JPH02152191A - Vapor deposition method of electroluminescent luminous membrane - Google Patents
Vapor deposition method of electroluminescent luminous membraneInfo
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- JPH02152191A JPH02152191A JP63304820A JP30482088A JPH02152191A JP H02152191 A JPH02152191 A JP H02152191A JP 63304820 A JP63304820 A JP 63304820A JP 30482088 A JP30482088 A JP 30482088A JP H02152191 A JPH02152191 A JP H02152191A
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Abstract
Description
【発明の詳細な説明】
〈産業上の利用分野〉
この発明は薄膜EL(エレクトロルミネッセンス)素子
に使用するエレクトロルミネッセンス発光膜の気相成長
法に関する。DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to a vapor phase growth method for electroluminescent films used in thin film EL (electroluminescent) devices.
〈従来の技術〉
従来、エレクトロルミネッセンス発光膜(本明細書では
以下、発光膜と略す。)の成長方法としては次のような
方法が知られている。すなわち、■ ZnSとMnの混
合焼結ペレットを材料とする電子ビーム蒸着法。<Prior Art> Conventionally, the following method is known as a method for growing an electroluminescent film (hereinafter abbreviated as a light-emitting film). Namely, ■ an electron beam evaporation method using a mixed sintered pellet of ZnS and Mn as a material;
■ Zn、Mn、およびSを蒸気の状態で交互に基板上
へ供給して、単原子層ずつ形成する原子層エピタキシー
法(ALE法)。(2) An atomic layer epitaxy method (ALE method) in which Zn, Mn, and S are alternately supplied in the form of vapor onto a substrate to form monoatomic layers one by one.
■ ■族元素の有機金属化合物と■族元素の水素化物を
基板上で熱分解反応させてII−VIl模膜堆積形成す
る有機金属気相成長法(MOCVD法)。(2) A metal organic chemical vapor deposition method (MOCVD method) in which an organometallic compound of a group (2) element and a hydride of a group (2) element are subjected to a thermal decomposition reaction on a substrate to form a II-VII pattern film.
■ ハロゲン輸送法によって発光中心となる元素をドー
ピングして、発光膜を形成するハライドCVD法である
。(2) This is a halide CVD method in which a light-emitting film is formed by doping an element that becomes a light-emitting center using a halogen transport method.
〈発明が解決しようとする課題〉
しかしながら、上記従来の■の電子ビーム蒸着法は、膜
成長の初期段階に3次元的な粒が形成されるため結晶性
が良くない発光膜が形成される。<Problems to be Solved by the Invention> However, in the conventional electron beam evaporation method (2) described above, three-dimensional grains are formed in the initial stage of film growth, resulting in the formation of a light-emitting film with poor crystallinity.
したがって、輝度が低く、品質が良くないという欠点が
ある。上記■の原子層エピタキシー法は、2次元的な層
状膜成長を行うので、結晶性が良く高輝度の発光膜を形
成することができるが、成長速度が極めて遅いので量産
性に欠ける。また上記■の有機金属気相成長法は、結晶
性が良い発光膜を形成することができるが、大面積のも
のを得ることができず、かつ量産性に欠ける。上記■の
ハライF’ CV D法は、結晶性が良い高品質の発光
膜を得ることができ、しかも大面積化が可能で量産性に
優れた方法である。しかし、膜成長のソース材料として
蒸気圧の低い無機固型物を使用しているので、上記ソー
ス材料を加熱する手段を必要とし、さらに蒸気圧が低い
ため輸送量の制御が困難である。このためそれに供する
装置は複雑で大がかりなものになっている。Therefore, the brightness is low and the quality is poor. The above atomic layer epitaxy method (2) performs two-dimensional layered film growth and can form a light-emitting film with good crystallinity and high brightness, but the growth rate is extremely slow and it lacks mass productivity. In addition, although the organometallic vapor phase epitaxy method described in (1) above can form a light-emitting film with good crystallinity, it is not possible to obtain a large-area film, and it lacks mass productivity. The Harai F' CVD method described in (2) above is a method that can obtain a high-quality light-emitting film with good crystallinity, and is also capable of producing a large area and is excellent in mass production. However, since an inorganic solid material with a low vapor pressure is used as a source material for film growth, a means for heating the source material is required, and furthermore, the low vapor pressure makes it difficult to control the amount of transport. For this reason, the equipment used therefor has become complicated and large-scale.
