JPH04255332A - Manufacture of resistance control endless belt material - Google Patents

Manufacture of resistance control endless belt material

Info

Publication number
JPH04255332A
JPH04255332A JP2414872A JP41487290A JPH04255332A JP H04255332 A JPH04255332 A JP H04255332A JP 2414872 A JP2414872 A JP 2414872A JP 41487290 A JP41487290 A JP 41487290A JP H04255332 A JPH04255332 A JP H04255332A
Authority
JP
Japan
Prior art keywords
tube
mandrel
controlled
endless belt
gas
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.)
Granted
Application number
JP2414872A
Other languages
Japanese (ja)
Other versions
JP2886350B2 (en
Inventor
Katsumi Okuyama
奥山 克己
Makoto Morikoshi
誠 森越
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Petrochemical Co Ltd
Original Assignee
Mitsubishi Petrochemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Petrochemical Co Ltd filed Critical Mitsubishi Petrochemical Co Ltd
Priority to JP2414872A priority Critical patent/JP2886350B2/en
Publication of JPH04255332A publication Critical patent/JPH04255332A/en
Application granted granted Critical
Publication of JP2886350B2 publication Critical patent/JP2886350B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To prepare a resistance control endless belt with a uniform diameter and thickness and a uniform surface resistance level. CONSTITUTION:A thermoplastic resin compsn. compounded with an electrically conductive filler is melted and is extruded downward into a tube-like shape from a ring die 3 mounted on an extruder 2. A temp.-controlled gas is blown on the outer peripheral face of this tube and a gas both feeding pressure and flow quantity of which are controlled is continuously fed and discharged inside of the tube. Then, the tube is brought into contact with a temp.-controlled mandrel 5 and temp.-controlled gas is blown again to the outer peripheral face of the tube at a point being adjoining to the position of contact. Then, while the tube-like shape is kept, the tube is continuously taken up by means of nip rolls and it is cut into round slices to obtain a resistance control endless belt material.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は、電子写真式複写機、レ
ーザープリンタ等の感光体装置、中間転写装置、転写分
離装置、帯電装置等において使用するエンドレスベルト
の素材となる抵抗制御エンドレスベルト材の製造方法に
関するものである。
[Industrial Application Field] The present invention is a resistance-controlled endless belt material used in electrophotographic copying machines, photoreceptor devices such as laser printers, intermediate transfer devices, transfer separation devices, charging devices, etc. The present invention relates to a manufacturing method.

【0002】0002

【従来の技術】従来、電子写真式複写機、レーザープリ
ンタ等の感光体装置、中間転写装置、転写分離装置、帯
電装置等においては、継ぎ目部を有するエンドレスベル
トが多用されている。
2. Description of the Related Art Conventionally, endless belts having seams have been frequently used in electrophotographic copying machines, photoreceptor devices such as laser printers, intermediate transfer devices, transfer separation devices, charging devices, and the like.

【0003】このような継ぎ目部を有するエンドレスベ
ルトを駆動する場合には、継ぎ目部で微小振動が発生し
、高速化できないという問題点を有している。又、感光
体装置、中間転写装置等の抵抗制御エンドレスベルトと
して使用する場合には、継ぎ目部における感光性能、転
写性能が他の部分と著しく異なり、機能上使用できない
という問題点を有している。
When driving an endless belt having such a seam, there is a problem in that minute vibrations occur at the seam, making it impossible to increase the speed. Furthermore, when used as a resistance-controlled endless belt in a photoreceptor device, intermediate transfer device, etc., the photosensitive performance and transfer performance at the seam are significantly different from other parts, and there is a problem that the belt cannot be used functionally. .

【0004】そこで、継ぎ目部を有さないエンドレスベ
ルトを得る種々の製造方法が提案されているが、未だ満
足すべき製造方法は得られていないというのが現状であ
る。
[0004] Various manufacturing methods for obtaining endless belts without seams have been proposed, but the current situation is that a satisfactory manufacturing method has not yet been obtained.

【0005】このようなエンドレスベルトの製造方法と
して、本発明者等は、特開平1−228823号公報に
おいてポリカーボネート製のエンドレスベルト材の製造
方法を提案した。
As a method for manufacturing such an endless belt, the present inventors proposed a method for manufacturing an endless belt material made of polycarbonate in Japanese Unexamined Patent Publication No. 1-228823.

【0006】[0006]

【発明が解決しようとする課題】特開平1−22882
3号公報において提案したような環状ダイ近傍の温調リ
ングから気体を吹き付けた後、内部からマンドレルのみ
で冷やす方法では、得られたエンドレスベルトの表面抵
抗は±2〜3オーダー以上バラツクことが判明した。こ
の程度の抵抗制御レベルのエンドレスベルトを電子写真
式複写機等に使用すると、画像ムラが発生して鮮明な画
像が得られないという問題点を有していた。
[Problem to be solved by the invention] JP-A-1-22882
In the method proposed in Publication No. 3, in which gas is blown from a temperature control ring near the annular die and then cooled from inside using only a mandrel, it has been found that the surface resistance of the obtained endless belt varies by more than ±2 to 3 orders of magnitude. did. When an endless belt with such a resistance control level is used in an electrophotographic copying machine or the like, there is a problem in that image unevenness occurs and clear images cannot be obtained.

