Critical patent/JPH07133182A/en
Withdrawn legal-status Critical Current

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Abstract

PURPOSE:To obviate the formation of unnecessary deposits at the time of hydrothermal synthesis and to facilitate maintenance by disposing a solute capturing member for selectively capturing solute near the focusing point of solute transporting flow. CONSTITUTION:This growth vessel 10 for hydrothermal synthesis has internally a baffle plate 13 and is segmented to a low-temp. part 15 and a high-temp. part 17 by the baffle plate 13. ZnO sintered compacts 5 which are an example of the growth product are packed in the high-temp. part 17 and ZnO seed crystals 3 are hung down in the low-temp. part 15. The deposit capturing net 30 is disposed. The dissolved ZnO is transported from the high-temp. part 17 to the low-temp. part 15 through the through holes 13p of the baffle plate 13 by the thermal convection generated by a temp. difference between the low-temp. part 15 and the high-temp. part 17. The supersatd. components of the dissolved ZnO grow the seed crystals 3 by precipitating on the seed crystals 3 and pass the deposit capturing net 30. The remaining parts of the supersatd. components of the ZnO precipitated on the seed crystals 3 precipitate selectively on the capturing net 3 at the time of passing the capturing net 30.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、水熱合成方法及び水熱
合成法に用いる容器に係り、更に詳細には、水熱合成に
際し、不要な析出物が析出・付着しにくい水熱合成方法
及び水熱合成用育成容器に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hydrothermal synthesis method and a container used in the hydrothermal synthesis method, and more specifically to a hydrothermal synthesis method in which unnecessary precipitates are less likely to deposit and adhere during hydrothermal synthesis. And a container for hydrothermal synthesis.

【0002】[0002]

【従来の技術】従来から、新規物質の合成、不完全結晶
からの不純物除去、鉱物の改質、及び種々の物質の単結
晶を育成する方法の一つとして、水熱合成法が知られて
いる。例えば、この水熱合成法による単結晶の育成にお
いては、育成容器の低温部に種結晶を吊下げ、高温部に
は適当な原料を充填し、所定のアルカリ又は塩類等の希
薄溶液を注入し、温度差による溶解度の差を利用して種
結晶上に所定物質を析出させることにより、単結晶が育
成される。
2. Description of the Related Art Conventionally, hydrothermal synthesis has been known as one of methods for synthesizing new substances, removing impurities from incomplete crystals, modifying minerals, and growing single crystals of various substances. There is. For example, in growing a single crystal by this hydrothermal synthesis method, a seed crystal is hung in a low temperature part of a growth container, an appropriate raw material is filled in a high temperature part, and a dilute solution of a predetermined alkali or salt is injected. The single crystal is grown by precipitating a predetermined substance on the seed crystal by utilizing the difference in solubility due to the temperature difference.

【0003】この際、原料より溶解した溶質は高温部と
低温部との温度差に起因する熱対流により低温部に輸送
され、しかる後、溶質は、溶質の過飽和状態となった低
温部において、種結晶上に析出し、種結晶を成長させ
る。
At this time, the solute dissolved from the raw material is transported to the low temperature part by thermal convection caused by the temperature difference between the high temperature part and the low temperature part, and thereafter, the solute in the supersaturated low temperature part of the solute, Precipitates on the seed crystal and grows the seed crystal.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、このよ
うな従来の水熱合成法においては、低温部で過飽和状態
になっている溶質は、種結晶上のみならず、種結晶を吊
下げている貴金属線、この貴金属線を締結するフレーム
や育成容器の内壁にも析出物として析出することがあっ
た。
However, in such a conventional hydrothermal synthesis method, the solute that is in a supersaturated state at a low temperature part is not only on the seed crystal but also on the precious metal that suspends the seed crystal. Wires, the frame that fastens this noble metal wire, and the inner wall of the growth container were sometimes deposited as precipitates.

