JP3441876B2 - Method for manufacturing light receiving member - Google Patents
Method for manufacturing light receiving memberInfo
- Publication number
- JP3441876B2 JP3441876B2 JP04152796A JP4152796A JP3441876B2 JP 3441876 B2 JP3441876 B2 JP 3441876B2 JP 04152796 A JP04152796 A JP 04152796A JP 4152796 A JP4152796 A JP 4152796A JP 3441876 B2 JP3441876 B2 JP 3441876B2
- Authority
- JP
- Japan
- Prior art keywords
- support
- container
- heating
- gas
- auxiliary member
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/50—Photovoltaic [PV] energy
Landscapes
- Photoreceptors In Electrophotography (AREA)
- Chemical Vapour Deposition (AREA)
- Photovoltaic Devices (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、プラズマCVD法
により、上に機能性堆積膜、特に電子写真用感光体、光
起電力デバイス、画像入力用ラインセンサー、撮像デバ
イス、TFT等の半導体素子として好適に利用できる、
結晶質、または非単結晶質半導体を連続的に形成する改
良された堆積膜形成方法に関するものである。特に本発
明は、電子写真感光体のような大面積の堆積膜を形成す
るための連続生産装置での製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a semiconductor device such as a functionally deposited film, especially a photoconductor for electrophotography, a photovoltaic device, a line sensor for image input, an image pickup device, and a TFT, which are formed by a plasma CVD method. Can be used suitably,
The present invention relates to an improved deposited film forming method for continuously forming a crystalline or non-single crystalline semiconductor. In particular, the present invention relates to a manufacturing method in a continuous production apparatus for forming a large-area deposited film such as an electrophotographic photosensitive member.
【0002】[0002]
【従来の技術の説明】従来、半導体デバイス、電子写真
用感光体、画像入力用ラインセンサー、撮像デバイス、
光起電力デバイス、その他各種エレクトロニクス素子、
光学素子等に用いる素子部材として、アモルファスシリ
コン、例えば水素または/及びハロゲン(例えばフッ
素、塩素等)で補償されたアモルファスシリコン[以
下、A−Si(H,X)と略記する]のような非単結晶
質の堆積膜またはダイヤモンド薄膜のような結晶質の堆
積膜が提案され、その中のいくつかは実用に供されてい
る。そして、こうした堆積膜は、プラズマCVD法、す
なわち、直流または高周波、あるいはマイクロ波による
グロー放電によって原料ガスを分解し、堆積膜をガラ
ス、石英、耐熱性合成樹脂フィルム、ステンレス、アル
ミニウムなどの支持体上に形成させる方法により形成さ
れ、そのための装置も各種提案されている。Description of the Related Art Conventionally, semiconductor devices, electrophotographic photoconductors, image input line sensors, image pickup devices,
Photovoltaic device, other various electronic elements,
As an element member used for an optical element or the like, a non-crystalline material such as amorphous silicon, for example, amorphous silicon compensated with hydrogen or / and halogen (eg, fluorine, chlorine, etc. [hereinafter, abbreviated as A-Si (H, X)]) is used. Single crystalline deposited films or crystalline deposited films such as diamond thin films have been proposed, some of which have been put to practical use. Then, such a deposited film is decomposed into a raw material gas by a plasma CVD method, that is, a glow discharge by a direct current, a high frequency, or a microwave, and the deposited film is formed of a support such as glass, quartz, a heat resistant synthetic resin film, stainless steel, or aluminum. It is formed by the method of forming on the above, and various apparatuses for it are proposed.
【0003】例えば、図1は高周波プラズマCVD法
(以後「PCVD」と略記する)による電子写真用感光
体の連続生産装置の一例を示す模式的な構成図である。
図1に示す生産装置の構成は以下の通りである。この装
置は大別すると、支持体投入容器(1100)、支持体
加熱装置(1200)、反応装置(1300)、支持体
冷却及び排出装置(1400)、これらの容器間で移動
可能な搬送専用の装置(1900)から構成されてい
る。各装置の真空容器(1101、1201、1301
a〜c、1401、1901)には容器内を真空にする
為の排気手段(1501〜1507)、排気バルブ(1
601〜1607)、各真空容器は接続可能な開閉ゲー
ト(1801〜1807)が設置されている。また、支
持体投入容器(1101)は、容器内を大気に戻す為の
リークバルブ(1701)が設けられている。支持体加
熱容器(1201)には、加熱時に使用するガスを流入
させる為の補助バルブ(1702)があり、支持体冷却
及び排出容器(1401)は、容器内を大気に戻す為の
リークバルブ(1705)が設けられている。反応容器
(1301a〜c)は、反応ガス流出バルブ(1703
a〜c、1704)、高周波マッチングボックス(図示
せず)が接続されている。搬送専用の真空容器には、容
器内を真空にする為の排気バルブ(1607)、ゲート
間を真空にする為の排気バルブ(1608)、ゲート間
を大気に戻す為のリークバルブ(1706)、支持体チ
ャッキング(1951)、移動用レール(1952)が
設けられている。支持体投入容器(1101)、加熱容
器(1201)、反応容器(1301a〜c)、冷却及
び取り出し容器(1401)の数は、それぞれの処理時
間により無駄の無いようにその数の組み合わせが選択さ
れる。また、搬送専用の真空容器(1901)は、同時
に複数の支持体を移送出来るように複数個でも可能で、
搬送装置(1900)は直線移動方式、円周方向の移動
でも可能である。For example, FIG. 1 is a schematic configuration diagram showing an example of a continuous production apparatus for electrophotographic photoreceptors by a high frequency plasma CVD method (hereinafter abbreviated as "PCVD").
The structure of the production apparatus shown in FIG. 1 is as follows. This device is roughly classified into a support charging container (1100), a support heating device (1200), a reaction device (1300), a support cooling and discharging device (1400), and a dedicated transfer device that can move between these containers. It is composed of a device (1900). Vacuum container (1101, 1201, 1301) of each device
a to c, 1401, and 1901), exhaust means (1501 to 1507) for evacuating the inside of the container, exhaust valve (1
Opening / closing gates (1801 to 1807) that can be connected to each vacuum container are installed. The support charging container (1101) is provided with a leak valve (1701) for returning the inside of the container to the atmosphere. The support heating container (1201) has an auxiliary valve (1702) for introducing gas used for heating, and the support cooling and discharge container (1401) has a leak valve (for returning the inside of the container to the atmosphere). 1705) is provided. The reaction vessel (1301a-c) is provided with a reaction gas outflow valve (1703).
a to c, 1704) and a high frequency matching box (not shown) are connected. The transfer-dedicated vacuum container includes an exhaust valve (1607) for creating a vacuum inside the container, an exhaust valve (1608) for creating a vacuum between the gates, and a leak valve (1706) for returning the space between the gates to the atmosphere. A support chucking (1951) and a moving rail (1952) are provided. The number of the support input container (1101), the heating container (1201), the reaction containers (1301a to 1301c), the cooling and taking out container (1401) is selected so that there is no waste depending on the processing time. It Further, a plurality of vacuum containers (1901) dedicated to transfer can be provided so that a plurality of supports can be transferred at the same time.
The transfer device (1900) may be a linear movement type or a movement in the circumferential direction.
【0004】こうした、連続生産装置では、操作は例え
ば以下のように行う。In such a continuous production apparatus, the operation is performed as follows, for example.
【0005】支持体投入容器(1101)に支持体を投
入し容器内を徐々に大気圧から所定の真空度になるまで
排気する。所定の真空度に到達したら、搬送専用の真空
容器(1901)を用い、真空の支持体加熱容器(12
01)に移送し、加熱用ガスを補助バルブ(1702)
から所定の圧力になる様に流し、容器内に設置されてい
るヒーター(図示せず)を用い、所定の温度に加熱す
る。加熱された支持体は搬送専用の真空容器(190
1)を用い、真空の反応容器(1301a〜c)内へ移
送される。反応容器内で所定の手段により堆積膜を形成
し、その後、真空の冷却及び排出容器(1401)に移
送され、所定の温度になるまで冷却されたのち、リーク
バルブ(1705)からリーク用ガスを大気圧になるま
で流し、その後排出する。A support is put into a support feeding container (1101), and the inside of the container is gradually evacuated from atmospheric pressure to a predetermined vacuum degree. When a predetermined degree of vacuum is reached, a vacuum container (1901) dedicated to transportation is used, and a vacuum support heating container (12) is used.
01) to transfer the heating gas to the auxiliary valve (1702)
From above to a predetermined pressure, and heated to a predetermined temperature using a heater (not shown) installed in the container. The heated support is a vacuum container (190
1) and transferred into a vacuum reaction container (1301a-c). A deposited film is formed by a predetermined means in the reaction container, and then the film is transferred to a vacuum cooling and discharge container (1401) and cooled to a predetermined temperature, and then a leak gas is leaked from a leak valve (1705). Flow until atmospheric pressure, then discharge.