【0007】本発明は、かかる問題点に鑑みてなされた
ものであり、その目的とするところは、真円かつ肉厚が
均一であって、表面抵抗レベルも均一なエンドレスベル
ト材を得る製造方法を提供するものである。
The present invention has been made in view of these problems, and its purpose is to provide a manufacturing method for obtaining an endless belt material that is perfectly circular, has a uniform wall thickness, and has a uniform surface resistance level. It provides:

【0008】[0008]

【課題を解決するための手段】本発明者等は上記問題点
を解決すべく鋭意検討を行った結果、エンドレスベルト
表面の抵抗レベルが不均一となるのは、環状ダイから押
し出された溶融状態のチュ−ブがマンドレルを通過する
間に不均一に冷却されるためであることを見出した。そ
して、チューブが最も大きく変形するマンドレル上端近
傍においてチューブの外周面から再度気体を吹き付けて
その外周面温度をマンドレル温度に近づけることにより
、エンドレスベルトの表面抵抗レベルを±1オーダー以
内に制御可能なことを見出したのである。
[Means for Solving the Problems] As a result of intensive studies to solve the above problems, the inventors of the present invention found that the reason why the resistance level of the endless belt surface is uneven is due to the molten state extruded from the annular die. It has been found that this is because the tube is cooled unevenly while passing through the mandrel. Furthermore, the surface resistance level of the endless belt can be controlled within ±1 order by blowing gas again from the outer peripheral surface of the tube near the upper end of the mandrel where the tube deforms the most to bring the temperature of the outer peripheral surface closer to the mandrel temperature. They discovered this.

【0009】すなわち、本発明のエンドレスベルト材の
製造方法は、導電性フィラ−を配合した熱可塑性樹脂組
成物を溶融し、押出機に装着した環状ダイより下方にチ
ュ−ブ状に押し出し、このチューブの外周面に温調した
気体を吹き付けるとともに、チューブの内側に供給圧力
と供給流量を制御した気体を連続的に供給・排除させ、
次いで、温調されたマンドレルに接触させるとともに、
マンドレルに接触を開始する近傍のチューブの外周面に
再度温調した気体を吹き付け、しかる後、チューブ状を
維持したままで連続して引き取って輪切り状に切断する
ことにようにしたことを特徴とする抵抗制御エンドレス
ベルト材の製造方法である。
That is, the method for manufacturing an endless belt material of the present invention involves melting a thermoplastic resin composition containing a conductive filler and extruding it into a tube shape downward through an annular die attached to an extruder. At the same time as blowing temperature-controlled gas onto the outer circumferential surface of the tube, gas with controlled supply pressure and flow rate is continuously supplied and removed from the inside of the tube.
Next, while bringing it into contact with a temperature-controlled mandrel,
The temperature-controlled gas is again blown onto the outer peripheral surface of the tube near where it starts contacting the mandrel, and then the tube is continuously pulled out and cut into slices while maintaining its tube shape. This is a method for manufacturing a resistance-controlled endless belt material.

【0010】0010

【実施例】本発明において適用される樹脂組成物は、基
本的に熱可塑性樹脂に導電性フィラーを配合したもので
ある。
[Example] The resin composition applied in the present invention is basically a thermoplastic resin mixed with a conductive filler.

【0011】熱可塑性樹脂としては、ポリカーボネート
、ポリエチレンテレフタレート、ポリエーテルエーテル
ケトン、ポリフッカビニリデン、ポリアミド、アクリル
、ポリオレフィン、ポリスルホン、ポリエーテルスルホ
ン、エチレンテトラフロロエチレン共重合体、アクリル
共重合体、ポリエステルエステル共重合体、ポリエ−テ
ルエステル共重合体、ポリエーテルアミド共重合体、オ
レフィン共重合体、ポリウレタン共重合体から選ばれる
少なくとも1種またはこれら数種の混合物からなるもの
が好ましい。
Examples of thermoplastic resins include polycarbonate, polyethylene terephthalate, polyether ether ketone, polyfukkavinylidene, polyamide, acrylic, polyolefin, polysulfone, polyether sulfone, ethylenetetrafluoroethylene copolymer, acrylic copolymer, and polyester. It is preferable to use at least one selected from copolymers, polyetherester copolymers, polyetheramide copolymers, olefin copolymers, and polyurethane copolymers, or a mixture of several of these.

【0012】導電性フィラーとしては、カーボンブラッ
ク、グラファイト、カーボン繊維、金属粉、導電性金属
酸化物、有機金属化合物、有機金属塩、導電性高分子等
から選ばれる少なくとも1種またはこれら数種の混合物
からなるものが好ましい。その中でも特に、カーボンブ
ラックが好ましい。カ−ボンブラックとしては、アセチ
レンブラック、ファーネスブラック、チャンネルブラッ
ク等のカーボンブラックがある。比表面積の大きいS.
C.F.(Super Conductive Fur
nace) 、E.C.F.(Electric Co
nductive Furnace)、ケッチェンブラ
ックEC(AKZO社製商品名)を用いると少量の配合
割合で目的の導電性が得られる点で有利である。
The conductive filler is at least one selected from carbon black, graphite, carbon fiber, metal powder, conductive metal oxide, organometallic compound, organometallic salt, conductive polymer, etc., or several of these. Those consisting of a mixture are preferred. Among them, carbon black is particularly preferred. Carbon blacks include carbon blacks such as acetylene black, furnace black, and channel black. S. with a large specific surface area.
C. F. (Super Conductive Fur
nace), E. C. F. (Electric Co.
It is advantageous to use Ketjen Black EC (trade name, manufactured by AKZO), as it is possible to obtain the desired conductivity with a small amount of blending ratio.