【0005】そして、貴金属線に析出した場合には、こ
の析出物が育成させようとする種結晶と接触してその成
長を阻害するという課題があり、フレームや育成容器内
壁に析出した場合には、次の単結晶育成に際し、析出物
を除去しなければならず、時間的ロスが大きくなるとい
う課題があった。更に、育成容器内壁とフレームとの間
隙に析出物が形成された場合には、育成容器からフレー
ムを取り出すことが困難になるという課題があった。
When it is deposited on the noble metal wire, there is a problem that the deposit contacts the seed crystal to be grown and inhibits its growth. When it is deposited on the frame or the inner wall of the growth container, it has a problem. In the next single crystal growth, the precipitate must be removed, and there is a problem that the time loss becomes large. Furthermore, if a precipitate is formed in the gap between the inner wall of the growth container and the frame, it is difficult to remove the frame from the growth container.

【0006】本発明は、このような従来技術の有する課
題に鑑みてなされたものであり、その目的とするところ
は、水熱合成に際し、不要な析出物が生成せず育成効率
に優れ、しかもメンテナンスが容易な水熱合成方法及び
水熱合成用育成容器を提供することにある。
The present invention has been made in view of the above problems of the prior art, and an object of the present invention is not to generate unnecessary precipitates in hydrothermal synthesis, which is excellent in growth efficiency, and An object of the present invention is to provide a hydrothermal synthesis method and a hydrothermal synthesis growth container that are easy to maintain.

【0007】[0007]

【課題を解決するための手段】本発明者は、上記課題を
解決すべく鋭意研究した結果、特定の析出物捕集部材
(溶質捕集部材)を用いることにより、上記課題が解決
できることを見出し、本発明を完成するに至った。従っ
て、本発明の水熱合成方法は、育成容器内の高温部と低
温部との温度差に起因する熱対流によって発生する溶質
輸送流の集束点近傍に、溶質を選択的に捕集する溶質捕
集手段を設けて、育成容器の内壁に結晶が析出するのを
防止することを特徴とする。
As a result of intensive studies to solve the above-mentioned problems, the present inventor has found that the above-mentioned problems can be solved by using a specific precipitate trapping member (solute trapping member). The present invention has been completed. Therefore, the hydrothermal synthesis method of the present invention is a solute that selectively collects solutes in the vicinity of the focusing point of the solute transport flow generated by thermal convection due to the temperature difference between the high temperature part and the low temperature part in the growth container. It is characterized in that a collecting means is provided to prevent crystals from precipitating on the inner wall of the growth container.

【0008】また、本発明の水熱合成用育成容器は、水
熱合成に用いる育成容器において、バッフル板と析出物
捕集部材とを備え、その内部が、上記バッフル板により
低温部と高温部とに区画され、この低温部に、上記析出
物捕集部材が配設されて成ることを特徴とする。
Further, the hydrothermal synthesis growth container of the present invention is a growth container used for hydrothermal synthesis, comprising a baffle plate and a precipitate collecting member, the interior of which is a low temperature part and a high temperature part by the baffle plate. It is characterized in that the precipitate collecting member is disposed in the low temperature portion.

【0009】[0009]

【作用】本発明の水熱合成用育成容器においては、特定
の析出物捕集部材を溶質輸送流(高温部と低温部との温
度差に起因する熱対流)の集束点近傍に配置することに
した。従って、従来、水熱合成に際し、育成容器の内壁
等に析出していた不要な析出物は、この析出物捕集部材
に選択的に捕集される。
In the hydrothermal synthesis growth container of the present invention, the specific precipitate-collecting member is arranged near the focusing point of the solute transport flow (heat convection due to the temperature difference between the high temperature part and the low temperature part). I chose Therefore, unnecessary deposits that have conventionally been deposited on the inner wall of the growth container during hydrothermal synthesis are selectively collected by this deposit collection member.

【0010】即ち、例えば、水熱合成法による単結晶の
育成においては、育成容器の下部に位置する高温部に充
填された原料より溶解した溶質が、上部に位置する低温
部との温度差に起因する熱対流により、バッフル板を介
して上昇し、溶質の過飽和分が低温部に配置された種結
晶上に析出する。その後、種結晶上に析出しきらなかっ
た残余の溶質は更に上昇し、育成容器の頂部内壁と接触
し、下方向に反転するが、この際、残余の溶質は上記析
出物捕集部材に選択的に捕集される。
That is, for example, in the growth of a single crystal by the hydrothermal synthesis method, the solute dissolved from the raw material filled in the high temperature part located in the lower part of the growth container has a temperature difference from that in the low temperature part located in the upper part. Due to the resulting heat convection, it rises through the baffle plate, and the supersaturated component of the solute is deposited on the seed crystal arranged in the low temperature part. After that, the residual solute that was not completely precipitated on the seed crystal further rises, contacts the inner wall of the top of the growth container, and inverts downward, but at this time, the residual solute is selected as the precipitate collecting member. To be collected.