【0006】各真空容器(1101、1201、130
1a〜c、1401)と搬送専用の真空容器(1901)
間での支持体の受け渡しは、まず、搬送装置(190
0)が、取り出す真空容器上に移動し、ゲート(180
7)を取り出す真空容器のゲート(1801〜1806
のいずれか)に接続させる。その後排気手段 (150
7)、排気バルブ(1608)にてゲート間を真空にす
る。尚、真空容器(1901)内が所定の真空度で無い
場合は、排気バルブ(1607)にて真空引きを行な
う。ゲート間が所定の真空度になったら、双方のゲート
を開き、支持体の受け渡しを行なう。受け渡し終了後、
双方のゲートは閉され、ゲート間リークバルブ(170
6)からリーク用ガスを流し、ゲート間を大気圧にす
る。その後、搬送専用の真空容器(1901)のゲート
(1807)は切り離され、搬送装置(1900)は次
工程へ移動する。尚、支持体の受け渡しはチャッキング
(1951)を用いて行なわれる。これらの工程は全て
自動制御によって行なわれる。Each vacuum container (1101, 1201, 130)
1 a to c, 1401) and dedicated to carrying the vacuum container (1901)
In order to transfer the support between the
0) moves onto the vacuum container to be taken out, and the gate (180
7) The gate (1801-1806) of the vacuum container for taking out
One of the above). After that, exhaust means (150
7) A vacuum is applied between the gates by the exhaust valve (1608). When the inside of the vacuum container (1901) is not at a predetermined degree of vacuum, the exhaust valve (1607) evacuates. When the degree of vacuum between the gates reaches a predetermined level, both gates are opened to transfer the support. After delivery,
Both gates are closed and the gate-to-gate leak valve (170
The gas for leak is made to flow from 6), and atmospheric pressure is applied between the gates. After that, the gate (1807) of the vacuum container (1901) dedicated to transfer is cut off, and the transfer device (1900) moves to the next step. The transfer of the support is performed using chucking (1951). All of these steps are performed by automatic control.
【0007】反応容器について図2の反応装置の模式的
な構成図を用いて更に詳細に説明すると、堆積装置(2
100)、原料ガスの供給装置(2200)、開閉ゲー
ト(2120)、反応容器(2111)内を減圧にする
ための排気装置(図示せず)から構成されている。堆積
装置(2100)中の反応容器(2111)内には支持
体(2112)、支持体加熱用ヒーター(2113)、
原料ガス導入管(2114)が設置され、更に高周波マ
ッチングボックス(2115)が接続されている。The reaction vessel will be described in more detail with reference to the schematic configuration diagram of the reaction apparatus shown in FIG.
100), a source gas supply device (2200), an opening / closing gate (2120), and an exhaust device (not shown) for reducing the pressure inside the reaction vessel (2111). A support (2112), a heater for heating the support (2113), a reaction vessel (2111) in the deposition apparatus (2100),
A raw material gas introduction pipe (2114) is installed, and a high frequency matching box (2115) is further connected.
【0008】原料ガス供給装置(2200)は、SiH
4 、GeH4 、H2 、CH4 、B2H6 、PH3 等の原
料ガスのボンベ(2221〜2226)とバルブ(22
31〜2236、2241〜2246、2251〜22
56)およびマスフローコントローラー(2211〜2
216)から構成され、各原料ガスのボンベはバルブ
(2260)を介して反応容器(2111)内のガス導
入管(2114)に接続されている。The source gas supply device (2200) is made of SiH.
4 , GeH 4 , H 2 , CH 4 , B 2 H 6 , PH 3 and other source gas cylinders (2212-1226) and valves (22)
31-2236, 2241-2246, 2251-22
56) and a mass flow controller (2211-2)
216), and the cylinder of each source gas is connected to the gas introduction pipe (2114) in the reaction vessel (2111) via the valve (2260).
【0009】こうした堆積膜形成装置を用いた堆積膜の
形成は、例えば以下のように行なわれる。Formation of a deposited film using such a deposited film forming apparatus is performed, for example, as follows.
【0010】まず、排気手段(図示せず)により真空に
排気された反応容器(2111)内に所定の温度に加熱
された支持体(2112)を搬送専用の真空容器(図示
せず)により開閉ゲート(2120)を介して投入し、
支持体加熱用ヒーター(2113)により支持体(21
12)の温度を所定の温度に制御する。First, a support (2112) heated to a predetermined temperature is opened / closed in a reaction container (2111) which is evacuated to a vacuum by an evacuation means (not shown) by a vacuum container (not shown) dedicated to transportation. Input through the gate (2120),
The support (2113) is heated by the heater (2113) for heating the support.
The temperature of 12) is controlled to a predetermined temperature.
【0011】堆積膜形成用の原料ガスを反応容器(21
11)に流入させるには、ガスボンベのバルブ(223
1〜2236)、反応容器のリークバルブ(2123)
が閉じられていることを確認し、又、流入バルブ(22
41〜2246)、流出バルブ(2251〜225
6)、補助バルブ(2260)が開かれていることを確
認して、まずメインバルブ(2118)を開いて反応容
器(2111)およびガス配管内(2116)を排気す
る。A raw material gas for forming a deposited film is supplied to a reaction vessel (21
11), the gas cylinder valve (223
1 to 2236), the leak valve of the reaction vessel (2123)
Make sure that the inlet valve (22
41 to 2246), the outflow valve (2251 to 225)
6) After confirming that the auxiliary valve (2260) is opened, first, the main valve (2118) is opened to exhaust the reaction vessel (2111) and the gas pipe (2116).
【0012】次に真空計(2124)の読みが約5×1
0-6Torrになった時点で補助バルブ(2260)、
流出バルブ(2251〜2256)を閉じる。Next, the reading of the vacuum gauge (2124) is about 5 × 1.
Auxiliary valve (2260) at 0 -6 Torr,
Close the outflow valves (2251-2256).
【0013】その後、ガスボンベ(2221〜222
6)より各ガスをバルブ(2231〜2236)を開い
て導入し、圧力調整器(2261〜2266)により各
ガス圧を2kg/cm2 に調整する。After that, the gas cylinders (2221-222)
From (6), each gas is introduced by opening the valves (2231-2236), and the pressure of each gas is adjusted to 2 kg / cm 2 by the pressure adjuster (2261-2266).
【0014】次に、流入バルブ(2241〜2246)
を徐々に開けて、各ガスをマスフローコントローラー
(2211〜2216)内に導入する。Next, the inflow valves (2241-2246)
Is gradually opened and each gas is introduced into the mass flow controller (2211 to 2216).
【0015】以上のようにして成膜の準備が完了した
後、以下の手順で各層の形成を行う。After the preparation for film formation is completed as described above, each layer is formed by the following procedure.
【0016】支持体(2112)が所定の温度になった
ところで流出バルブ(2251〜2256)のうちの必
要なものおよび補助バルブ(2260)を徐々に開き、
ガスボンベ(2221〜2226)から所定のガスをガ
ス導入管(2114)を介して反応容器(2111)内
に導入する。次にマスフローコントローラー(2211
〜2216)によって各原料ガスが所定の流量になるよ
うに調整する。その際、反応容器(2111)内の圧力
が1Torr以下の所定の圧力になるように真空計(2
124)の出力を参照してメインバルブ(2118)の
開口を調整する。内圧が安定したところで、周波数1
3.56MHzの高周波電源(不図示)を所望の電力に
設定して、高周波マッチングボックス(2115)を通
じて反応容器(2111)内に高周波電力を導入し、グ
ロー放電を生起させる。この放電エネルギーによって反
応容器内に導入された原料ガスが分解され、支持体(2
112)上に所定のシリコンを主成分とする堆積膜が形
成されるところとなる。所望の膜厚の形成が行なわれた
後、高周波電力の供給を止め、流出バルブを閉じて反応
容器へのガスの流入を止め、堆積膜の形成を終える。When the support (2112) reaches a predetermined temperature, the necessary ones of the outflow valves (2251-2256) and the auxiliary valve (2260) are gradually opened,
A predetermined gas is introduced from the gas cylinders (2212-1226) into the reaction container (2111) through the gas introduction pipe (2114). Next, mass flow controller (2211
.About.2216) so that each raw material gas is adjusted to have a predetermined flow rate. At that time, a vacuum gauge (2) is used so that the pressure inside the reaction vessel (2111) becomes a predetermined pressure of 1 Torr or less.
The opening of the main valve (2118) is adjusted with reference to the output of 124). When the internal pressure is stable, frequency 1
A high frequency power supply (not shown) of 3.56 MHz is set to a desired power, and high frequency power is introduced into the reaction vessel (2111) through the high frequency matching box (2115) to cause glow discharge. The source gas introduced into the reaction vessel is decomposed by this discharge energy, and the support (2
112) where a predetermined deposited film containing silicon as a main component is formed. After the desired film thickness is formed, the supply of the high frequency power is stopped, the outflow valve is closed to stop the gas from flowing into the reaction container, and the formation of the deposited film is completed.
【0017】同様の操作を複数回繰り返すことによっ
て、所望の多層構造の光受容層を形成することができ
る。By repeating the same operation a plurality of times, a desired light-receiving layer having a multilayer structure can be formed.
【0018】それぞれの層を形成する際には必要なガス
以外の流出バルブはすべて閉じられていることは言うま
でもなく、また、それぞれのガスが反応容器(211
1)内、流出バルブ(2251〜2256)から反応容
器(2111)に至る配管内に残留することを避けるた
めに、流出バルブ(2251〜2256)を閉じ、補助
バルブ(2260)を開き、さらにメインバルブ(21
18)を全開にして系内を一旦高真空に排気する操作を
必要に応じて行う。この間は、全て自動制御により行な
われるものである。Needless to say, all the outflow valves other than the necessary gas are closed when forming the respective layers, and the respective gases are supplied to the reaction vessel (211).
1) In order to avoid remaining in the pipe from the outflow valve (2251 to 2256) to the reaction vessel (2111), the outflow valve (2251 to 2256) is closed, the auxiliary valve (2260) is opened, and the main valve is further opened. Valve (21
If necessary, the operation of 18) is fully opened and the system is once evacuated to a high vacuum. During this period, all is performed by automatic control.
【0019】この様にして、電子写真感光体のような大
面積を有する堆積膜を形成する場合、膜厚、膜質の均一
化が必要であり、そのための装置構成も各種提案されて
いる。When a deposited film having a large area such as that of an electrophotographic photosensitive member is formed in this way, it is necessary to make the film thickness and film quality uniform, and various apparatus configurations have been proposed for that purpose.