【0013】カ−ボンブラックの配合量は、熱可塑性樹
脂100重量部に対して3〜25重量部である。カーボ
ンブラックが上記範囲未満では導電性に乏しく、上記範
囲以上では製品の外観が悪くなり、また、材料強度が低
下して好ましくない。
The amount of carbon black blended is 3 to 25 parts by weight per 100 parts by weight of the thermoplastic resin. If the carbon black is less than the above range, the conductivity will be poor, and if it is more than the above range, the appearance of the product will be poor and the material strength will be reduced, which is not preferable.

【0014】樹脂組成物には、本発明の目的を阻害しな
い限りにおいて、通常の樹脂組成物に配合される各種の
付加的成分を含むことができる。このような成分として
は、酸化防止剤、滑剤、離型剤などがある。
[0014] The resin composition may contain various additional components that are commonly incorporated into resin compositions, as long as they do not impede the object of the present invention. Such components include antioxidants, lubricants, mold release agents, and the like.

【0015】エンドレスベルト材の製造装置1は、図1
、図2および図3に示すように、押出機2に装着した環
状ダイ3に支持管棒4の上部を同軸状に固定し、この支
持管棒4の下部にマンドレル5を同軸状に固定したもの
である。
The endless belt material manufacturing apparatus 1 is shown in FIG.
As shown in FIGS. 2 and 3, the upper part of the support tube rod 4 was fixed coaxially to the annular die 3 attached to the extruder 2, and the mandrel 5 was coaxially fixed to the lower part of the support tube rod 4. It is something.

【0016】環状ダイ3とマンドレル5との間に支持管
棒4と同軸状に温調リング6,6′,6″を配設し、マ
ンドレルの下方には複数組のニップロ−ル9を配設して
ある。ニップロ−ル9はマンドレル5の下方の支持管棒
4の外周に配設した複数の内側ロール7,7と、これら
内側ロール7,7に対応して配設した外側ロール8,8
とからなる。
Temperature control rings 6, 6', 6'' are arranged coaxially with the support tube rod 4 between the annular die 3 and the mandrel 5, and a plurality of sets of nip rolls 9 are arranged below the mandrel. The nip roll 9 includes a plurality of inner rolls 7, 7 disposed on the outer periphery of the support pipe rod 4 below the mandrel 5, and an outer roll 8 disposed corresponding to these inner rolls 7, 7. ,8
It consists of.

【0017】前記支持管棒4には供給圧力・供給流量制
御気体連続供給機構10およびマンドレル内熱媒供給機
構11を付設してある。
The support tube rod 4 is provided with a gas continuous supply mechanism 10 for controlling supply pressure and supply flow rate and a mandrel heating medium supply mechanism 11.

【0018】前記供給圧力・供給流量制御気体連続供給
機構10は、前記支持管棒4内を通り吹出口12に開口
する供給管13と、前記支持管棒4内を通り吹込口14
に開口する排出管15とよりなる。
The supply pressure/supply flow rate control gas continuous supply mechanism 10 includes a supply pipe 13 that passes through the support tube rod 4 and opens to the blowout port 12, and a supply tube 13 that passes through the support tube rod 4 and opens to the blowout port 14.
It consists of a discharge pipe 15 that opens to.

【0019】前記マンドレル内熱媒供給機構11は、前
記支持管棒4内を通りマンドレル5内の流入口16に開
口してある供給管17と、前記支持管棒4内を通りマン
ドレル5内の流出口18に開口する排出管19とよりな
る。
The in-mandrel heating medium supply mechanism 11 includes a supply pipe 17 passing through the support tube rod 4 and opening to an inlet 16 in the mandrel 5, and a supply tube 17 passing through the support tube rod 4 and opening into the inlet 16 in the mandrel 5. It consists of a discharge pipe 19 that opens to the outlet 18.

【0020】環状ダイ3の向きは、押出機2に対して上
向きとすると自重によりチュ−ブが変形し折り目等が発
生するため、下向きに取り付けなければならない。
[0020] The annular die 3 must be installed facing downwards, since if it faces upwards with respect to the extruder 2, the tube will deform due to its own weight and creases will occur.

【0021】環状ダイ3の構造は、何等制限されるもの
ではないが、チューブの肉厚の均一性という点からはス
パイラルダイが好ましい。また、単層ダイでも多層ダイ
でもよく、多層ダイの場合において各層の樹脂組成物は
同一のものであってもよいし、異なるものであってもよ
い。
The structure of the annular die 3 is not limited in any way, but a spiral die is preferable from the viewpoint of uniformity of the wall thickness of the tube. Further, the die may be a single layer die or a multilayer die, and in the case of a multilayer die, the resin compositions of each layer may be the same or different.