【0011】従って、例えば、水熱合成法による単結晶
の育成では、析出物が種結晶を吊下げた貴金属線等に付
着し、種結晶の成長を妨げることを防止でき、また、育
成容器に付着した析出物を除去することも不要となる。
Therefore, for example, in growing a single crystal by the hydrothermal synthesis method, it is possible to prevent deposits from adhering to a precious metal wire or the like on which the seed crystal is suspended and hindering the growth of the seed crystal. It is also unnecessary to remove the deposited deposits.

【0012】以下、本発明の水熱合成用育成容器につい
て詳細に説明する。本発明の育成容器は、バッフル板と
析出物捕集部材とを内蔵する。ここで、育成容器の形状
は、特に限定されるものではなく、立方体、直方体、3
角柱、多角柱等の種々の形状をとり得るが、育成容器内
の圧力の均一性や育成容器内への熱伝達の均一性を考慮
すれば、円柱状が好ましい。
The hydrothermal synthesis growth container of the present invention will be described in detail below. The growth container of the present invention contains a baffle plate and a precipitate collecting member. Here, the shape of the growing container is not particularly limited, and may be a cube, a rectangular parallelepiped, or a cube.
Although various shapes such as a prism and a polygonal column can be adopted, a columnar shape is preferable in view of the uniformity of pressure in the growth container and the uniformity of heat transfer into the growth container.

【0013】育成容器の材質も、特に限定されるもので
はないが、水熱合成により得ようとする物質の種類、溶
媒等に応じた耐蝕性、耐熱性及び耐圧性を備えた材料を
選定する必要がある。例えば、ZnO単結晶の育成につ
いては、Ag又はPt製とするのが好ましい。
The material of the growth container is not particularly limited, but a material having corrosion resistance, heat resistance and pressure resistance is selected according to the type of substance to be obtained by hydrothermal synthesis, the solvent and the like. There is a need. For example, for growing a ZnO single crystal, it is preferable to use Ag or Pt.

【0014】上述の如く、この育成容器の内部にはバッ
フル板が設置されているが、このバッフル板により、育
成容器内部が低温部と高温部とに区画されている。この
バッフル板は、育成容器に注入する溶媒の熱対流を抑制
して低温部と高温部との温度差を保つために設置するも
のであり、貫通孔を有する。その開孔率は、水熱合成処
理する物質の種類に応じて適宜変更し得るものである
が、ZnO単結晶を育成する場合には、3〜10%程度
とするのが好ましい。また、バッフル板の材質は、特に
限定されず、上記育成容器と同様に、得ようとする物質
の種類等に応じて耐熱性、耐蝕性等を考慮して適宜選定
すればよい。
As described above, the baffle plate is installed inside the growing container, and the inside of the growing container is divided into the low temperature part and the high temperature part by the baffle plate. This baffle plate is installed in order to suppress the thermal convection of the solvent injected into the growth container and maintain the temperature difference between the low temperature part and the high temperature part, and has a through hole. The porosity can be appropriately changed according to the kind of the substance to be subjected to the hydrothermal synthesis treatment, but when growing a ZnO single crystal, it is preferably about 3 to 10%. The material of the baffle plate is not particularly limited, and may be appropriately selected in consideration of heat resistance, corrosion resistance, etc., depending on the type of substance to be obtained, etc., as in the above-mentioned growth container.