そこでこの発明の目的は、形成する発光膜が高品質・大
面積化可能・量産性に優れたハライドCVD法の利点を
生かしつつ、ソース材料を加熱する必要がなく、輸送量
の制御が容易で、しかも小型・簡略な装置で行うことが
できる気相成長法を提供することにある。Therefore, the purpose of this invention is to take advantage of the halide CVD method, which produces a light-emitting film of high quality, can be formed in a large area, and has excellent mass productivity, while also eliminating the need to heat the source material and easily controlling the amount of transport. The object of the present invention is to provide a vapor phase growth method that can be performed using a small and simple device.
く課題を解決するための手段〉
上記目的を達成するするために、この発明のエレクトロ
ルミネッセンス発光膜の気相成長法は、反応管内の水素
または不活性ガスの雰囲気下にエレクトロルミネッセン
ス素子用基板を配置して所定温度に保持し、この基板表
面に、II−VI族半導体を構成しうる■族元素または
■族元素の化合物と■族元素または■族元素の化合物と
、■−■族半導体中で発光中心となる元素のハロゲン化
物とを各々蒸気の形態で同時に輸送して接触させること
により、上記基板に■−■族半導体を母体とし、この半
導体内部に発光中心となる元素が含有されたエレクトロ
ルミネッセンス発光膜の気相成長方法であって、上記■
族元素、VI族元素、■族元素の化合物、VI族元素の
化合物3発光中心となる元素および発光中心となる元素
の化合物のうち少なくとも一つについて有機化合物の蒸
気の状態で上記反応管へ導入して、上記反応管内に設け
た高温部において、この有機化合物を、熱分解反応によ
り、■族元素、VI族元素および発光中心となる元素の
うちの少なくとも一つの元素、または上記■族元素、V
I族元素または発光中心となる元素のうちの少なくとも
一つの元素の無機化合物となすと共に、上記高温部にお
いて、上記元素や上記無機化合物と、ハロゲン化水素ガ
スとを混合して、化学反応により■族元素または■族元
素または発光中心となる元素のハロゲン化物の蒸気を生
成した後、この蒸気を基板上へ供給することを特徴とし
ている。Means for Solving the Problems> In order to achieve the above object, the vapor phase growth method of an electroluminescent film of the present invention involves growing a substrate for an electroluminescent element in an atmosphere of hydrogen or inert gas in a reaction tube. A group II element or a compound of a group III element, a group III element or a compound of a group III element, which can constitute a II-VI group semiconductor, and a group III element or a compound of a group By simultaneously transporting and contacting the halides of the elements that form the luminescent center in vapor form, the substrate is made of a ■-■ group semiconductor, and the element that is the luminescent center is contained inside this semiconductor. A method for vapor phase growth of an electroluminescent film, the method comprising:
Group elements, Group VI elements, compounds of Group II elements, compounds of Group VI elements, and at least one of the elements serving as luminescent centers and the compounds of elements serving as luminescent centers are introduced into the reaction tube in the form of organic compound vapor. Then, in the high-temperature section provided in the reaction tube, this organic compound is subjected to a thermal decomposition reaction to convert it into at least one element selected from group (1) elements, group VI elements, and elements serving as luminescent centers; V
An inorganic compound of at least one element selected from group I elements or elements serving as a luminescent center is formed, and the above element or inorganic compound is mixed with hydrogen halide gas in the high temperature section, and a chemical reaction is performed to produce The method is characterized in that after a vapor of a group element, a group Ⅰ element, or a halide of an element serving as a luminescent center is generated, this vapor is supplied onto a substrate.