【0020】例えば、特開昭58−101420号公報
によれば支持体を放電電極として用い一対の電極間に自
己電位を打ち消すような形にDCバイアスを印加する事
により、両電極から同時に、複数の均一で良好な特性を
有する堆積膜を得る方法が記載されている。For example, according to Japanese Patent Laid-Open No. 58-101420, a support is used as a discharge electrode and a DC bias is applied between a pair of electrodes so as to cancel a self-potential. A method for obtaining a deposited film with uniform and good properties of is described.
【0021】また特公平4−350171号公報には連
続移動可能な帯状部材を支持体及び放電空間に対し外壁
を形成する様に配置しDCバイアスを印加し、帯状部材
自体を加熱する事で欠陥の少ない均一な堆積膜の得る方
法が記載されている。しかしこれらの方法は堆積膜の形
成時に使用するものであり、加熱時に補助的な役割をす
るとの記載は一切ない。Further, in Japanese Examined Patent Publication No. 4-350171, a continuously movable strip-shaped member is arranged so as to form an outer wall with respect to a support and a discharge space, a DC bias is applied, and the strip-shaped member itself is heated. A method for obtaining a uniform deposited film with less loss is described. However, these methods are used at the time of forming a deposited film, and there is no description that they play an auxiliary role at the time of heating.
【0022】[0022]
【発明が解決しようとする課題】しかしながら、従来の
装置で作成された電子写真用感光体は、膜厚、膜質が均
一化され歩留の面で改善されてきたが、連続生産での特
性の安定化を図る上でさらに改良される余地が存在する
のが実状である。However, although the electrophotographic photosensitive member produced by the conventional apparatus has been improved in yield in terms of uniform film thickness and film quality, it has a characteristic of continuous production. The reality is that there is room for further improvement in terms of stabilization.
【0023】このような状況下において、前述した従来
技術により上記課題についてある程度の膜厚、膜質の均
一化が可能になってはきたが、更なる生産の安定性向上
に関しては未だ充分とはいえない。特にアモルファスシ
リコン系感光体の更なる高画質化への課題として、更
に、均一な膜を得ることとともに、連続生産における経
時的な膜厚変化による特性変化を起こさず、安定的に生
産を行なうことが挙げられる。Under such circumstances, although the film thickness and film quality can be made uniform to some extent by the above-mentioned conventional technique with respect to the above problems, it is still sufficient to further improve the stability of production. Absent. In particular, as a challenge to further improve the image quality of amorphous silicon-based photoconductors, it is necessary to obtain a uniform film and to perform stable production without causing characteristic changes due to changes in film thickness over time in continuous production. Is mentioned.
【0024】そのためには、反応空間内の放電の安定性
を確立することが必要であると同時に均一な堆積膜を得
る為の条件を更に詰めていく必要がある。特にアモルフ
ァスシリコン感光体の様に堆積膜の形成には支持体を加
熱する必要がある場合、支持体を均一な温度分布に維持
することは堆積膜に特性にも大きく影響する。そこでよ
り安定した温度分布が重要な要素となってくる。For that purpose, it is necessary to establish the stability of the discharge in the reaction space, and at the same time, it is necessary to further improve the conditions for obtaining a uniform deposited film. Especially when it is necessary to heat the support for forming the deposited film as in the case of the amorphous silicon photosensitive member, maintaining the support with a uniform temperature distribution greatly affects the properties of the deposited film. Therefore, more stable temperature distribution becomes an important factor.
【0025】[0025]
【発明の目的】本発明の主たる目的は、支持体の温度分
布の安定性を図り、膜厚および膜質が均一な堆積膜を定
常的に形成しうるプラズマCVD法による光受容部材の
連続生産方法を提供することにある。SUMMARY OF THE INVENTION The main object of the present invention is to provide a continuous production method of a photoreceptive member by a plasma CVD method, which can stabilize the temperature distribution of a support and can constantly form a deposited film having a uniform film thickness and film quality. To provide.
【0026】本発明の他の目的は、形成される膜の諸物
性、成膜速度、再現性の向上、膜の生産性を向上し、量
産化を行う場合その歩留まりを飛躍的に向上させる事を
可能にするプラズマCVD法による堆積膜連続生産方法
を提供することにある。Another object of the present invention is to improve various physical properties of a film to be formed, film formation speed, reproducibility, film productivity, and dramatically improve the yield in mass production. Another object of the present invention is to provide a method for continuously producing a deposited film by a plasma CVD method that enables the above.
【0027】[0027]
【課題を解決するための手段及び作用】本発明者らは、
従来の堆積膜形成方法における前述の問題を克服して、
前述の本発明の目的を達成すべく鋭意研究を重ねたとこ
ろ、特性の安定性は、支持体の温度に関する所が大きい
と言う知見を得た。Means and Actions for Solving the Problems The present inventors have
Overcoming the above-mentioned problems in the conventional deposited film forming method,
As a result of intensive studies to achieve the above-mentioned object of the present invention, it was found that the stability of the characteristics depends largely on the temperature of the support.
【0028】特に加熱工程と、成膜工程が離れているよ
うな連続生産装置の場合、加熱工程は全ての成膜工程に
おいて共通である為、加熱工程がスムーズに進む事が重
要であると同時に温度分布が毎回一定である必要があ
る。Particularly in the case of a continuous production apparatus in which the heating step and the film forming step are separated from each other, it is important that the heating step proceeds smoothly because the heating step is common to all the film forming steps. The temperature distribution needs to be constant every time.
【0029】支持体は機械搬送によって真空内移動とな
ることから、搬送中に温度分布にムラがあると温度の低
い部分と高い部分が打ち消し合い、加熱時と違った分布
になってしまう。このことから、支持体の温度分布の均
一性を効果的に得る手段として、加熱容器内に温度分布
がより均一になる補助部材を設ける事で加熱工程での温
度分布の均一化を図ることにより今まで以上に温度分布
の安定化が図れ、昇温速度も上りその結果、連続生産装
置でも、真空搬送時の温度変化を抑え、堆積される堆積
膜の膜質及び膜厚を常に均一にすることが出来た。また
加熱容器内の補助部材と支持体の距離を一定の範囲に設
定することで、連続生産装置での効果がより向上した。Since the support moves in a vacuum by mechanical transportation, if there is uneven temperature distribution during transportation, the low temperature portion and the high temperature portion cancel each other out, resulting in a distribution different from that during heating. From this fact, as a means for effectively obtaining the uniformity of the temperature distribution of the support, by providing an auxiliary member that makes the temperature distribution more uniform in the heating container, it is possible to make the temperature distribution uniform in the heating step. The temperature distribution can be stabilized more than ever, and the rate of temperature rise is also increased. As a result, even in continuous production equipment, the temperature change during vacuum transfer is suppressed, and the quality and thickness of the deposited film are always uniform. Was completed. Further, by setting the distance between the auxiliary member in the heating container and the support within a certain range, the effect in the continuous production apparatus was further improved.
【0030】即ち、特定の範囲の距離を保つ事で、堆積
される光受容部材の膜質及び膜厚の経時的変化をなくす
ことができ、連続生産での生産性を飛躍的に向上させる
ことを可能にすることが分かった。That is, by keeping the distance within a specific range, it is possible to eliminate the change with time in the film quality and film thickness of the deposited light receiving member, and it is possible to dramatically improve the productivity in continuous production. I found it possible.
【0031】本発明は、諸知見に基づいて完成に至った
もので光受容部材の製造にあたり、少なくとも支持体加
熱容器と堆積膜を形成するための反応容器及びこれらの
容器間で移動可能な搬送専用の真空容器とからなり、各
容器は接続可能な開閉ゲートを設け、前記支持体加熱容
器及び反応容器と前記搬送専用の真空容器との間で支持
体の出し入れ移動可能としたを備えた連続生産装置を用
い、前記支持体加熱容器内に加熱分布を均一にするため
の、支持体に対向する長手方向に開口部のない加熱補助
部材を設けて支持体の温度を高めた後、前記支持体を前
記反応容器内に搬送し、プラズマCVD法により堆積膜
を作ることを特徴とする新規な技術である。The present invention has been completed based on various findings, and at the time of manufacturing a light receiving member, at least a support heating container and a reaction container for forming a deposited film, and these
It consists of a vacuum container dedicated to transportation that can be moved between containers.
The container has a connectable open / close gate,
Between the reactor and reaction vessel and the vacuum vessel dedicated to the transfer
In order to make uniform the heat distribution in the support heating container, using a continuous production device equipped with movable body
After raising the temperature of the support body by providing a heating auxiliary member having no opening in the longitudinal direction facing the support body, the support body is placed in front of the support body.
The film is transferred into the reaction vessel and deposited by plasma CVD.
Is a new technology that is characterized by
【0032】[0032]
【発明の実施の形態】以下図面を用いて本発明について
詳述する。BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described in detail below with reference to the drawings.
【0033】図3は、本発明のプラズマCVD法による
光受容部材の製造装置における加熱容器内の支持体と加
熱用補助部材の配置を模式的に示す断面図である。図中
3111は加熱容器、3112は支持体、3113は支
持体加熱用ヒーター、3114はガス導入パイプ、31
15は加熱容器内に装着された加熱用補助部材、311
6はガス導入管、3117はリークバルブ、3118は
排気バルブ、3119は真空計、3120はゲートバル
ブ、3121はベース台、3122は絶縁リング、31
24は排気配管をそれぞれ示す。FIG. 3 is a sectional view schematically showing the arrangement of the support and the heating auxiliary member in the heating container in the apparatus for manufacturing a light receiving member by the plasma CVD method of the present invention. In the figure, 3111 is a heating container, 3112 is a support, 3113 is a heater for heating the support, 3114 is a gas introduction pipe, 31
15 is an auxiliary member for heating mounted in the heating container, 311
6 is a gas introduction pipe, 3117 is a leak valve, 3118 is an exhaust valve, 3119 is a vacuum gauge, 3120 is a gate valve, 3121 is a base stand, 3122 is an insulating ring, 31
Reference numerals 24 denote exhaust pipes, respectively.