【0015】次に、上記析出物捕集部材は、育成容器内
部の低温部に配置され、好ましくは、溶質輸送流(上記
熱対流)が、種結晶の吊下げ位置を超えた位置(種結晶
より上部側)であって、この溶質輸送流の集束点近傍に
配置される。典型的には、この捕集部材を配置する位置
は育成容器の頂部近傍であり、代表的に、育成容器の寸
法が内径30mm×高さ350mmの場合には、育成容
器の頂部から5〜25mm程度の位置に配置するのがよ
い。また、育成容器の頂部を球面状に凸設することによ
り、溶質輸送流の経路を、頂部近傍に配置した析出物捕
集部材を選択的に通過させるように制御できるので、育
成容器の頂部をこのように形成するのが好ましい。
Next, the precipitate collecting member is arranged at a low temperature portion inside the growth container, and preferably, the position where the solute transport flow (heat convection) exceeds the suspension position of the seed crystal (seed crystal). It is located on the upper side) and near the focusing point of this solute transport flow. Typically, the position where this collecting member is arranged is near the top of the growing container. Typically, when the size of the growing container is 30 mm inside diameter x 350 mm in height, 5 to 25 mm from the top of the growing container. It is better to place it at a certain position. Further, by providing a spherical projection on the top of the growth container, the path of the solute transport flow can be controlled so as to selectively pass through the precipitate collecting member arranged near the top, so that the top of the growth container is It is preferably formed in this way.

【0016】上記析出物捕集部材の形状は、特に限定さ
れるものではないが、線状部材を複数組み合わせて構成
されるのが好ましく、代表的に、簾形状やネット形状を
例示できる。また、線状部材の材質も、特に限定される
ものではなく、意図する水熱合成処理、使用する溶媒等
に応じて適宜変更でききるが、Ag、Pt等の貴金属が
好ましく、H22のような酸素発生剤を用いる場合には
Ptが好ましい。
The shape of the deposit collecting member is not particularly limited, but it is preferable that a plurality of linear members are combined, and a typical example is a blind shape or a net shape. Further, the material of the linear member is not particularly limited and can be appropriately changed according to the intended hydrothermal synthesis treatment, the solvent used, etc., but a noble metal such as Ag or Pt is preferable, and H 2 O 2 When using such an oxygen generating agent, Pt is preferable.

【0017】[0017]

【実施例】以下、本発明を、図面を参照して実施例によ
り詳細に説明する。図1に、本発明の水熱合成用育成容
器の一実施例を示す。同図において、育成容器1は、そ
の内部にバッフル板13を備え、このバッフル板13に
より低温部15と高温部17とに区画されている。高温
部17には、育成物の一例であるZnO焼結体5が充填
されており、低温部15には、ZnO種結晶3が吊下げ
られており、また、析出物捕集ネット30が設けられて
いる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in detail below with reference to the drawings with reference to the accompanying drawings. FIG. 1 shows an embodiment of the hydrothermal synthesis growth container of the present invention. In the figure, the growth container 1 is provided with a baffle plate 13 inside and is divided into a low temperature part 15 and a high temperature part 17 by this baffle plate 13. The high temperature part 17 is filled with a ZnO sintered body 5 which is an example of a grown product, the low temperature part 15 is hung with the ZnO seed crystal 3, and a precipitate collecting net 30 is provided. Has been.

【0018】種結晶3は、貴金属線7により貴金属製の
フレーム20に締結されて吊下げられている。そして、
フレーム20の頂部22は環状に形成されており、この
環状の頂部22に、貴金属製の析出物捕集ネット30が
貴金属線7を介して締結されている。なお、本実施例に
おいて、析出物捕集ネット30が締結された環状頂部2
2とフレーム20とは一体的に形成されているが、両者
を別体で形成し、析出物捕集ネット30が締結された環
状部材22をフレーム20に載置してもよい。また、バ
ッフル板13には、貫通孔13p及び13hが穿設され
ており、熱対流はこの貫通孔13p及び13hを介して
起こっている。
The seed crystal 3 is fastened to and suspended from a noble metal frame 20 by a noble metal wire 7. And
The top portion 22 of the frame 20 is formed in an annular shape, and the precious metal deposit collecting net 30 is fastened to the annular top portion 22 via the noble metal wire 7. In this embodiment, the annular top 2 to which the precipitate collecting net 30 is fastened
Although 2 and the frame 20 are integrally formed, they may be formed separately and the annular member 22 to which the precipitate collecting net 30 is fastened may be placed on the frame 20. Further, through holes 13p and 13h are formed in the baffle plate 13, and thermal convection occurs through these through holes 13p and 13h.