〈実施例〉
以下、この発明の実施例を詳細に説明する。本実施例は
特に、ソース材料として■族元素Znの有機化合物であ
るジメチル亜鉛Zn(CH3)t、 VI族元素Sの化
合物である硫化水素H,S、全9.心となる元素Mnの
有機化合物であるトリカルボニルメチルシクロペンタジ
ェニルマンガン(TCM)を使用して、発光膜ZnS:
Mnを成長する方法である。以下、この実施例を第1図
に示す横型気相成長装置の構成図により説明する。<Examples> Examples of the present invention will be described in detail below. In particular, this example uses dimethylzinc Zn(CH3)t, which is an organic compound of the group I element Zn, and hydrogen sulfide H, S, which is a compound of the group VI element S, as the source material. Using tricarbonylmethylcyclopentadienylmanganese (TCM), which is an organic compound containing the core element Mn, a light-emitting film ZnS:
This is a method for growing Mn. This embodiment will be explained below with reference to a block diagram of a horizontal vapor phase growth apparatus shown in FIG.
第1図において、lは長さ1m、内径5cmの石英製の
反応管、laは上記反応管lの一端部に設けた枝管、2
,3はそれぞれ上記反応管lの枝管1a側の端部付近に
設けた導入管である。上記反応管lを電気炉4内に収納
し、長平方向の温度分布を図中に示す通り高温部を60
0℃に設定している。In FIG. 1, l is a quartz reaction tube with a length of 1 m and an inner diameter of 5 cm, la is a branch pipe provided at one end of the reaction tube l, and 2
, 3 are inlet tubes provided near the end of the reaction tube 1 on the side of the branch tube 1a, respectively. The above reaction tube l was housed in an electric furnace 4, and the high temperature part was set at 60°C as shown in the figure to show the temperature distribution in the longitudinal direction.
It is set at 0℃.
そして上記反応管1の他端部から反応管l内にできる反
応生成物等を主バルブ17を通して油回転ポンプ18に
よって排気するようにしている。そして、上記導入管2
,3の先端と上記他端との間の反応域に基板ボルダ6を
設け、発光膜の下地膜を堆積したガラス製の基板5を傾
斜立脚させている。また、■族元素Znの有機化合物で
あるZn(CH3)、液を入れたバブラ8を恒温槽9内
に、発光中心となる元素Mnの有機化合物であるTCM
液を入れたバブラ10を恒温槽ll内にそれぞれ収納し
、一定温度に保持している。From the other end of the reaction tube 1, reaction products and the like produced in the reaction tube 1 are exhausted through a main valve 17 by an oil rotary pump 18. Then, the introduction pipe 2
, 3 and the other end thereof, a substrate boulder 6 is provided in the reaction area, and the glass substrate 5 on which the base film of the light-emitting film is deposited is erected at an angle. In addition, a bubbler 8 containing Zn(CH3), an organic compound of the group element Zn, and a liquid was placed in a thermostatic chamber 9, and TCM, an organic compound of the element Mn, which is the center of luminescence, was placed in a thermostatic chamber 9.
The bubblers 10 filled with liquid are each housed in a constant temperature bath 11 and maintained at a constant temperature.
上記横型気相成長装置を用いて、発光膜の成長は次のよ
うにして行う。A light emitting film is grown in the following manner using the horizontal vapor phase growth apparatus described above.
■ H,ガスボンベ13から出た!]、ガスをマスフロ
ーコントローラ12cで流量制御して、バブラ8内でバ
ブルする。すなわち、12. n(CH3) tをH2
をキャリアガスとしてバブル法により輸送する。HCQ
ガスボンベ14から出たHC&ガスをマスフローコント
ローラ12bで上記Z n(C+−+ 3)tの2倍の
モル供給量になるように流量制御して、これらを混合し
、バルブ7cを通して導入管2へ供給する。■ H, it came out of gas cylinder 13! ], the flow rate of the gas is controlled by the mass flow controller 12c, and the gas is bubbled in the bubbler 8. That is, 12. n(CH3) t to H2
is transported using the bubble method as a carrier gas. H.C.Q.
The mass flow controller 12b controls the flow rate of the HC & gas discharged from the gas cylinder 14 so that the molar supply amount is twice the above Z n (C + - + 3) t, mixes them, and supplies them to the introduction pipe 2 through the valve 7 c. supply
■ H、Sガスを予めH2ガスで希釈したものをガスボ
ンベ15から出し、マスフローコントローラ12aで上
記Zn(CH3)zと同じモル供給量になるように流量
制御して、バルブ7bを通して直接に反応管1の枝管1
aへ供給する。■ H, S gases diluted in advance with H2 gas are discharged from the gas cylinder 15, the flow rate is controlled by the mass flow controller 12a so that the molar supply amount is the same as that of Zn(CH3)z, and the gases are directly supplied to the reaction tube through the valve 7b. 1 branch pipe 1
Supply to a.