【0034】従来装置においては、支持体は加熱用ガス
の雰囲気中に設置され加熱されるだけであった。しかし
その状態では電子写真感光体用に更なる特性向上が求め
られると、温度分布が電子写真特性に影響を及ぼしてし
まうと言う問題があった。こうした問題を解決する為、
ガス量や内圧の変更を行ない、連続生産での対応を図
り、ある程度改善されたものの、生産性等の問題でまだ
不十分である。In the conventional apparatus, the support was simply placed and heated in the atmosphere of the heating gas. However, in such a state, there is a problem that the temperature distribution will affect the electrophotographic characteristics if further improvement of the characteristics is required for the electrophotographic photosensitive member. To solve these problems,
Although the amount of gas and the internal pressure were changed and the continuous production was dealt with, and some improvements were made, productivity and other problems are still insufficient.
【0035】本発明では支持体投入容器、支持体加熱容
器、堆積膜を形成するための反応容器、支持体冷却及び
排出容器と、これらの容器間で移動可能な搬送専用の真
空容器とからなり、各容器は接続可能な開閉ゲートを設
け、前記支持体加熱容器及び反応容器と前記搬送専用の
真空容器との間で支持体の出し入れ移動可能とした連続
生産装置においては、前記支持体加熱容器内に設置され
た、支持体に対向する長手方向に開口部のない加熱補助
部材を設けた事により、支持体表面の温度分布を均一に
し、昇温速度を上げる事が出来、常に堆積される堆積膜
の膜質及び膜厚の均一化が図られることになる。The present invention comprises a support charging container, a support heating container, a reaction container for forming a deposited film , a support cooling and discharging container, and a vacuum container dedicated to the transfer which is movable between these containers. , Each container is provided with a connectable opening / closing gate, and is dedicated to the support heating container and the reaction container and the transport .
In a continuous production apparatus in which a support can be moved in and out of a vacuum container, a heating auxiliary member, which is installed in the support heating container and has no opening in the longitudinal direction facing the support, must be provided. As a result, the temperature distribution on the surface of the support can be made uniform and the rate of temperature rise can be increased, and the quality and thickness of the deposited film that is constantly deposited can be made uniform.
【0036】本発明において使用される熱緩衝性の補助
部材としては、熱伝導性の良い物であればいずれの素材
でも良いが特に、Al、Cr、Mo、Au、In、N
b、Te、V、Ti、Pt、Pd、Fe等の金属、およ
びこれらの合金、例えばステンレス等が挙げられる。ま
た、ポリエステル、ポリエチレン、ポリカーボネート、
セルロースアセテート、ポリプロピレン、ポリ塩化ビニ
ル、ポリスチレン、ポリアミド等の合成樹脂のフィルム
またはシート、ガラス、セラミック更にはアルミナ等が
本発明には適している。The heat buffering auxiliary member used in the present invention may be made of any material as long as it has a good thermal conductivity, but especially Al, Cr, Mo, Au, In, N.
Examples thereof include metals such as b, Te, V, Ti, Pt, Pd, and Fe, and alloys thereof, such as stainless steel. In addition, polyester, polyethylene, polycarbonate,
Films or sheets of synthetic resins such as cellulose acetate, polypropylene, polyvinyl chloride, polystyrene and polyamide, glass, ceramics and alumina are suitable for the present invention.
【0037】本発明に用いられる加熱用補助材の長手方
向の長さは加熱容器に納まれば良いが支持体の長手方向
の長さをLとし、加熱補助部材の長手方向の長さをYと
した時Yは好ましくは0.83L≦Y≦1.80L、最
適にはL≦Y≦1.40Lとするのが好ましい。The length in the longitudinal direction of the heating auxiliary material used in the present invention may be stored in the heating container, but the length in the longitudinal direction of the support is L, and the length in the longitudinal direction of the heating auxiliary member is Y. In this case, Y is preferably 0.83L ≦ Y ≦ 1.80L, and optimally L ≦ Y ≦ 1.40L.
【0038】本発明に用いられる加熱補助部材と支持体
の間隔については、支持体の外径をS、加熱補助部材の
外径をWとした時好ましくは1.1≦W/S≦3.0、
最適には1.2≦W/S≦2.5とするのが好ましい。The distance between the heating assisting member and the support used in the present invention is preferably 1.1≤W / S≤3, where S is the outer diameter of the support and W is the outer diameter of the heating assisting member. 0,
Optimally, it is preferable that 1.2 ≦ W / S ≦ 2.5.
【0039】本発明に用いられる加熱用のガスとして
は、加熱に適したガスであればいずれのガスでも良い
が、Ar、He、Ne、Xe等の不活性ガス、またはN
2 、H2等も本発明には有効である。The heating gas used in the present invention may be any gas as long as it is suitable for heating, but an inert gas such as Ar, He, Ne, Xe, or N.
2 , H 2, etc. are also effective in the present invention.
【0040】本発明において使用される支持体として
は、導電性でも電気絶縁性であってもよい。The support used in the present invention may be conductive or electrically insulating.
【0041】導電性支持体としては、Al、Cr、M
o、Au、In、Nb、Te、V、Ti、Pt、Pd、
Fe等の金属、およびこれらの合金、例えばステンレス
等が挙げられる。また、ポリエステル、ポリエチレン、
ポリカーボネート、セルロースアセテート、ポリプロピ
レン、ポリ塩化ビニル、ポリスチレン、ポリアミド等の
合成樹脂のフィルムまたはシート、ガラス、セラミック
等の電気絶縁性支持体の少なくとも光受容層を形成する
側の表面を導電処理した支持体も用いることができる。As the conductive support, Al, Cr, M
o, Au, In, Nb, Te, V, Ti, Pt, Pd,
Metals such as Fe, and alloys of these, such as stainless steel, may be mentioned. Also, polyester, polyethylene,
A support in which at least the surface of the electrically insulating support, such as a film or sheet of synthetic resin such as polycarbonate, cellulose acetate, polypropylene, polyvinyl chloride, polystyrene, or polyamide, glass, or ceramic, on which the light receiving layer is formed, is subjected to a conductive treatment. Can also be used.
【0042】本発明に於いて使用される支持体の形状は
平滑表面あるいは凹凸表面の円筒状または板状無端ベル
ト状であることができ、その厚さは、所望通りの電子写
真用感光体を形成し得るように適宜決定するが、電子写
真用感光体としての可撓性が要求される場合には、支持
体としての機能が充分発揮できる範囲内で可能な限り薄
くすることができる。しかしながら、支持体は製造上お
よび取り扱い上、機械的強度等の点から通常は10μm
以上とされる。The shape of the support used in the present invention may be a cylindrical or plate-like endless belt having a smooth surface or an uneven surface, and the thickness of the support may be a desired value for an electrophotographic photoreceptor. It is appropriately determined so that it can be formed, but when flexibility as an electrophotographic photoreceptor is required, it can be made as thin as possible within a range in which the function as a support can be sufficiently exhibited. However, the support is usually 10 μm in terms of manufacturing and handling, mechanical strength and the like.
That is all.
【0043】特にレーザー光などの可干渉性光を用いて
像記録を行う場合には、可視画像において現われる、い
わゆる干渉縞模様による画像不良をより効果的に解消す
るために、支持体の表面に凹凸を設けてもよい。支持体
の表面に設けられる凹凸は、特開昭60−168156
号公報、同60−178457号公報、同60−225
854号公報等に記載された公知の方法により作成され
る。In particular, when image recording is performed using coherent light such as laser light, in order to more effectively eliminate image defects due to so-called interference fringe patterns that appear in visible images, the surface of the support is You may provide unevenness. The unevenness provided on the surface of the support is disclosed in JP-A-60-168156.
No. 60-178457, No. 60-225.
It is created by a known method described in Japanese Patent Publication No. 854.
【0044】また、レーザー光などの可干渉光を用いた
場合の干渉縞模様による画像不良をより効果的に解消す
る別の方法として、支持体の表面に複数の球状痕跡窪み
による凹凸形状を設けてもよい。即ち、支持体の表面が
電子写真用感光体に要求される解像力よりも微少な凹凸
を有し、しかも該凹凸は、複数の球状痕跡窪みによるも
のである。支持体の表面に設けられる複数の球状痕跡窪
みによる凹凸は、特開昭61−231561号公報に記
載された公知の方法により作成される。Further, as another method for more effectively eliminating the image defect due to the interference fringe pattern when the coherent light such as laser light is used, the surface of the support is provided with a concavo-convex shape by a plurality of spherical trace depressions. May be. That is, the surface of the support has irregularities that are smaller than the resolving power required for the electrophotographic photoreceptor, and the irregularities are due to a plurality of spherical trace depressions. The unevenness due to the plurality of spherical trace depressions provided on the surface of the support is prepared by the known method described in JP-A-61-231561.
【0045】本発明の装置を用いて、グロー放電法によ
って堆積膜を形成するには、基本的にはシリコン原子
(Si)を供給し得るSi供給用の原料ガスと、水素原
子(H)を供給し得るH供給用の原料ガスまたは/及び
ハロゲン原子(X)を供給し得るX供給用の原料ガス
を、反応容器内に所望のガス状態で導入して、該反応容
器内にグロー放電を生起させ、あらかじめ所定の位置に
設置されてある所定の支持体上にa−Si:H,Xから
なる層を形成すればよい。In order to form a deposited film by the glow discharge method using the apparatus of the present invention, basically, a source gas for supplying Si capable of supplying silicon atoms (Si) and hydrogen atoms (H) are used. A raw material gas for H supply that can be supplied and / or a raw material gas for X supply that can supply a halogen atom (X) are introduced into the reaction vessel in a desired gas state, and glow discharge is performed in the reaction vessel. The layer made of a-Si: H, X may be formed on a predetermined support which has been raised and installed at a predetermined position in advance.