【0022】マンドレル5は環状ダイ3の下方に離隔し
て位置させてあるが、環状ダイ3の下方に接続してもよ
く、環状ダイ3を貫通して外部の構造体に接続してもよ
い。
Although the mandrel 5 is spaced apart below the annular die 3, it may be connected below the annular die 3 or may pass through the annular die 3 and be connected to an external structure. .

【0023】環状ダイ3のダイリップと溶融状態のチュ
ーブが最初にマンドレル5に接する位置との距離は20
mm以上500mm以下が望ましい。20mm未満とす
ると、ダイリップとマンドレル5間でチューブが急激に
変形するため切断し易くなり、連続生産が困難となる。 一方、500mm以上とすると、ダイリップとマンドレ
ル5間のチューブにおいて溶融張力の小さい溶融チュー
ブの占める割合が大となるためチューブ形状が不安定と
なり、安定的連続生産が困難となる。
The distance between the die lip of the annular die 3 and the position where the molten tube first contacts the mandrel 5 is 20
It is desirable that the length is not less than mm and not more than 500 mm. If it is less than 20 mm, the tube will deform rapidly between the die lip and the mandrel 5, making it easy to cut and making continuous production difficult. On the other hand, if the length is 500 mm or more, the molten tube with low melt tension will occupy a large proportion of the tube between the die lip and the mandrel 5, making the tube shape unstable and making stable continuous production difficult.

【0024】環状ダイ3のダイリップの直径D1 とマ
ンドレル5の直径D2 との関係は、図3に示すように
、D2 =3D1以下、D2 =0.5D1 以上とす
ることが望ましく、好ましくはD2 =1.5D1 以
下、D2 =0.6D1 以上であり、さらに好ましく
はD2 =0.99D1 以下、D2 =0.8D1 
以上である。マンドレル5の直径D2 が3D1 以上
であると、溶融状態のチューブがマンドレル5に接する
位置でスティックスリップによる垂みが発生し、長手方
向に肉厚の均一なチューブが得られなくなる。一方、D
2 が0.5D1 未満であると、溶融状態のチューブ
が円周方向において同時にマンドレル5に接触しなくな
り、肉厚の均一なチューブが得られなくなる。
As shown in FIG. 3, the relationship between the diameter D1 of the die lip of the annular die 3 and the diameter D2 of the mandrel 5 is preferably D2 = 3D1 or less and D2 = 0.5D1 or more, preferably D2 = 1.5D1 or less, D2 = 0.6D1 or more, more preferably D2 = 0.99D1 or less, D2 = 0.8D1
That's all. If the diameter D2 of the mandrel 5 is 3D1 or more, stick-slip sag occurs at the position where the molten tube contacts the mandrel 5, making it impossible to obtain a tube with a uniform wall thickness in the longitudinal direction. On the other hand, D
If 2 is less than 0.5D1, the molten tube will not contact the mandrel 5 at the same time in the circumferential direction, making it impossible to obtain a tube with a uniform wall thickness.

【0025】もっとも望ましくは、図3に示すように、
ダイリップの直径D1 よりマンドレル5の直径D2 
を若干小とし、マンドレル5にチューブを完全に接触さ
せて温調固化させるとよい。
Most preferably, as shown in FIG.
The diameter D2 of the mandrel 5 is determined by the diameter D1 of the die lip.
It is preferable to make the temperature slightly smaller and bring the tube into complete contact with the mandrel 5 for solidification at controlled temperature.

【0026】マンドレル5の環状ダイ3側の周縁部は2
mmR以上20mmR以下の面取りをするのが好ましい
The peripheral edge of the mandrel 5 on the annular die 3 side is 2
It is preferable to chamfer with a radius of mmR or more and 20 mm or less.

【0027】マンドレル5の長手方向の長さは、望まし
くは10mm以上であるが、20mm以上かつダイリッ
プの直径D1 の3倍以下が好ましい。10mm未満で
あると、ダイリップとマンドレル5と溶融状態のチュー
ブとで囲まれた空間内の圧力制御が不安定となる。ダイ
リップの直径D1 の3倍以上となると、固化したチュ
ーブとマンドレル5側面との摩擦力が増大し、マンドレ
ル5と続いて位置するニップロール9との間で固化した
チューブが塑性変形し、チューブの肉厚が不均一になる
The length of the mandrel 5 in the longitudinal direction is preferably 10 mm or more, but preferably 20 mm or more and 3 times or less the diameter D1 of the die lip. If it is less than 10 mm, pressure control within the space surrounded by the die lip, mandrel 5, and molten tube will become unstable. When the diameter D1 of the die lip is three times or more, the frictional force between the solidified tube and the side surface of the mandrel 5 increases, and the solidified tube is plastically deformed between the mandrel 5 and the nip roll 9 located next, causing the wall of the tube to deteriorate. The thickness becomes uneven.