■ H,ガスボンベ13から出たH、ガスをマスフロー
コントローラ12eで流量制御して、バブラlO内でバ
ブルする。ずなわち、TCMをH。(2) The flow rate of the H gas discharged from the H gas cylinder 13 is controlled by the mass flow controller 12e, and the H gas is bubbled in the bubbler lO. In other words, TCM is H.
をキャリアガスとしてバブル法により輸送する。is transported using the bubble method as a carrier gas.
■〜ICρガスボンベ14から出たHCQ、ガスをマス
フローコントローラ12dで上記TCMの2倍のモル供
給量になるように流1制御して、これらを混合し、バル
ブ7aを通して導入管3へ供給する。(2) ~ ICρ The flow of HCQ and gas discharged from the gas cylinder 14 is controlled by the mass flow controller 12d so that the molar supply amount is twice that of the TCM, mixed, and supplied to the introduction pipe 3 through the valve 7a.
■ 上記■のZn(CH3)zおよび■のTCMは高温
で不安定な材料であって、それぞれ約400℃、約50
0℃以上になると熱分解する性質を有している。そのた
めそれぞれ分解して単体のZn。■ Zn(CH3)z (■) and TCM (■) are unstable materials at high temperatures, about 400℃ and 50℃, respectively.
It has the property of thermally decomposing at temperatures above 0°C. Therefore, each is decomposed into a single piece of Zn.
Mnが生じる。この単体Zn、Mnは導入管3.2の内
部でそれぞれ共に供給されたHC&ガスと直ちに反応す
る。次の(1)、(2)に示す反応式に従って、より高
い蒸気圧を有するZnCL、MnCLが生じる。Mn is produced. These simple substances Zn and Mn immediately react with the HC and gas supplied together inside the introduction pipe 3.2. According to the reaction formulas shown in the following (1) and (2), ZnCL and MnCL having higher vapor pressure are produced.
Zn+2 HCQ”ZnCQt+Hz −(1
)Mn+2HCf2→MnC12t+Ht ・=
(2)■ ■において導入管3.2の内部に生じたZn
CQ t 、 M n C(! を蒸気と、■において
直接に枝管1aに供給したH t Sガスは、反応管l
の他端で排気しているので、上記反応管l内を上記他端
の方へ流れる。これらは上記導入管3.2の先端と上記
他端との間の反応域にて化学反応を起こし、基板5上に
発光膜であるZnS:Mnを堆積させる。Zn+2 HCQ”ZnCQt+Hz −(1
)Mn+2HCf2→MnC12t+Ht ・=
(2) ■ Zn generated inside the introduction pipe 3.2 in ■
CQ t , M n C(!) as steam, and H t S gas directly supplied to the branch pipe 1a in
Since the other end is evacuated, the reaction tube 1 flows toward the other end. These cause a chemical reaction in the reaction zone between the tip of the introduction tube 3.2 and the other end, and deposit ZnS:Mn, which is a light emitting film, on the substrate 5.
このようにして、発光膜を成長した場合、■原材料のZ
n輸送速度と上記発光膜の成長速度の関係は第2図に示
すようになる。上記成長速度はZn輸送速度にほぼ比例
して増大しているので、膜成長過程が材料の供給律速に
基づくものであることを示すと共に、輸送量を調節する
ことによって膜厚の制御か容易に行えることを示してい
る。また、上記Zn輸送潰を一定値1 x 10−’m
o12/minとした場合、発光中心となるMnの輸送
速度と上記エレクトロルミネッセンス発光膜中のM n
aflJとの関係は、第3図に示すようになる。上記
Mn濃度はMn輸送速度5 x l O−8mo12/
l1lin付近から急速に増加し始めている。この原因
については、質屯分析計によるガス組成の測定から、M
n輸送速度を増大させると、反応管l内に同時に輸送さ
れるl−1c&ガスの分圧が高くなり、上記基板5上に
堆積した発光膜中のZnが上記HCl2ガスによってエ
ツチングされて、結果的にMnのドーピング率がMn輸
送速度に比例しなくなるためであることが判明している
。When a luminescent film is grown in this way, ■ Z of the raw material
The relationship between the n transport rate and the growth rate of the light emitting film is shown in FIG. The above growth rate increases almost in proportion to the Zn transport rate, indicating that the film growth process is rate-limited by material supply, and that the film thickness can be easily controlled by adjusting the transport rate. It shows that it can be done. In addition, the above Zn transport collapse is set to a constant value of 1 x 10-'m
o12/min, the transport speed of Mn, which is the luminescent center, and the Mn in the electroluminescent film
The relationship with aflJ is as shown in FIG. The above Mn concentration is Mn transport rate 5 x l O-8mol12/
It begins to increase rapidly from around l1lin. The cause of this can be determined from the measurement of gas composition using a mass spectrometer.