【0046】本発明において使用されるSi供給用ガス
となり得る物質としては、SiH4、Si2 H6 、Si3
H8 、Si4 H10等のガス状態の、またはガス化し得
る水素化珪素(シラン類)が有効に使用されるものとし
て挙げられ、更に層作成時の取り扱い易さ、Si供給効
率の良さ等の点でSiH4 、Si2 H6 が好ましいもの
として挙げられる。The substances which can be used as the Si supply gas in the present invention include SiH 4 , Si 2 H 6 and Si 3
Gaseous or gasifiable silicon hydrides (silanes) such as H 8 and Si 4 H 10 are mentioned as being effectively used. Further, they are easy to handle during layer formation, have good Si supply efficiency, etc. In this respect, SiH 4 and Si 2 H 6 are preferable.
【0047】そして、形成される堆積膜中に水素原子を
構造の構成中に導入し、水素原子の導入割合の制御をい
っそう容易になるようにはかり、本発明の目的を達成す
る膜特性を得るために、これらのガスに更にH2 および
/またはHeあるいは水素原子を含む珪素化合物のガス
も所要量混合して層形成するとよい。また、各ガスは単
独種のみでなく所定の混合比で複数種混合しても差し支
えないものである。Then, hydrogen atoms are introduced into the structure of the structure in the deposited film to be formed so that the introduction ratio of hydrogen atoms can be controlled more easily to obtain film characteristics that achieve the object of the present invention. Therefore, it is advisable to form a layer by mixing a required amount of H 2 and / or He or a silicon compound gas containing a hydrogen atom with these gases. Further, each gas may be mixed not only with one kind but also with plural kinds at a predetermined mixing ratio.
【0048】また本発明において使用されるハロゲン原
子供給用の原料ガスとして有効なのは、たとえばハロゲ
ンガス、ハロゲン化物、ハロゲン間化合物、ハロゲンで
置換されたシラン誘導体等のガス状のまたはガス化し得
るハロゲン化合物が好ましく挙げられる。また、さらに
はシリコン原子とハロゲン原子とを構成要素とするガス
状のまたはガス化し得る、ハロゲン原子を含む水素化珪
素化合物も有効なものとして挙げることができる。本発
明に於て好適に使用し得るハロゲン化合物としては、具
体的には弗素ガス(F2 )、BrF、ClF、ClF
3 、BrF3 、BrF5 、IF3 、IF7 等のハロゲン
間化合物を挙げることができる。ハロゲン原子を含む珪
素化合物、いわゆるハロゲン原子で置換されたシラン誘
導体としては、具体的には、たとえばSiF4 、Si2
F6 等の弗化珪素が好ましいものとして挙げることがで
きる。Further, as a raw material gas for supplying a halogen atom used in the present invention, a gaseous or gasifiable halogen compound such as a halogen gas, a halide, an interhalogen compound, a halogen-substituted silane derivative and the like is effective. Are preferred. Further, a gaseous or gasifiable silicon hydride compound containing a halogen atom, which contains silicon atoms and a halogen atom as constituent elements, can also be cited as an effective one. Specific examples of the halogen compound that can be preferably used in the present invention include fluorine gas (F 2 ), BrF, ClF and ClF.
Examples thereof include interhalogen compounds such as 3 , BrF 3 , BrF 5 , IF 3 and IF 7 . Specific examples of a silicon compound containing a halogen atom, a so-called silane derivative substituted with a halogen atom, include SiF 4 and Si 2
Silicon fluoride such as F 6 can be mentioned as a preferable example.
【0049】堆積膜中に含有される水素原子または/及
びハロゲン原子の量を制御するには、例えば支持体の温
度、水素原子または/及びハロゲン原子を含有させるた
めに使用される原料物質の反応容器内へ導入する量、放
電電力等を制御すればよい。The amount of hydrogen atoms and / or halogen atoms contained in the deposited film can be controlled by, for example, the temperature of the support, the reaction of the raw material used to contain the hydrogen atoms and / or halogen atoms. The amount introduced into the container, the discharge power, etc. may be controlled.
【0050】本発明は次のような条件のもとでも充分有
効に適用できる。即ち、本発明における堆積膜には必要
に応じてキヤリアの電気伝導性を制御する原子を含有さ
せることが好ましい。キヤリアの電気伝導性を制御する
原子は、堆積膜中に万偏なく均一に分布した状態で含有
されても良いし、あるいは層厚方向には不均一な分布状
態で含有している部分があってもよい。The present invention can be effectively applied even under the following conditions. That is, it is preferable that the deposited film in the present invention contains, if necessary, atoms that control the electrical conductivity of the carrier. Atoms that control the electric conductivity of the carrier may be contained in the deposited film in a uniformly distributed state, or may be contained in a non-uniformly distributed state in the layer thickness direction. May be.
【0051】前記伝導性を制御する原子としては、半導
体分野における、いわゆる不純物を挙げることができ、
p型伝導特性を与える周期律表第III b族に属する原子
(以後「第III b族原子」と略記する)またはn型伝導
特性を与える周期律表第Vb族に属する原子(以後「第
Vb族原子」と略記する)を用いることができる。Examples of the atoms for controlling the conductivity include so-called impurities in the field of semiconductors,
An atom belonging to Group IIIb of the periodic table giving the p-type conductivity (hereinafter abbreviated as “Group IIIb atom”) or an atom belonging to Group Vb of the periodic table giving the n-type conductivity (hereinafter “Vb”). (Abbreviated as "group atom") can be used.
【0052】第III b族原子としては、具体的には、硼
素(B)、アルミニウム(Al)、ガリウム(Ga)、
インジウム(In)、タリウム(Tl)等があり、特に
B、Al、Gaが好適である。第Vb族原子としては、
具体的には燐(P)、砒素(As)、アンチモン(S
b)、ビスマス(Bi)等があり、特にP、Asが好適
である。Specific examples of the Group IIIb atom include boron (B), aluminum (Al), gallium (Ga),
There are indium (In), thallium (Tl) and the like, and B, Al and Ga are particularly preferable. As the group Vb atom,
Specifically, phosphorus (P), arsenic (As), antimony (S)
b), bismuth (Bi), etc., and P and As are particularly preferable.
【0053】堆積膜に含有される伝導性を制御する原子
の含有量としては、好ましくは1×10-2〜1×104
原子ppm、より好ましくは5×10-2〜5×103 原
子ppm、最適には1×10-1〜1×103 原子ppm
とされるのが望ましい。The content of atoms controlling the conductivity contained in the deposited film is preferably 1 × 10 -2 to 1 × 10 4.
Atomic ppm, more preferably 5 × 10 -2 to 5 × 10 3 atomic ppm, optimally 1 × 10 -1 to 1 × 10 3 atomic ppm
Is desirable.
【0054】伝導性を制御する原子、たとえば、第III
b族原子あるいは第Vb族原子を構造の構成中に導入す
るには、層形成の際に、第III b族原子導入用の原料物
質あるいは第Vb族原子導入用の原料物質をガス状態で
反応容器中に、堆積膜を形成するための他のガスととも
に導入してやればよい。第III b族原子導入用の原料物
質あるいは第Vb族原子導入用の原料物質となり得るも
のとしては、常温常圧でガス状のまたは、少なくとも層
形成条件下で容易にガス化し得るものが採用されるのが
望ましい。Atoms that control conductivity, eg, III
To introduce a group b atom or a group Vb atom into the structure, a raw material for introducing a group IIIb atom or a raw material for introducing a group Vb atom is reacted in a gas state during layer formation. It may be introduced into the container together with another gas for forming a deposited film. As a raw material for introducing a Group IIIb atom or a raw material for introducing a Group Vb atom, a gaseous substance at room temperature and normal pressure, or at least a substance that can be easily gasified under the layer forming condition is adopted. Is desirable.
【0055】そのような第III b族原子導入用の原料物
質として具体的には、硼素原子導入用としては、B2 H
6 、B4 H10、B5 H9 、B5 H11、B6 H10、B6 H
12、B6 H14等の水素化硼素、BF3 、BCl3 、BB
r3 等のハロゲン化硼素等が挙げられる。この他、Al
Cl3 、GaCl3 、Ga(CH3 )3 、InCl3、
TlCl3 等も挙げることができる。As a raw material for introducing such a group IIIb atom, specifically, for introducing a boron atom, B 2 H
6, B 4 H 10, B 5 H 9, B 5 H 11, B 6 H 10, B 6 H
12 , borohydride such as B 6 H 14 , BF 3 , BCl 3 , BB
Examples thereof include boron halides such as r 3 . In addition to this, Al
Cl 3 , GaCl 3 , Ga (CH 3 ) 3 , InCl 3 ,
TlCl 3 and the like can also be mentioned.
【0056】第Vb族原子導入用の原料物質として有効
に使用されるのは、燐原子導入用としては、PH3 、P
2 H4 等の水素化燐、PH4 I、PF3 、PF5 、PC
l3、PCl5 、PBr3 、PBr5 、PI3 等のハロ
ゲン化燐が挙げられる。この他、AsH3 、AsF3 、
AsCl3 、AsBr3 、AsF5 、SbH3 、SbF
3 、SbF5 、SbCl3 、SbCl5 、BiH3 、B
iCl3 、BiBr3等も第Vb族原子導入用の出発物
質の有効なものとして挙げることができる。Effectively used as a raw material for introducing a group Vb atom is PH 3 , P for introducing a phosphorus atom.