【0028】マンドレル5の表面状態は0.3μ以上の
凹凸を有するいわゆる梨地加工処理とするのが望ましく
、好ましくは凹凸を0.5μ以上25μ以下とし、さら
に好ましくは1μ以上10μ以下とするのがよい。凹凸
が0.3μ未満であると、溶融状態のチューブがマンド
レル5に接する位置でスティックスリップを発生し長手
方向に均一な肉厚のチューブが得られなくなり、凹凸が
25μ以上であると、チューブの内面に引掻き傷が発生
するとともに、ダイリップとマンドレル5と溶融状態の
チューブとで囲まれた空間内の圧力制御が不安定となる
[0028] The surface condition of the mandrel 5 is desirably treated with a so-called satin finish having an unevenness of 0.3μ or more, preferably 0.5μ or more and 25μ or less, and more preferably 1μ or more and 10μ or less. good. If the unevenness is less than 0.3μ, stick-slip will occur at the position where the molten tube contacts the mandrel 5, making it impossible to obtain a tube with a uniform wall thickness in the longitudinal direction.If the unevenness is 25μ or more, the tube will Scratches occur on the inner surface, and pressure control within the space surrounded by the die lip, mandrel 5, and molten tube becomes unstable.

【0029】マンドレル5の素材は金属、セラミックス
、木、布等が望ましく、好ましくは金属またはセラミッ
クスである。テフロン等のプラスチック素材はスティッ
クスリップが発生し易いため好ましくない。
The material of the mandrel 5 is preferably metal, ceramics, wood, cloth, etc., and preferably metal or ceramics. Plastic materials such as Teflon are not preferred because they tend to cause stick-slip.

【0030】マンドレル5は、真円で長手方向直径を一
定としたもの、あるいはダイリップに近い側の直径を大
とし5/100以下の勾配を有する逆テーパー状とした
もの、いずれであってもよい。
The mandrel 5 may be a perfect circle with a constant diameter in the longitudinal direction, or may have a reverse tapered shape with a larger diameter on the side closer to the die lip and a slope of 5/100 or less. .

【0031】マンドレル5の表面温度はガラス転位点(
Tg)以下あるいは融点(Tm)以下とすることが望ま
しく、好ましくはTg−10℃以下あるいはTm−10
℃以下である。TgあるいはTm以上となるとマンドレ
ル5上でスティックスリップが発生し、長手方向に肉厚
の均一なチューブが得られなくなる。
The surface temperature of the mandrel 5 is the glass transition point (
It is desirable that the temperature be below Tg) or below the melting point (Tm), preferably below Tg-10°C or below Tm-10
below ℃. When the temperature exceeds Tg or Tm, stick-slip occurs on the mandrel 5, making it impossible to obtain a tube with a uniform wall thickness in the longitudinal direction.

【0032】マンドレル5の表面温度調整には公知の手
段を採用し得るが、温調精度および温調能力の点から、
マンドレル5内部に温調した熱媒を循環させるようにす
るのが望ましい。
Although known means can be used to adjust the surface temperature of the mandrel 5, from the viewpoint of temperature control accuracy and temperature control ability,
It is desirable to circulate a temperature-controlled heating medium inside the mandrel 5.

【0033】ダイリップとマンドレル5と溶融状態のチ
ューブとで囲まれた空間には、供給圧力と供給量を制御
した気体を連続的に供給しかつ排出する必要があり、前
記空間が密閉状態にあると、チユーブの肉厚の均一性に
は影響を与えない程度の微小な引取りむらを起生し、あ
るいはダイリップとマンドレル5との間の溶融状態にあ
るチューブが周方向において同時に接触しなくなり、肉
厚の均一なチューブが得られなくなる。
[0033] It is necessary to continuously supply and discharge gas with controlled supply pressure and supply amount to the space surrounded by the die lip, mandrel 5, and molten tube, and the space is kept in a sealed state. This may cause slight unevenness in the drawing that does not affect the uniformity of the wall thickness of the tube, or the tube in a molten state between the die lip and the mandrel 5 may not be in contact with each other in the circumferential direction at the same time. A tube with uniform wall thickness cannot be obtained.

【0034】連続的に供給する気体としては空気、窒素
が好ましく、また供給する気体の温度は一定温度とする
ことが好ましい。
The gas to be continuously supplied is preferably air or nitrogen, and the temperature of the gas to be supplied is preferably constant.

【0035】図1および図3に示すように、溶融状態の
チューブがマンドレル5に接する位置の近傍において、
環状ダイ3の中心とマンドレル5の中心とを通る垂直面
で切った断面に関し、溶融状態のチューブがマンドレル
5に接する点をA点とし、このA点直近上位のチューブ
上の点をB点とし、A点を通り環状ダイ3の中心とマン
ドレル5の中心とを通る線に平行な線上の点をC点とす
る。
As shown in FIGS. 1 and 3, near the position where the molten tube contacts the mandrel 5,
Regarding the cross section cut along the vertical plane passing through the center of the annular die 3 and the center of the mandrel 5, the point where the molten tube touches the mandrel 5 is defined as point A, and the point on the tube immediately above point A is defined as point B. , a point on a line passing through point A and parallel to a line passing through the center of the annular die 3 and the center of the mandrel 5 is defined as point C.