When the n transport speed is increased, the partial pressure of the l-1c & gas simultaneously transported into the reaction tube l increases, and the Zn in the luminescent film deposited on the substrate 5 is etched by the HCl2 gas, resulting in It has been found that this is because the Mn doping rate is no longer proportional to the Mn transport rate.
薄膜EL素子の発光膜を上記方法によって、Zn輸送速
速度 X l O−’IIIo(/min、Mn輸送速
度8XlO−”mo(17minにて成長して膜厚が0
.6μm、Mn濃度0.4at%の場合に、代表的な発
光輝度−印加電圧特性および発光効率−印加電圧特性は
第4図に示すようになる。この場合、発光の開始電圧1
60V、最大発光輝度3000 Cd/m’、最大発光
効率4Qm/wである。従来のノーライドCVD法によ
って発光膜を成長する場合と同様に良好な特性が得られ
ている。The light-emitting film of the thin film EL device was grown by the above method at a Zn transport rate of X l O-'IIIo (/min) and a Mn transport rate of 8XlO-'mo (17 min) to a film thickness of 0.
.. In the case of 6 μm and Mn concentration of 0.4 at%, typical luminance luminance-applied voltage characteristics and luminous efficiency-applied voltage characteristics are shown in FIG. In this case, the starting voltage for light emission is 1
60V, maximum luminance of 3000 Cd/m', and maximum luminous efficiency of 4Qm/w. Good characteristics are obtained as in the case where a light emitting film is grown by the conventional noride CVD method.
また、この発明を実施できるように大面積の発光膜形成
用に設計した縦型ノーライドCVD装置を第5図に示す
。反応管lは内径28cm、高さ70cmの石英製であ
り、上部に原料導入用細管21a、21b、21cを備
えている。基板25設置部と原料導入用細管21a、2
1cの箇所に電気炉22.2423をそれぞれ備えてい
る。上記基板25は、最大サイズ9インチのものまで設
置できるように設計してあり、発光膜成長中は、ホルダ
26にセットして基板回転用モータ27により終始回転
するようにしである。上記縦型ハライドCVD装置によ
って発光膜を成長する場合、反応ガスの流れが上記基板
25に回転対称的であり、しかも基板25は回転してい
るので、膜厚の面内分布・発光膜の分布の均一性を向上
させることができる。すなわち、大面積で特性良好な発
光膜を成長することができる。Further, FIG. 5 shows a vertical no-ride CVD apparatus designed for forming a large-area light-emitting film so as to be able to carry out the present invention. The reaction tube 1 is made of quartz and has an inner diameter of 28 cm and a height of 70 cm, and is equipped with thin tubes 21a, 21b, and 21c for introducing raw materials at the upper part. Substrate 25 installation part and raw material introduction thin tubes 21a, 2
Electric furnaces 22 and 2423 are provided at locations 1c, respectively. The substrate 25 is designed so that it can be installed up to a maximum size of 9 inches, and is set in a holder 26 and rotated by a substrate rotation motor 27 throughout the growth of the luminescent film. When growing a light-emitting film using the vertical halide CVD apparatus, the flow of the reaction gas is rotationally symmetrical to the substrate 25, and the substrate 25 is rotating, so the in-plane distribution of film thickness and the distribution of the light-emitting film uniformity can be improved. That is, it is possible to grow a light-emitting film with a large area and good characteristics.