2 H 4 etc. Phosphorus hydride, PH 4 I, PF 3 , PF 5 , PC
Examples thereof include phosphorus halides such as l 3 , PCl 5 , PBr 3 , PBr 5 , and PI 3 . In addition, AsH 3 , AsF 3 ,
AsCl 3 , AsBr 3 , AsF 5 , SbH 3 , SbF
3 , SbF 5 , SbCl 3 , SbCl 5 , BiH 3 , B
iCl 3 , BiBr 3 and the like can also be mentioned as effective starting materials for introducing a Group Vb atom.
【0057】また、これらの伝導性を制御する原子導入
用の原料物質は必要に応じてH2 および/またはHeに
より希釈して使用してもよい。Further, these raw material substances for introducing atoms for controlling the conductivity may be diluted with H 2 and / or He as necessary and used.
【0058】本発明の目的を達成し、所望の膜特性を有
する堆積膜を形成するには、Si供給用のガスと希釈ガ
スとの混合比、反応容器内のガス圧、放電電力ならびに
支持体温度を適宜設定するとよい。In order to achieve the object of the present invention and form a deposited film having desired film characteristics, the mixing ratio of the gas for supplying Si and the diluting gas, the gas pressure in the reaction vessel, the discharge power and the support The temperature may be set appropriately.
【0059】希釈ガスとして使用するH2 および/また
はHeの流量は、層設計にしたがって適宜最適範囲が選
択されるが、Si供給用ガスに対しH2 および/または
Heを、通常の場合3〜20倍、好ましくは4〜15
倍、最適には5〜10倍の範囲に制御することが望まし
い。The flow rate of H 2 and / or He used as the diluent gas is appropriately selected in accordance with the layer design, but H 2 and / or He is usually added to the Si supply gas in the range of 3 to 3. 20 times, preferably 4 to 15
It is desirable to control in the range of double, optimally 5 to 10 times.
【0060】反応容器内のガス圧も同様に層設計にした
がって適宜最適範囲が選択されるが、通常の場合1×1
0-4〜10Torr、好ましくは5×10-4〜5Tor
r、最適には1×10-3〜1Torrとするのが好まし
い。Similarly, the gas pressure in the reaction vessel is appropriately selected in the optimum range according to the layer design.
0 −4 to 10 Torr, preferably 5 × 10 −4 to 5 Torr
r, optimally 1 × 10 −3 to 1 Torr is preferable.
【0061】放電電力もまた同様に層設計にしたがって
適宜最適範囲が選択されるが、Si供給用のガスの流量
に対する放電電力を、通常の場合2〜7倍、好ましくは
2.5〜6倍、最適には3〜5倍の範囲に設定すること
が望ましい。Similarly, the discharge power is appropriately selected according to the layer design, but the discharge power with respect to the flow rate of the gas for supplying Si is usually 2 to 7 times, preferably 2.5 to 6 times. Optimally, it is desirable to set the range of 3 to 5 times.
【0062】さらに、支持体の温度は、層設計にしたが
って適宜最適範囲が選択されるが、通常の場合200〜
350℃とするのが望ましい。Further, the temperature of the support is appropriately selected in accordance with the layer design, and is usually 200 to
The temperature is preferably 350 ° C.
【0063】本発明においては、堆積膜を形成するため
の支持体温度、ガス圧の望ましい数値範囲として前記し
た範囲が挙げられるが、これらの条件は通常は独立的に
別々に決められるものではなく、所望の特性を有する電
子写真用感光体を形成すべく相互的且つ有機的関連性に
基づいて最適値を決めるのが望ましい。In the present invention, the above-mentioned ranges are mentioned as desirable numerical ranges of the temperature of the support and the gas pressure for forming the deposited film, but these conditions are not usually independently determined separately. It is desirable to determine the optimum value on the basis of mutual and organic relationships so as to form an electrophotographic photoreceptor having desired characteristics.
【0064】以下、本発明の装置について、実施例、比
較例により更に詳しく説明するが、本発明はこれらによ
り限定されるものではない。
[加熱実験例1]長さ358mm、外径φ108mmの
鏡面加工を施したAl製シリンダー(支持体)を載置し
たAl製ホルダー(長さ1000mm)を用い、図2に
示した支持体加熱容器にて、図4に示す支持体と同様の
長さをした複数の熱緩衝性補助部材を用い、表1に示す
条件にて、それぞれの長手方向及び、円周方向の温度分
布を測定した。その結果を表2に示す。尚加熱用のガス
としてはArを用いた。Hereinafter, the apparatus of the present invention will be described in more detail with reference to Examples and Comparative Examples, but the present invention is not limited thereto. [Heating Experimental Example 1] A support heating container shown in FIG. 2 using an Al holder (length 1000 mm) on which a mirror-finished Al cylinder (support) having a length of 358 mm and an outer diameter φ108 mm is mounted. Then, the temperature distributions in the longitudinal direction and the circumferential direction were measured under the conditions shown in Table 1 using a plurality of heat-buffering auxiliary members having the same length as the support shown in FIG. The results are shown in Table 2. Ar was used as the heating gas.
【0065】また温度分布の評価方法としては下記のよ
うな基準により評価を行なった。
(長手方向の温度分布の評価)
温度ムラが10℃以下であり特に優れている・・・・◎
温度ムラが10℃〜20℃であり良好である・・・・○
温度ムラが20℃以上であるが実用上問題ない・・・△
(周方向の温度分布の評価)
温度ムラが5℃以下であり特に優れている・・・・・◎
温度ムラが5℃〜10℃であり良好である・・・・・○
温度ムラが10℃以上あるが実用上問題ない・・・・△
以上それぞれ3段階の評価を行った。As a method of evaluating the temperature distribution, the evaluation was performed according to the following criteria. (Evaluation of Temperature Distribution in Longitudinal Direction) Temperature unevenness is 10 ° C. or less, which is particularly excellent ... ◎ Temperature unevenness is 10 ° C. to 20 ° C., which is excellent. However, there is no problem in practical use. △ (Evaluation of temperature distribution in the circumferential direction) Temperature unevenness is 5 ° C or less, which is particularly excellent ◎ ◎ Temperature unevenness is 5 ° C to 10 ° C, which is good. Yes ... Temperature unevenness is 10 ° C. or more, but there is no problem in practical use .... △ The above three-level evaluation was performed.
【0066】[0066]
【表1】
[加熱実験例2]熱緩衝性補助部材を用いなかった以外
は、加熱実験例1と同様の支持体加熱容器と加熱条件に
て加熱を行った。その後加熱実験例1と同様の方法にて
評価を行った。その結果は同様に表2に示す。同様に目
標温度に達するまでの昇温速度を加熱実験例1と比較し
た結果を図9に示す。同図で白丸は加熱実験例1の、黒
丸は加熱実験例2を示す。[Table 1] [Experimental Heating Example 2] Heating was performed under the same support heating container and heating conditions as in Experimental Heating Example 1 except that the thermal buffering auxiliary member was not used. After that, evaluation was performed in the same manner as in heating experiment example 1. The results are also shown in Table 2. Similarly, FIG. 9 shows the result of comparing the heating rate until reaching the target temperature with the heating experimental example 1. In the figure, white circles indicate heating experiment example 1, and black circles indicate heating experiment example 2.
【0067】[0067]
【表2】
表2、及び図9より明らかに円筒状の熱緩衝性補助部材
が一番長手方向にも周方向にも最良の結果となった。ま
た熱緩衝性補助部材がある事で昇温速度も早くなった。
[加熱実験例3]実験例1と同様の支持体加熱容器を用
い、熱緩衝性補助部材としては図4に示すType1の
熱緩衝性補助部材を使用した。そのとき表3に示す条件
にてArの流量と内圧を変化させて長手方向と周方向の
温度分布の測定を行った。その結果を表4に示す。[Table 2] It is apparent from Table 2 and FIG. 9 that the cylindrical heat buffering auxiliary member has the best results both in the longitudinal direction and in the circumferential direction. In addition, the rate of temperature rise was also increased due to the presence of the heat buffering auxiliary member. [Experimental Heating Example 3] The same support heating container as in Experimental Example 1 was used, and the type 1 thermal buffering auxiliary member shown in FIG. 4 was used as the thermal buffering auxiliary member. At that time, the flow rate of Ar and the internal pressure were changed under the conditions shown in Table 3 to measure the temperature distribution in the longitudinal direction and the circumferential direction. The results are shown in Table 4.
【0068】[0068]
【表3】 [Table 3]
【0069】[0069]
【表4】
表4より明らかにArが1000sccm〜2000s
ccmの範囲で内圧が0.50torrの時において良
好な結果を示した。
[加熱実験例4]加熱実験例1と同様の支持体加熱容器
にてType1の熱緩衝性補助部材を用いて熱緩衝性補
助部材の長手方向の長さを変化させた時、長手方向の温
度分布を測定した。その結果を表6に示す。尚この時は
表5に示す条件にて加熱を行った。[Table 4] From Table 4, it is clear that Ar is 1000 sccm to 2000 s
Good results were shown when the internal pressure was 0.50 torr in the range of ccm. [Experimental heating example 4] When the length in the longitudinal direction of the thermal buffering auxiliary member was changed using the thermal buffering auxiliary member of Type 1 in the same support heating container as in heating experimental example 1, the temperature in the longitudinal direction was changed. The distribution was measured. The results are shown in Table 6. At this time, heating was performed under the conditions shown in Table 5.
【0070】[0070]
【表5】 [Table 5]
【0071】[0071]
【表6】
表6より明らかに716〜1000の範囲において良好
な結果が得られた。
[加熱実験例5]加熱実験例3と同様の支持体と装置と
熱緩衝性補助部材を用いて表5に示す条件にて加熱を行
った。このとき熱緩衝性補助部材に異なる材質を用いた
時の長手方向と、周方向の温度分布を測定した。その結
果を表7に示す。[Table 6] From Table 6, it is clear that good results were obtained in the range of 716 to 1000. [Experimental heating example 5] Heating was performed under the conditions shown in Table 5 using the same support, apparatus and heat buffering auxiliary member as in experimental heating example 3. At this time, the temperature distributions in the longitudinal direction and the circumferential direction when different materials were used for the heat buffering auxiliary member were measured. The results are shown in Table 7.