【0019】図2は、育成容器1を用いて水熱合成する
際に、溶解したZnOが輸送される様子を示した断面説
明図である。同図の矢印Fで示すように、溶解したZn
Oは、低温部15と高温部17との温度差により生じた
熱対流により、高温部17からバッフル板13の貫通孔
13pを介して低温部15に輸送される。次いで、溶解
したZnOの過飽和分は、種結晶3上に析出して種結晶
3を成長させ、析出物捕集ネット30を通過する。
FIG. 2 is a cross-sectional explanatory view showing how molten ZnO is transported during hydrothermal synthesis using the growth container 1. As shown by the arrow F in the figure, the dissolved Zn
O is transported from the high temperature portion 17 to the low temperature portion 15 through the through hole 13p of the baffle plate 13 by thermal convection caused by the temperature difference between the low temperature portion 15 and the high temperature portion 17. Then, the supersaturated portion of the dissolved ZnO is deposited on the seed crystal 3 to grow the seed crystal 3 and passes through the deposit collection net 30.

【0020】この析出物捕集ネット30を通過する際、
種結晶3上に析出したZnO過飽和分の残余分は、この
捕集ネット30に選択的に析出する。従って、種結晶3
以外の部分、例えば、フレーム20の貴金属線7やフレ
ーム20と育成容器10の内壁との間等に、余分なZn
O(析出物)が付着することはなく、種結晶3の成長を
妨げたり、育成容器10をロット毎に洗浄することなど
を回避できる。
When passing through the deposit collecting net 30,
The ZnO supersaturated residue deposited on the seed crystal 3 is selectively deposited on the collection net 30. Therefore, seed crystal 3
Other than the above, for example, between the noble metal wire 7 of the frame 20 and between the frame 20 and the inner wall of the growth container 10, extra Zn is added.
O (precipitate) does not adhere, and it is possible to prevent growth of the seed crystal 3 or to wash the growth container 10 for each lot.

【0021】そして、溶解したZnOは捕集ネット30
を通過した後、育成容器10の頂部10tに到達し、反
転して下降し、バッフル板13の貫通孔13hを介して
高温部17に戻る。この際、頂部13tのなす曲面によ
り、ZnO輸送流Fは滑らかに反転し、ZnOが頂部近
傍に付着するのを一層良好に回避することができる。
Then, the dissolved ZnO is collected net 30.
After passing through, it reaches the top 10t of the growth container 10, is inverted and descends, and returns to the high temperature part 17 through the through hole 13h of the baffle plate 13. At this time, due to the curved surface formed by the top portion 13t, the ZnO transport flow F is smoothly inverted, and ZnO can be better prevented from adhering to the vicinity of the top portion.

【0022】(実施例1)上記育成容器10を用い、Z
nO単結晶を育成した。この際、育成容器10の形状
は、内径30mm×高さ350mmで内容積は約250
mlである。育成用原料としてはZnO焼結体を200
g充填し、種結晶3としては1×1×10mmのZnO
柱状結晶を10個吊下げた。析出物捕集ネット30はA
g製のものを用い、育成容器10の頂部10tから15
mmの位置に配置した。また、バッフル板13の開孔率
は5%である。
(Example 1) Using the above-mentioned growth container 10, Z
An nO single crystal was grown. At this time, the shape of the growing container 10 has an inner diameter of 30 mm and a height of 350 mm and an inner volume of about 250 mm.
ml. A ZnO sintered body was used as a growth raw material for 200 times.
g as a seed crystal 3 and 1 × 1 × 10 mm ZnO
Ten columnar crystals were suspended. The deposit collection net 30 is A
15 g from the top 10t of the growth container 10
It was arranged at a position of mm. The open rate of the baffle plate 13 is 5%.

【0023】育成容器10内に、3mol/lのKOH
と1.5mol/lのLiOHとから成るアルカリ溶媒
を、育成容器10のフリー内容積の約80%の割合で注
入した。この育成容器10を図示しないオートクレーブ
に収容し、このオートクレーブに、圧媒としての蒸留水
をオートクレーブのフリー内容積の約70%の割合で注
入した。
In the growth vessel 10, 3 mol / l KOH
An alkaline solvent composed of 1.5 mol / l of LiOH was injected at a rate of about 80% of the free internal volume of the growth container 10. The growing container 10 was housed in an autoclave (not shown), and distilled water as a pressure medium was injected into the autoclave at a rate of about 70% of the free internal volume of the autoclave.