以上より明らかなように、この実施例はソース材料を蒸
気あるいはガスの状態で供給しているので、ソース材料
を加熱する必要がない。また、これらは常温で十分に蒸
気圧が高いので、輸送途中で凝縮したりするようなこと
がなく、そのためマスフローコントローラによって精密
に流量制御すなわち輸送里制御することができる。した
がって気相成長装置を小型・簡略することができる。As is clear from the above, in this embodiment, the source material is supplied in the form of vapor or gas, so there is no need to heat the source material. Furthermore, since these materials have sufficiently high vapor pressure at room temperature, they do not condense during transportation, and therefore, the mass flow controller can precisely control the flow rate, that is, the transportation distance. Therefore, the vapor phase growth apparatus can be made smaller and simpler.
なお、この実施例では、■族元素Znの有機化合物とし
てZn(C10)zを使用したが、これに限るものでは
なくノエチル亜鉛Zn(CtHs)tでもよい。また上
記■族元素Znは他の■族元素で6よい。また、発光中
心となる元素Mnの有機化合物としてTCMを使用した
が、ジπンクロペンタノエニルマンガンMn(CtH6
)2でらよい。また上記発光中心となる元素は他の発光
中心となる元素でもよく、VI族元素Sも他の■族元素
でもよい。In this example, Zn(C10)z was used as the organic compound of group (I) element Zn, but the present invention is not limited to this, and noethylzinc Zn(CtHs)t may also be used. Further, the above-mentioned group (2) element Zn may be any other group (6) element. In addition, TCM was used as an organic compound of the element Mn, which is the luminescent center, but di-cyclopentanoenylmanganese Mn (CtH6
) 2 is fine. Further, the element serving as the luminescence center may be another element serving as the luminescence center, and the Group VI element S may also be another Group Ⅰ element.
また、上記反応管l内の高温部の温度はZnのものは3
00〜600℃、Mnのちは500〜700℃、基板の
温度は400〜600°Cの範囲が適当である。In addition, the temperature of the high temperature part in the reaction tube 1 is 3.
Suitably, the temperature range is 00 to 600°C, 500 to 700°C for Mn, and 400 to 600°C for the substrate.
ソース材料の輸送速度は反応管の断面積に依存するが、
ZnおよびSの場合は1o−5〜to−2mOQ/n+
in、 Mnの場合は10−”〜I O−3mol/m
inの範囲が適当である。そして、上記発光膜の成長時
間は、その膜厚が0.3〜1μmとなるように成長速度
によって調節するのが望ましい。The transport rate of the source material depends on the cross-sectional area of the reaction tube;
For Zn and S, 1o-5~to-2mOQ/n+
in, in the case of Mn, 10-”~I O-3 mol/m
A range of in is appropriate. The growth time of the luminescent film is desirably adjusted by the growth rate so that the film thickness is 0.3 to 1 μm.
さらに、上記実施例は、■族元素、VI族元索1発光中
心となる元素のいずれの化合物も蒸気あるいはガス状態
のソース材料を使用したが、これらのうち一部は他の状
態のものを使用しても良い。Furthermore, in the above embodiments, source materials in the vapor or gas state were used for the compounds of Group Ⅰ elements and Group VI elements serving as the luminescence centers, but some of them were in other states. May be used.
〈発明の効果〉
以上より明らかなように、この発明のエレクトロルミネ
ッセンス発光膜の気相成長方法は、形成する発光膜が高
品質で大面積化可能・量産性に優れたハライドCVD法
において、■族元素、VI族元素、■族元素の化合物、
VI族元素の化合物1発光中心となる元素および発光中
心となる元素の化合物のうち少なくとも一つを有機化合
物の蒸気の形態で反応管へ導入しているので、ソース材
料を加熱する必要がなく、輸送量の制御が容易で、しか
も小型・簡略な装置で行うことができる。<Effects of the Invention> As is clear from the above, the method of vapor phase growth of an electroluminescent film of the present invention has two advantages over the halide CVD method, which produces a high-quality light-emitting film, can be formed in a large area, and is excellent in mass production. Compounds of group elements, group VI elements, group ■ elements,
Compound 1 of Group VI Elements Since at least one of the element serving as the luminescent center and the compound of the element serving as the luminescent center is introduced into the reaction tube in the form of organic compound vapor, there is no need to heat the source material. It is easy to control the amount of transportation, and it can be done with a small and simple device.