【0036】マンドレル5に向かって左側に関し、A点
とC点を結ぶ線ACと、A点とB点とを結ぶ線ABとの
なす∠CABが時計回りを−、反時計回りを+とすると
き、∠CABは+20°以下−45°以上が望ましく、
好ましくは+10°以下−30°以上、さらに好ましく
は0°以下−20°以上とするとよい。∠CABが+2
0°以上になると、溶融状態のチューブがマンドレル5
に周方向同時に接触しなくなり肉厚の均一なチューブが
得られなくなる。一方、∠CABが−45°未満になる
と、マンドレル5上でスティックスリップが発生し均一
な肉厚のチューブが得られなくなる。
Regarding the left side when facing the mandrel 5, ∠CAB formed by the line AC connecting points A and C and the line AB connecting points A and B, clockwise is - and counterclockwise is +. When ∠CAB is preferably +20° or less and −45° or more,
The angle is preferably +10° or less and −30° or more, more preferably 0° or less and −20° or more. ∠CAB is +2
If the temperature exceeds 0°, the molten tube will move to the mandrel 5.
This prevents simultaneous contact in the circumferential direction, making it impossible to obtain a tube with uniform wall thickness. On the other hand, when ∠CAB is less than -45°, stick-slip occurs on the mandrel 5, making it impossible to obtain a tube with uniform wall thickness.

【0037】固化したチューブに折り目を付けずに連続
的に引取る手段としては、ニップロ−ルを採用する。連
続的に移動しているチューブの内側に支持管棒の周囲に
少なくとも2ケ所以上に内側ロール7を取付け、これら
に内側ロール7に対応してチューブの外側にゴム弾性体
で被覆した外側ロール8を配設し、。内側ロール7と外
側ロール8とによりチューブを挾み付けることによりチ
ュ−ブを連続的に引き取る。。
[0037] As a means for continuously taking off the solidified tube without creating creases, a nip roll is employed. Inside the continuously moving tube, inner rolls 7 are attached at at least two places around the support tube rod, and corresponding to these inner rolls 7, outer rolls 8 covered with a rubber elastic material are provided on the outside of the tube. and. By sandwiching the tube between an inner roll 7 and an outer roll 8, the tube is continuously taken up. .

【0038】チューブを引取る駆動力は、外側ロール8
側に付与する方が装置の簡易性、操作性の点から好まし
い。
The driving force for taking up the tube is provided by the outer roll 8.
It is preferable to apply it to the side from the viewpoint of simplicity and operability of the device.

【0039】ニップロール9により引き取ったチューブ
は、多少の変形が許される場合には、チューブ内に気体
を保持したままの状態で巻取ることができるし、僅かの
変形も許されない場合には、ニップロール9より引き取
ったチューブを所望の長さに輪切り状に切断すればよい
If the tube taken up by the nip rolls 9 is allowed to be slightly deformed, it can be wound up while retaining the gas inside the tube, and if even a slight deformation is not allowed, the tube can be taken up by the nip rolls. What is necessary is just to cut the tube taken out from 9 into round slices to a desired length.

【0040】本発明により得るチューブの肉厚は10μ
以上2000μ以下が望ましく、好ましくは20μ以上
1000μ以下である。チューブの肉厚が10μ未満に
なると、ニップロール9で引き取る際塑性変形し肉厚の
均一なチューブが得られない。2000μ以上になると
、マンドレル5上での冷却が困難となる。
The wall thickness of the tube obtained according to the present invention is 10μ.
The thickness is preferably 20μ or more and 2000μ or less, preferably 20μ or more and 1000μ or less. If the wall thickness of the tube is less than 10 μm, plastic deformation occurs when the tube is taken off by the nip rolls 9, making it impossible to obtain a tube with a uniform wall thickness. When the thickness exceeds 2000μ, cooling on the mandrel 5 becomes difficult.

【0041】このように、押出機2に装着した環状ダイ
3より押出された溶融チューブの外周面を温調リング6
,6′,6″から吹出す気体により温調するとともに、
供給管13より供給圧力・供給流量を制御された気体を
連続して供給して常に内側圧力を所定圧力としながら、
チューブの内側をマンドレル5に接触させて温調固化さ
せ、次いで支持管棒4の周方向に所定間隔毎に配設した
ニップロール9間に通しチューブ状を維持しながら引取
るから、引き取られたチューブを輪切り状に切断しても
継ぎ目、折り目はない。
In this way, the outer peripheral surface of the molten tube extruded from the annular die 3 attached to the extruder 2 is heated by the temperature control ring 6.
, 6′, 6″ to control the temperature,
While continuously supplying gas with controlled supply pressure and supply flow rate from the supply pipe 13 to always keep the internal pressure at a predetermined pressure,
The inside of the tube is brought into contact with a mandrel 5 to solidify at a controlled temperature, and then passed between nip rolls 9 arranged at predetermined intervals in the circumferential direction of the support tube rod 4 and taken off while maintaining the tube shape. Even when cut into rounds, there are no seams or creases.

【0042】なお、得られたチューブは、熱的、経時的
寸法安定性を向上するため、また微小な塑性変形を修正
するために、張力を付与した状態で熱処理するとよい。
[0042] The obtained tube is preferably heat-treated under tension in order to improve its thermal and temporal dimensional stability and to correct minute plastic deformations.

【0043】次に、本発明の具体的実施例について説明
する。
Next, specific embodiments of the present invention will be explained.