【0024】次いで、低温部15の温度が高温部17の
温度より常に低くなるように昇温し、低温部15を38
0℃、高温部17を395℃に加熱し、このままの状態
で14日間維持した。しかる後、室温まで温度を下げて
からZnO単結晶を取り出した。種結晶3に析出せず、
育成容器10及びフレーム等に付着したZnOの重量を
測定した結果、その付着量は0.8gであった。
Then, the temperature of the low temperature section 15 is raised so that the temperature of the low temperature section 15 is always lower than that of the high temperature section 17, and the temperature of the low temperature section 15 is adjusted to 38.
The high temperature part 17 at 0 ° C. was heated to 395 ° C. and maintained as it was for 14 days. Then, the temperature was lowered to room temperature and the ZnO single crystal was taken out. Does not precipitate on seed crystal 3,
As a result of measuring the weight of ZnO attached to the growth container 10 and the frame, the attached amount was 0.8 g.

【0025】(比較例1)析出物捕集ネット30を使用
せず、且つ育成容器10の頂部を平坦な形状にした以外
は、実施例1と同様の操作を繰り返した。ZnOの付着
量は、9.0gであった。このことより、本発明の水熱
合成用育成容器を用いれば、余分なZnOの付着量を著
しく低減できることがわかる。
(Comparative Example 1) The same operation as in Example 1 was repeated except that the precipitate collecting net 30 was not used and the growth container 10 had a flat top. The amount of ZnO attached was 9.0 g. From this, it can be seen that the use of the hydrothermal growth container of the present invention can significantly reduce the amount of extra ZnO deposited.

【0026】以上、本発明を実施例により説明したが、
本発明はこれに限定されるものではなく、本発明の要旨
の範囲内において種々の変形が可能である。例えば、本
発明の育成容器は、ZnOの単結晶育成以外の種々の水
熱育成に用いることができる。また、析出物捕集ネット
30を締結する頂部22の平面形状は、円形のみならず
4角形、6角形等の多角形であってもよい。更に、育成
容器10の頂部10tは、必ずしも球面状をなす必要は
なく平坦な形状であってもよい。
The present invention has been described above with reference to the embodiments.
The present invention is not limited to this, and various modifications can be made within the scope of the gist of the present invention. For example, the growth container of the present invention can be used for various hydrothermal growths other than ZnO single crystal growth. Further, the planar shape of the top portion 22 for fastening the deposit collecting net 30 may be not only circular but also polygonal such as quadrangular and hexagonal. Furthermore, the top 10t of the growth container 10 does not necessarily have to be spherical, and may be flat.

【0027】[0027]

【発明の効果】以上説明したように、本発明によれば、
特定の析出物捕集部材を用いることとしたため、水熱合
成に際し、不要な析出物が生成せず育成効率に優れ、し
かもメンテナンスが容易な水熱合成方法及び水熱合成用
育成容器を提供することができる。
As described above, according to the present invention,
Since a specific precipitate collecting member is used, a hydrothermal synthesis method and a growth container for hydrothermal synthesis that are excellent in growth efficiency without generating unnecessary precipitates during hydrothermal synthesis and are easy to maintain are provided. be able to.

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

【図1】本発明の育成容器の一実施例を示す概略斜視図
である。
FIG. 1 is a schematic perspective view showing an embodiment of a growth container of the present invention.

【図2】水熱合成の際のZnO輸送流を示す断面説明図
である。
FIG. 2 is a cross-sectional explanatory diagram showing a ZnO transport flow during hydrothermal synthesis.