第1図はこの発明の一実施例に使用する横型気相成長装
置の構成図、第2図は上記実施例により形成したエレク
トロルミネッセンス発光膜の成長速度とZn輸送速度と
の関係を示す図、第3図は発光膜中のMrJ度とMn輸
送速度との関係を示す図、第4図は上記実施例により形
成したエレクトロルミネッセンス発光膜を使用した薄膜
EL素子の代表的な発光輝度および発光効率の印加電圧
依存性を示す図、第5図は上記実施例に使用する縦型ハ
ライドCDV装置の構成図である。
1・・・反応管、la・・・枝管、2.3・・・導入管
、4 22.23.24・・・電気炉、5.25・・・
基板、6.26・・・基板ボルダ、7 a、 7 b、
7 c・・・バルブ、8.10・・・バブラ、9.11
・・・恒温槽、+ 2a、 l 2b、 12c、 l
2d、 I 2e−・−マスフローコントローラ、
3・・・I−1!ガスボンベ、14・・HC(ガスボン
ベ、5・・H,希釈のH、Sガスボンベ、
6.28・・・圧力計、17.29・・・主バルブ、8
.31・・油回転ポンプ、
]a、2 lb、21cm原料導入用細管、7・・基板
回転用モータ、
0・・メカニカルブースタポンプ。
許 出 願 人 シャープ株式会社
理 人 弁理士 青 山 葆 ほか1名第2図
Zn 咄速度[xlOmo!/min)第3図
Mn輸送遣崖
[xlOmol /min]
第4区
卯ズバコ電1i−じ!−クイ11
(V)FIG. 1 is a block diagram of a horizontal vapor phase growth apparatus used in an embodiment of the present invention, and FIG. 2 is a diagram showing the relationship between the growth rate and Zn transport rate of an electroluminescent film formed according to the above embodiment. FIG. 3 is a diagram showing the relationship between the MrJ degree and the Mn transport rate in the luminescent film, and FIG. 4 is a diagram showing typical luminescence brightness and luminous efficiency of a thin film EL device using the electroluminescent luminescent film formed according to the above example. FIG. 5 is a block diagram of a vertical halide CDV apparatus used in the above embodiment. 1... Reaction tube, la... Branch pipe, 2.3... Introduction tube, 4 22.23.24... Electric furnace, 5.25...
Substrate, 6.26... Substrate boulder, 7 a, 7 b,
7 c... Valve, 8.10... Bubbler, 9.11
・・・Thermostat, + 2a, l 2b, 12c, l
2d, I 2e--mass flow controller, 3...I-1! Gas cylinder, 14...HC (gas cylinder, 5...H, dilution H, S gas cylinder, 6.28...pressure gauge, 17.29...main valve, 8
.. 31...Oil rotary pump, ]a, 2 lb, 21cm thin tube for introducing raw material, 7... Motor for substrate rotation, 0... Mechanical booster pump. Applicant: Sharp Co., Ltd. Patent attorney: Aoyama Aoyama and one other person Figure 2 Zn Mushing speed [xlOmo! /min) Figure 3 Mn transport cliff [xlOmol /min] District 4 Uzubakoden 1i-ji! -Qui 11 (V)
Claims (1)
レクトロルミネッセンス素子用基板を配置して所定温度
に保持し、この基板表面に、II−VI族半導体を構成しう
るII族元素またはII族元素の化合物とVI族元素またはV
I族元素の化合物と、II−VI族半導体中で発光中心とな
る元素のハロゲン化物とを各々蒸気の状態で同時に輸送
して接触させることにより、上記基板にII−VI族半導体
を母体とし、この半導体内部に発光中心となる元素が含
有されたエレクトロルミネッセンス発光膜の気相成長方
法であって、 上記II族元素、VI族元素、II族元素の化合物、VI族元素
の化合物、発光中心となる元素および発光中心となる元
素の化合物のうち少なくとも一つについて有機化合物の
蒸気の状態で上記反応管へ導入して、上記反応管内に設
けた高温部において、この有機化合物を、熱分解反応に
より、II族元素、VI族元素および発光中心となる元素の
うちの少なくとも一つの元素、または上記II族元素、V
I族元素または発光中心となる元素のうちの少なくとも
一つの元素の無機化合物となすと共に、上記高温部にお
いて、上記元素や上記無機化合物と、ハロゲン化水素ガ
スとを混合して、化学反応によりII族元素またはVI族元
素または発光中心となる元素のハロゲン化物の蒸気を生
成した後、この蒸気を基板上へ供給することを特徴とす
るエレクトロルミネッセンス発光膜の気相成長法。(1) An electroluminescent element substrate is placed in a hydrogen or inert gas atmosphere in a reaction tube, maintained at a predetermined temperature, and a group II element or a group II element that can constitute a group II-VI semiconductor is placed on the surface of the substrate. Compounds of elements and group VI elements or V