【0072】[0072]
【表7】
表7から明らかなようにどの材質を用いても良好な温度
分布の結果が得られた。
[実施例1]長さ358mm、外径φ108mmの鏡面
加工を施したAl製シリンダー(支持体)を載置したA
l製ホルダー(長さ1000mm)を用い、図2に示し
た装置に支持体と熱緩衝性補助部材の間隔を変化させた
時に支持体の昇温速度を測定した。その結果を図10に
示す。(間隔は支持体の外径=S、熱緩衝性補助部材の
外径=Wとした時W/Sで表し、図の符号に付した数字
がこの比である)
図10より明らかに1.2≦W/S≦2.5の範囲にお
いて良好な結果を示している。
[実施例2]実施例1と同様の支持体を用い支持体加熱
容器を具備した図1に示す連続生産装置にて、支持体加
熱容器に熱緩衝性補助部材を用いて加熱を行い、その後
反応容器に搬送し表8に示す条件にて10本連続成膜を
行った。但し熱緩衝性補助部材はステンレス製でW/S
=1.5として加熱容器内にセットした。[Table 7] As is clear from Table 7, good temperature distribution results were obtained regardless of the material used. [Example 1] A on which a cylinder (support) made of Al having a length of 358 mm and an outer diameter of 108 mm and having a mirror-finished surface was placed
Using a holder made of 1 (length 1000 mm), the temperature rising rate of the support was measured when the distance between the support and the thermal buffering auxiliary member was changed in the apparatus shown in FIG. The result is shown in FIG. (The interval is represented by W / S when the outer diameter of the support = S and the outer diameter of the heat buffering auxiliary member = W, and the numbers attached to the symbols in the figure are the ratios). Good results are shown in the range of 2 ≦ W / S ≦ 2.5. [Example 2] In the continuous production apparatus shown in Fig. 1 using the same support as in Example 1 and equipped with a support heating container, heating was performed using a heat buffering auxiliary member in the support heating container, and thereafter. The film was transported to a reaction container and 10 continuous films were formed under the conditions shown in Table 8. However, the heat buffering auxiliary member is made of stainless steel and has W / S
= 1.5 and set in the heating container.
【0073】この様にして作製された電子写真感光体を
電子写真的特性の評価を以下のようにして行った。The electrophotographic photosensitive member thus produced was evaluated for electrophotographic characteristics as follows.
【0074】作成した電子写真感光体を実験用に予めプ
ロセススピードを200〜800mm/secの範囲で
任意に変更できるように改造を行ったキヤノン社製複写
機NP6060にいれ、帯電器に5〜8kVの電圧を印
加してコロナ帯電を行い、通常の複写プロセスにより転
写紙上に画像を作製し、下の手順により画像性の評価を
行った。このようにして同一作製条件で製造した電子写
真感光体の評価を行い、評価結果を表9に示した。The electrophotographic photosensitive member thus prepared was put in a copying machine NP6060 manufactured by Canon Inc., which had been modified so that the process speed could be arbitrarily changed in the range of 200 to 800 mm / sec for an experiment, and the charging device was set to 5 to 8 kV. The voltage was applied to perform corona charging, an image was formed on a transfer paper by a normal copying process, and the image quality was evaluated by the following procedure. The electrophotographic photosensitive member manufactured under the same manufacturing conditions as described above was evaluated, and the evaluation results are shown in Table 9.
【0075】画像欠陥の評価
プロセススピードを変え全面ハーフトーン原稿及び文字
原稿を原稿台に置いてコピーした時に得られた画像サン
プル中で一番画像欠陥の多く現われる画像サンプルを選
び評価を行った。評価の方法としては画像サンプル上を
拡大鏡で観察し同一面積内にある白点の状態により評価
を行った。
◎ … 良好。
○ … 一部微少な白点有り。
△ … 全面に微少な白点があるが文字の認識には支障
無し。
× … 白点が多い為一部文字が読みにくい部分が有
る。Evaluation of Image Defect The image sample showing the largest number of image defects was selected and evaluated among the image samples obtained when a full-face halftone original and a character original were copied on the original table while changing the process speed. As an evaluation method, the image sample was observed with a magnifying glass and evaluated by the state of white spots within the same area. ◎… Good. ○: There are some white spots. △… There are slight white dots on the entire surface, but there is no problem in recognizing the characters. ×: Some characters are difficult to read because there are many white dots.
【0076】電子写真特性の評価(帯電能)
通常のプロセススピードで同一の帯電電圧を与えたとき
に現像位置で得られる感光体の表面電位を帯電能として
相対値により評価する。但し、比較例1で得られた電子
写真感光体の帯電能を100%としている。Evaluation of Electrophotographic Characteristics (Charging Ability) The surface potential of the photoconductor obtained at the developing position when the same charging voltage is applied at a normal process speed is evaluated by a relative value as the charging ability. However, the charging ability of the electrophotographic photosensitive member obtained in Comparative Example 1 is 100%.
【0077】電子写真特性(母線方向電位ムラ)
電子写真感光体の母線方向の5箇所の帯電電位を測定し
ムラを測定した。
ムラが5V未満非常に良好である ・・・○
ムラが5V以上、30V未満であり良好である・・・△
ムラが30V以上である ・・・×
電子写真特性(周方向電位ムラ)
電子写真感光体の周方向について一定の電流値を印加し
た時ある一点において周方向に電位を測定しそれを周方
向電位ムラとし、それを母線方向5点について測定しそ
のうちの最大値をその周方向電位ムラとして評価した。
ムラが5V未満非常に良好である ・・・○
ムラが5V以上、30V未満であり良好である・・・△
ムラが30V以上である ・・・×
(比較例1)支持体加熱容器内に熱緩衝性補助部材を用
いなかった以外は、実施例2と同様の支持体と装置にて
同様の条件で作製された電子写真感光体の電子写真特性
を比較例1として同様に表9に示す。Electrophotographic characteristics (potential unevenness in the busbar direction) The unevenness was measured by measuring the charging potential at five points in the busbar direction of the electrophotographic photosensitive member. The unevenness is less than 5 V, which is very good .... ○ The unevenness is 5 V or more and less than 30 V, which is good. Δ The unevenness is 30 V or more ... × Electrophotographic characteristics (circumferential potential unevenness) Electrophotography When a constant current value is applied in the circumferential direction of the photoconductor, the potential is measured in the circumferential direction at a certain point, and it is defined as the circumferential potential unevenness, and it is measured at five points in the busbar direction, and the maximum value is the circumferential potential. It was evaluated as unevenness. Mura is less than 5 V Very good ... O Mura is 5 V or more and less than 30 V, good ... Δ Mura is 30 V or more ... × (Comparative Example 1) In a support heating container The electrophotographic characteristics of the electrophotographic photosensitive member produced under the same conditions and conditions as in Example 2 except that the auxiliary member for heat buffering property was not used are also shown in Table 9 as Comparative Example 1. .
【0078】[0078]
【表8】 [Table 8]
【0079】[0079]
【表9】
表9から明らかなように、熱緩衝性補助部材を用いて作
製された電子写真感光体において安定した良好な結果が
得られた。また予期せぬ効果として帯電能の向上が見ら
れた。
[実施例3]成膜装置として図5、図6に示すμwPC
VD装置の加熱容器及び反応容器を用いた以外は、実施
例1と同様の支持体と、W/S=1.5に設定した熱緩
衝性補助部材を用い表10に示す条件にて加熱しその後
表11に示す条件にて、電荷注入阻止層、電荷輸送層、
電荷発生層、表面層からなる電子写真感光体を作製し、
実施例2と同様の評価を行ったところ、同様に良好な結
果が得られた。[Table 9] As is clear from Table 9, stable and good results were obtained in the electrophotographic photosensitive member produced using the heat buffering auxiliary member. Also, an unexpected effect was an improvement in charging ability. [Example 3] μwPC shown in FIGS. 5 and 6 as a film forming apparatus
Heating was performed under the conditions shown in Table 10 using the same support as in Example 1 and the thermal buffering auxiliary member set to W / S = 1.5, except that the heating container and reaction container of the VD apparatus were used. Then, under the conditions shown in Table 11, the charge injection blocking layer, the charge transport layer,
An electrophotographic photosensitive member comprising a charge generation layer and a surface layer is prepared,
When the same evaluation as in Example 2 was performed, similarly good results were obtained.
【0080】[0080]
【表10】 [Table 10]
【0081】[0081]
【表11】
[実施例4]成膜装置として図7、図8に示すVHFP
CVD装置の加熱容器及び反応容器を用いた以外は、実
施例1と同様の支持体と、W/S=1.5に設定した熱
緩衝性補助部材を用い表12に示す条件にて加熱し、そ
の後表13に示す条件にて、電子写真感光体を作製し、
実施例2と同様の評価を行ったところ、同様に良好な結
果が得られた。[Table 11] Example 4 VHFP shown in FIGS. 7 and 8 as a film forming apparatus
Heating was performed under the conditions shown in Table 12 using the same support as in Example 1 except that the heating vessel and reaction vessel of the CVD apparatus were used and the thermal buffering auxiliary member set to W / S = 1.5. After that, under the conditions shown in Table 13, an electrophotographic photosensitive member was prepared,
When the same evaluation as in Example 2 was performed, similarly good results were obtained.