【符号の説明】[Explanation of symbols]

10 育成容器、10t 頂部、13 バッフル
板、15 低温部、17 高温部、20 フレー
ム、30 析出物捕集ネット
10 growth container, 10 t top part, 13 baffle plate, 15 low temperature part, 17 high temperature part, 20 frame, 30 deposit collection net

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 育成容器内の高温部と低温部との温度差
に起因する熱対流によって発生する溶質輸送流の集束点
近傍に、溶質を選択的に捕集する溶質捕集手段を設け
て、育成容器の内壁に結晶が析出するのを防止すること
を特徴とする水熱合成方法。
1. A solute trapping means for selectively trapping a solute is provided in the vicinity of a focus point of a solute transport flow generated by thermal convection caused by a temperature difference between a high temperature part and a low temperature part in a growth container. A method for hydrothermal synthesis characterized by preventing crystals from precipitating on the inner wall of a growth container.
【請求項2】 水熱合成に用いる育成容器において、バ
ッフル板と析出物捕集部材とを備え、 その内部が、上記バッフル板により低温部と高温部とに
区画され、 この低温部に、上記析出物捕集部材が配設されて成る、 ことを特徴とする水熱合成用育成容器。
2. A growth container used for hydrothermal synthesis, comprising a baffle plate and a precipitate collecting member, the interior of which is divided into a low temperature part and a high temperature part by the baffle plate, and in this low temperature part, the above A growth container for hydrothermal synthesis, comprising a deposit collection member.
【請求項3】 析出物捕集部材が、溶質輸送流の種結晶
より上部側の集束点近傍に配設されていることを特徴と
する請求項2記載の育成容器。
3. The growth container according to claim 2, wherein the precipitate collecting member is arranged near the focusing point on the upper side of the seed crystal of the solute transport flow.
【請求項4】 析出物捕集部材が、上記低温部の頂部近
傍に配設されていることを特徴とする請求項2又は3記
載の育成容器。
4. The growth container according to claim 2, wherein the precipitate collecting member is arranged near the top of the low temperature portion.
【請求項5】 析出物捕集部材が、貴金属線で構成され
ていることを特徴とする請求項2〜4項のいずれか1つ
の項に記載の育成容器。
5. The growth container according to any one of claims 2 to 4, wherein the deposit collecting member is made of a noble metal wire.
【請求項6】 析出物捕集部材が、貴金属製のネットで
構成されていることを特徴とする請求項2〜5項のいず
れか1つの項に記載の育成容器。
6. The growth container according to claim 2, wherein the deposit collecting member is composed of a net made of a noble metal.
【請求項7】 その頂部が球面状に凸設されていること
を特徴とする請求項2〜6項のいずれか1つの項に記載
の育成容器。
7. The growing container according to any one of claims 2 to 6, characterized in that the top part thereof is provided in a spherical shape.
JP27445093A 1993-11-02 1993-11-02 Hydrothermal synthesis and growth vessel for hydrothermal synthesis Withdrawn JPH07133182A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27445093A JPH07133182A (en) 1993-11-02 1993-11-02 Hydrothermal synthesis and growth vessel for hydrothermal synthesis

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27445093A JPH07133182A (en) 1993-11-02 1993-11-02 Hydrothermal synthesis and growth vessel for hydrothermal synthesis

Publications (1)

Publication Number Publication Date
JPH07133182A true JPH07133182A (en) 1995-05-23

Family

ID=17541864

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27445093A Withdrawn JPH07133182A (en) 1993-11-02 1993-11-02 Hydrothermal synthesis and growth vessel for hydrothermal synthesis

Country Status (1)

Country Link
JP (1) JPH07133182A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004002152A (en) * 2002-02-22 2004-01-08 Mitsubishi Chemicals Corp Method of manufacturing nitride single crystal
JP2008143778A (en) * 2007-12-26 2008-06-26 Mitsubishi Chemicals Corp Method for producing nitride single crystal
JP2011190135A (en) * 2010-03-12 2011-09-29 Seiko Epson Corp Apparatus and method for manufacturing crystal and filter member

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004002152A (en) * 2002-02-22 2004-01-08 Mitsubishi Chemicals Corp Method of manufacturing nitride single crystal
JP2008143778A (en) * 2007-12-26 2008-06-26 Mitsubishi Chemicals Corp Method for producing nitride single crystal
JP2011190135A (en) * 2010-03-12 2011-09-29 Seiko Epson Corp Apparatus and method for manufacturing crystal and filter member

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