By simultaneously transporting a compound of a group I element and a halide of an element that is a luminescent center in a group II-VI semiconductor in a vapor state and bringing them into contact with each other, the group II-VI semiconductor is used as a matrix on the substrate, This is a vapor phase growth method for an electroluminescent light-emitting film containing an element serving as a luminescent center inside the semiconductor, the method comprising: At least one of an element and a compound of an element serving as a luminescent center is introduced into the reaction tube in the form of an organic compound vapor, and this organic compound is subjected to a thermal decomposition reaction in a high temperature section provided in the reaction tube. , at least one element selected from a group II element, a group VI element, and an element serving as a luminescent center, or the above group II element, V
In addition to forming an inorganic compound of at least one element among Group I elements or elements serving as a luminescent center, the above element or the above inorganic compound is mixed with hydrogen halide gas in the high temperature section, and a chemical reaction is performed to produce II 1. A vapor phase growth method for an electroluminescent film, which comprises generating a vapor of a group element, a group VI element, or a halide of an element serving as a luminescence center, and then supplying this vapor onto a substrate.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63304820A JPH0752669B2 (en) | 1988-11-30 | 1988-11-30 | Vapor growth method of electroluminescent light-emitting film |
| US07/442,634 US5087531A (en) | 1988-11-30 | 1989-11-29 | Electroluminescent device |
| US07/779,235 US5356657A (en) | 1988-11-30 | 1991-10-18 | Method of manufacturing an electroluminescent device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63304820A JPH0752669B2 (en) | 1988-11-30 | 1988-11-30 | Vapor growth method of electroluminescent light-emitting film |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02152191A true JPH02152191A (en) | 1990-06-12 |
| JPH0752669B2 JPH0752669B2 (en) | 1995-06-05 |
Family
ID=17937647
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63304820A Expired - Fee Related JPH0752669B2 (en) | 1988-11-30 | 1988-11-30 | Vapor growth method of electroluminescent light-emitting film |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0752669B2 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5116640A (en) * | 1989-10-24 | 1992-05-26 | Sharp Kabushiki Kaisha | Process for preparing an electroluminescent device |
| JPH04248292A (en) * | 1991-01-24 | 1992-09-03 | Fuji Electric Co Ltd | Formation method of luminous membrane of electro-luminescence display panel |
| JPH0817575A (en) * | 1994-04-26 | 1996-01-19 | Nippondenso Co Ltd | Manufacture of electoluminescent element and manufacturing device therefor |
| US6004618A (en) * | 1994-04-26 | 1999-12-21 | Nippondenso., Ltd. | Method and apparatus for fabricating electroluminescent device |
-
1988
- 1988-11-30 JP JP63304820A patent/JPH0752669B2/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5116640A (en) * | 1989-10-24 | 1992-05-26 | Sharp Kabushiki Kaisha | Process for preparing an electroluminescent device |
| JPH04248292A (en) * | 1991-01-24 | 1992-09-03 | Fuji Electric Co Ltd | Formation method of luminous membrane of electro-luminescence display panel |
| JPH0817575A (en) * | 1994-04-26 | 1996-01-19 | Nippondenso Co Ltd | Manufacture of electoluminescent element and manufacturing device therefor |
| US6004618A (en) * | 1994-04-26 | 1999-12-21 | Nippondenso., Ltd. | Method and apparatus for fabricating electroluminescent device |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0752669B2 (en) | 1995-06-05 |
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