【0044】(実施例1)ダイリツプの外径140mm
φ、リップ間隙1mmの4条環状スパイラルダイとした
環状ダイ3を貫通する支持管棒4に、外径135mmφ
、側面の長さ50mm、環状ダイ3側の周縁を5mmR
で面取りし、アルミナ系セラミックスを表面凹凸2μに
なるように溶射した鋼製マンドレル5を環状ダイ3の端
面より100mmの位置に取付ける。さらに、マンドレ
ル5の下端より下方100mmの位置に10mmφのゴ
ム製内側ロ−ル7,7を取り付け、これら2個の内側ロ
ール7,7にそれぞれ対応してチューブの外側に位置し
、かつモーター(図示しない)によって駆動される50
mmφのゴム製外側ロール8,8を設け、内側ロール7
と外側ロール8とからニップロール9,9を構成する。
(Example 1) Outer diameter of die lip: 140 mm
A support tube rod 4 with an outer diameter of 135 mmφ is inserted through the annular die 3, which is a four-row annular spiral die with a lip gap of 1 mm.
, the length of the side surface is 50mm, and the circumference on the annular die 3 side is 5mmR.
A steel mandrel 5, which has been chamfered with 100 mm and is sprayed with alumina ceramics so that the surface unevenness is 2 μm, is attached at a position 100 mm from the end face of the annular die 3. Furthermore, rubber inner rolls 7, 7 with a diameter of 10 mm are attached to a position 100 mm below the lower end of the mandrel 5, and a motor ( (not shown)
mmφ rubber outer rolls 8, 8 are provided, and an inner roll 7 is provided.
and the outer roll 8 constitute nip rolls 9, 9.

【0045】メルトフローレート(MFR)が4.6g
/10分(280℃)のポリカーボネート(三菱瓦斯化
学(株)製ユーピロンE−2000)83重量部、MF
Rが4.32g/10分(230℃)のポリブチレンテ
レフタレート(三菱化成(株)製ノバドール5020)
17重量部、および比表面積70m2 /gのアセチレ
ンブラック(電気化学(株)製)16重量部をベント付
二軸押出機を用いて混練造粒し、得られたペレットを、
50mmφの押出機より280℃の温度で押出し、環状
ダイ3に近接した温調リング6より150℃の空気を、
マンドレルの上端より上方20mmの位置の温調リング
6′より80℃の空気を、マンドレルの上端より下方2
0mmの位置の温調リング6″より80℃の空気をそれ
ぞれ吹き付けるとともに、供給管13から0.03kg
/cm2 、INL/minの空気を供給し、∠CAB
を−5°とした溶融状態のチューブを、供給管17から
85℃の温水を2L/minで循環させてあるマンドレ
ル5に接触せしめた後、ニップロール9,9によって2
m/minで引き取り、肉厚150μのチューブを得た
[0045] Melt flow rate (MFR) is 4.6g
/10 minutes (280°C) polycarbonate (Iupilon E-2000 manufactured by Mitsubishi Gas Chemical Co., Ltd.) 83 parts by weight, MF
Polybutylene terephthalate with R of 4.32 g/10 min (230°C) (Novadol 5020 manufactured by Mitsubishi Kasei Corporation)
17 parts by weight and 16 parts by weight of acetylene black (manufactured by Denki Kagaku Co., Ltd.) with a specific surface area of 70 m2/g were kneaded and granulated using a vented twin-screw extruder, and the resulting pellets were
Extruded from a 50 mmφ extruder at a temperature of 280°C, air at 150°C was passed through a temperature control ring 6 near the annular die 3,
Air at a temperature of 80°C is supplied from the temperature control ring 6' located 20 mm above the top of the mandrel.
Air at 80°C is blown from the temperature control ring 6'' at the 0mm position, and 0.03kg is supplied from the supply pipe 13.
/cm2, INL/min of air, ∠CAB
The tube in a molten state with -5° is brought into contact with the mandrel 5 in which hot water of 85°C is circulated at 2 L/min from the supply pipe 17, and then 2
A tube with a wall thickness of 150 μm was obtained by drawing at a speed of m/min.

【0046】得られたチューブの長手方向の直径変化は
±0.5mmであり、円周方向の肉厚変化は±5%であ
った。又、表面抵抗計ハイレスタHAプローブ(三菱油
化(株)製)を用い、測定電圧100v、測定時間10
秒で評価したところ、長手方向および円周方向の表面抵
抗は3×108 〜8×108 Ω/口の範囲にあり電
子写真式複写機用の抵抗制御エンドレスベルトとして十
分満足のいくものであった。
The diameter change in the longitudinal direction of the obtained tube was ±0.5 mm, and the wall thickness change in the circumferential direction was ±5%. In addition, using a surface resistance meter Hiresta HA probe (manufactured by Mitsubishi Yuka Co., Ltd.), the measurement voltage was 100V, and the measurement time was 10.
When evaluated in seconds, the surface resistance in the longitudinal and circumferential directions was in the range of 3 x 108 to 8 x 108 Ω/mouth, which was sufficiently satisfactory as a resistance control endless belt for electrophotographic copying machines. .

【0047】[0047]

【発明の効果】本発明によれば、直径と肉厚が均一で、
かつ、表面抵抗も均一な折り目のない抵抗制御エンドレ
スベルト材を製造することができ、所望の長さに輪切り
状に切断し、電子写真式複写機用の抵抗制御エンドレス
ベルトとして好適に使用できる。
[Effect of the invention] According to the present invention, the diameter and wall thickness are uniform;
In addition, a resistance-controlled endless belt material with uniform surface resistance and no creases can be produced, which can be cut into slices of a desired length and suitably used as a resistance-controlled endless belt for electrophotographic copying machines.