【0082】[0082]
【表12】 [Table 12]
【0083】[0083]
【表13】 [Table 13]
【0084】[0084]
【発明の効果】本発明によれば、熱緩衝性補助部材を用
いる事により支持体の温度分布を均一化させ、支持体の
昇温時間を短縮出来ることで、生産タクトの向上と省エ
ネ化が出来ると同時に連続生産における膜厚の経時変化
を抑え、歩留を飛躍的に向上することができる。According to the present invention, the temperature distribution of the support can be made uniform by using the heat buffering auxiliary member, and the time required for raising the temperature of the support can be shortened, thereby improving the production tact and saving energy. At the same time, it is possible to suppress the change in film thickness over time in continuous production, and to dramatically improve the yield.
【図1】支持体投入容器、支持体加熱容器、反応容器、
支持体冷却及び排出容器と、これらの容器間で移動可能
な搬送専用の真空容器を有する連続生産装置の模式的説
明図である。FIG. 1 is a support charging container, a support heating container, a reaction container,
It is a schematic explanatory view of a continuous production apparatus having a support cooling and discharge container and a vacuum container dedicated to transportation that is movable between these containers.
【図2】本発明のプラズマCVD法による堆積膜形成装
置における、電極を兼ねる円筒状加熱容器、支持体を含
む対向電極、ガス導入分岐管等を示す模式的説明図であ
る。FIG. 2 is a schematic explanatory view showing a cylindrical heating container that also serves as an electrode, a counter electrode including a support, a gas introduction branch pipe, and the like in the deposited film forming apparatus by the plasma CVD method of the present invention.
【図3】本発明の熱緩衝性補助部材を具備した支持体加
熱容器を模式的に示す断面図である。FIG. 3 is a cross-sectional view schematically showing a support heating container provided with the heat buffering auxiliary member of the present invention.
【図4】加熱実験例1における異なる形状の熱緩衝性補
助部材を示す図。FIG. 4 is a view showing heat cushioning auxiliary members having different shapes in heating experiment example 1.
【図5】実施例3における加熱容器を示す図。FIG. 5 is a diagram showing a heating container according to a third embodiment.
【図6】実施例3における反応容器を示す図。FIG. 6 is a diagram showing a reaction container in Example 3.
【図7】実施例4における加熱容器を示す図。FIG. 7 is a diagram showing a heating container according to a fourth embodiment.
【図8】実施例4における反応容器を示す図。FIG. 8 is a diagram showing a reaction container in Example 4.
【図9】加熱実験例1及び2における温度上昇の比較を
示す図。FIG. 9 is a diagram showing a comparison of temperature rises in heating experiment examples 1 and 2.
【図10】実施例1における温度上昇を示す図。FIG. 10 is a diagram showing a temperature rise in Example 1.
1100/1101 支持体投入装置/支持体投入容器 1200/1201 支持体加熱装置/支持体加熱容器 1300/1301a〜c 反応装置/反応容器 1400/1401 冷却及び排出装置/冷却及び排出容器 1501〜1507 排気手段(真空ポンプ) 1601〜1608 排気バルブ 1701、1705、1706 リークバルブ 1702 加熱用ガス補助バルブ 1703a〜c、1704 ガス流出バルブ 1801〜1807 開閉ゲート 1900/1901 搬送装置/搬送専用真空容器 1951 搬送用チャッキング 1952 搬送移動用レール 2100 堆積装置2111 反応容器 3111 加熱容器 2112、3112 支持体 2113、3113 加熱用ヒーター 2114、3114 原料ガス導入管 2115 マッチングボックス 2116、3116 原料ガス配管 2117、3117 反応容器リークバルブ 2118、3118 メイン排気バルブ 2119、3119 真空計 2200 原料ガス供給装置 2211〜2216 マスフローコントローラー 2221〜2226 原料ガスボンベ 2231〜2236 原料ガスボンベバルブ 2241〜2246 ガス流入バルブ 2251〜2256 ガス流出バルブ 2261〜2266 圧力調整器 3115 熱緩衝性補助部材 3120 ゲートバルブ 3121 ベース台 3122 絶縁リング 3124 排気配管 501-1/501-2、611-1/611-2 加熱容器/反応容器 502-2 μW導入窓 503-2 μW導入管 504-1、504-2、612-1、612-2 排気口 505-1、505-2、617-1、617-2 支持体 506-2 放電空間 507-1、507-2 加熱用ヒーター 508-1、508-2 回転軸 509-1、509-2 回転用モーター 510-2 DC電源 512-1、512-2 原料ガス導入パイプ 613-1、613-2 加熱用ヒーター 614-1、614-2 原料ガス導入パイプ 615-2 VHF導入棒 616-2 マッチングBOX1100/1101 Support feeding device / Support feeding container 1200/1201 Support heating device / Support heating container 1300 / 1301a to c Reactor / Reaction container 1400/1401 Cooling and discharging device / Cooling and discharging container 1501 to 1507 Exhaust Means (vacuum pump) 1601 to 1608 Exhaust valve 1701, 1705, 1706 Leak valve 1702 Heating gas auxiliary valve 1703a to c, 1704 Gas outflow valve 1801 to 1807 Open / close gate 1900/1901 Transport device / Vehicle dedicated to transport 1951 Transport chat King 1952 Transfer rail 2100 Deposition device 2111 Reaction vessel 3111 Heating vessels 2112, 3112 Supports 2113, 3113 Heating heaters 2114, 3114 Raw gas introduction pipe 2115 Matching boxes 2116, 3116 Raw gas pipes 2117, 3117 Reaction vessel leak valve 2118 , 3118 Main exhaust valve 2119, 3119 Vacuum gauge 2200 Source gas supply device 2211 to 2216 Mass flow controller 2221 to 2226 Source gas cylinder 2231 to 2236 Source gas cylinder valve 2241 2246 gas inlet valve 2251 to 2256 gas outflow valves 2261 to 2266 pressure regulators 3115 thermal buffer auxiliary member 3120 gate valve 3121 baseplate 3122 insulation ring 3124 exhaust pipe 501-1 / 501-2,611-1 / 611-2 heating Vessel / reaction vessel 502-2 μW introduction window 503-2 μW introduction pipe 504-1, 504-2, 612-1, 612-2 Exhaust port 505-1, 505-2, 617-1, 617-2 Support 506-2 Discharge space 507-1, 507-2 Heating heater 508-1, 508-2 Rotating shaft 509-1, 509-2 Rotating motor 510-2 DC power supply 512-1, 512-2 Raw material gas introduction pipe 613-1, 613-2 Heating heaters 614-1, 614-2 Raw material gas introduction pipe 615-2 VHF introduction rod 616-2 Matching box
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭64−56874(JP,A) 特開 平6−324505(JP,A) 特開 平8−27578(JP,A) 特開 平4−212167(JP,A) 特開 昭64−8275(JP,A) 特開 昭60−11850(JP,A) (58)調査した分野(Int.Cl.7,DB名) G03G 5/08 ─────────────────────────────────────────────────── ─── Continuation of the front page (56) Reference JP-A 64-56874 (JP, A) JP-A 6-324505 (JP, A) JP-A 8-27578 (JP, A) JP-A 4- 212167 (JP, A) JP 64-8275 (JP, A) JP 60-11850 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) G03G 5/08
Claims (4)
成するための反応容器及びこれらの容器間で移動可能な
搬送専用の真空容器とからなり、各容器は接続可能な開
閉ゲートを設け、前記支持体加熱容器及び反応容器と前
記搬送専用の真空容器との間で支持体の出し入れ移動可
能とした連続生産装置を用い、前記支持体加熱容器内に
支持体に対向する長手方向に開口部のない熱緩衝性補助
部材を設けて支持体の温度を高めた後、前記支持体を前
記反応容器内に搬送し、プラズマCVD法により堆積膜
を作ることを特徴とする光受容部材の製造方法。1. Forming at least a support heating vessel and a deposited film
And a support- use vacuum container for transporting the containers, each container being provided with an opening / closing gate which can be connected to the support heating container and the reaction container. using a continuous production apparatus which enables out movement of the support with the vacuum chamber of the transport dedicated to the support heating vessel
After increasing the temperature of the opposite longitudinally provided thermal buffer auxiliary member without opening the support to the support, before the support
A method of manufacturing a light-receiving member, which comprises transporting the material into a reaction container and forming a deposited film by a plasma CVD method.
断面形状とし支持体に対して間隔を設けて配置して行な
う事を特徴とする請求項1に記載の方法。2. A method according to claim 1, wherein the performing by arranged with a distance from the support of the heat shock auxiliary member and the support member and the similar cross-sectional shape.
し、前記支持体の外径をSとする時、下記式を満足する
事を特徴とする請求項1又は2のいずれかに記載の方
法。 1.1≦W/S≦3.0Wherein said heat shock auxiliary member with its outer diameter is W, the outer diameter of the support when the S, to claim 1 or 2, characterized in that it satisfies the following expression The method described. 1.1 ≦ W / S ≦ 3.0
し、前記支持体の外径をSとする時、下記式を満足する
事を特徴とする請求項3に記載の方法。 1.2≦W/S≦2.54. The method according to claim 3 , wherein when the outer diameter of the heat-absorbing auxiliary member is W and the outer diameter of the support is S, the following equation is satisfied. 1.2 ≦ W / S ≦ 2.5
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP04152796A JP3441876B2 (en) | 1996-02-28 | 1996-02-28 | Method for manufacturing light receiving member |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP04152796A JP3441876B2 (en) | 1996-02-28 | 1996-02-28 | Method for manufacturing light receiving member |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH09236936A JPH09236936A (en) | 1997-09-09 |
| JP3441876B2 true JP3441876B2 (en) | 2003-09-02 |
Family
ID=12610882
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP04152796A Expired - Fee Related JP3441876B2 (en) | 1996-02-28 | 1996-02-28 | Method for manufacturing light receiving member |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3441876B2 (en) |
-
1996
- 1996-02-28 JP JP04152796A patent/JP3441876B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH09236936A (en) | 1997-09-09 |
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