【図面の簡単な説明】[Brief explanation of the drawing]

【図1】本発明の抵抗制御エンドレスベルト材の製造方
法に適用する装置の要部断面図である。
FIG. 1 is a sectional view of a main part of an apparatus applied to the method of manufacturing a resistance-controlled endless belt material of the present invention.

【図2】図1におけるA−A線から視た断面図である。FIG. 2 is a sectional view taken along line AA in FIG. 1;

【図3】環状ダイとマンドレルとチューブとの関係を示
す説明図である。
FIG. 3 is an explanatory diagram showing the relationship between an annular die, a mandrel, and a tube.

【符号の説明】[Explanation of symbols]

1  抵抗制御エンドレスベルト材の製造装置2  押
出機 3  環状ダイ 4  支持管棒 5  マンドレル 6,6′,6″  温調リング 7  内側ロール 8  外側ロール 9  ニップロール 10  供給圧力・供給流量制御気体連続供給機構11
  マンドレル内熱媒供給機構
1 Resistance control endless belt material manufacturing device 2 Extruder 3 Annular die 4 Support pipe rod 5 Mandrel 6, 6', 6'' Temperature control ring 7 Inner roll 8 Outer roll 9 Nip roll 10 Supply pressure/supply flow rate control gas continuous supply mechanism 11
Heat medium supply mechanism in mandrel

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  導電性フィラーを配合した熱可塑性樹
脂組成物を溶融し、押出機に装着した環状ダイより下方
にチューブ状に押し出し、このチューブの外周面に温調
した気体を吹き付けるとともに、チューブの内側に供給
圧力と供給流量を制御した気体を連続的に供給・排除さ
せ、次いで、温調されたマンドレルに接触させるととも
に、マンドレルに接触を開始する近傍のチューブの外周
面に再度温調した気体を吹き付け、しかる後、チューブ
状を維持したままで連続して引き取って輪切り状に切断
するようにしたことを特徴とする抵抗制御エンドレスベ
ルト材の製造方法。
Claim 1: A thermoplastic resin composition containing a conductive filler is melted and extruded into a tube shape downward through an annular die attached to an extruder, and a temperature-controlled gas is blown onto the outer circumferential surface of the tube. Gas with controlled supply pressure and supply flow rate was continuously supplied and expelled to the inside of the tube, and then it was brought into contact with a temperature-controlled mandrel, and the temperature was again controlled on the outer peripheral surface of the tube near where it started contacting the mandrel. 1. A method for producing a resistance-controlled endless belt material, which comprises blowing a gas, and then continuously pulling the material while maintaining the tube shape to cut it into circular slices.
JP2414872A 1990-12-27 1990-12-27 Manufacturing method of resistance control endless belt material Expired - Lifetime JP2886350B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2414872A JP2886350B2 (en) 1990-12-27 1990-12-27 Manufacturing method of resistance control endless belt material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2414872A JP2886350B2 (en) 1990-12-27 1990-12-27 Manufacturing method of resistance control endless belt material

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP8228864A Division JP2886505B2 (en) 1996-08-29 1996-08-29 Endless belt material with resistance control

Publications (2)

Publication Number Publication Date
JPH04255332A true JPH04255332A (en) 1992-09-10
JP2886350B2 JP2886350B2 (en) 1999-04-26

Family

ID=18523303

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2886350B2 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1014203A3 (en) * 1998-12-22 2000-10-25 Canon Kabushiki Kaisha Endless belt for electrophotography, process for producing the endless belt, and image forming apparatus having the endless belt
JP2001042657A (en) * 1999-07-27 2001-02-16 Canon Inc Belt-like transfer member, production and image forming device
US6470165B2 (en) 2000-02-03 2002-10-22 Canon Kabushiki Kaisha Process for producing transfer member, transfer member, and image forming apparatus
WO2005033188A1 (en) * 2003-10-06 2005-04-14 Kureha Corporation Semiconductive film, electric charge control member and process for producing the semiconductive film
JP2012045804A (en) * 2010-08-26 2012-03-08 Canon Inc Method and apparatus of manufacturing hollow extrusion molded article using thermoplastic resin
JP2016117162A (en) * 2014-12-18 2016-06-30 富士ゼロックス株式会社 Extrusion molding device, and annular member
EP3043215A1 (en) 2015-01-09 2016-07-13 Ricoh Company Ltd. Semiconductive resin composition, member for electrophotography and image forming apparatus
US9891558B2 (en) 2015-01-09 2018-02-13 Ricoh Company, Ltd. Semiconductive resin composition, member for electrophotography and image forming apparatus

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1014203A3 (en) * 1998-12-22 2000-10-25 Canon Kabushiki Kaisha Endless belt for electrophotography, process for producing the endless belt, and image forming apparatus having the endless belt
JP2001042657A (en) * 1999-07-27 2001-02-16 Canon Inc Belt-like transfer member, production and image forming device
US6470165B2 (en) 2000-02-03 2002-10-22 Canon Kabushiki Kaisha Process for producing transfer member, transfer member, and image forming apparatus
WO2005033188A1 (en) * 2003-10-06 2005-04-14 Kureha Corporation Semiconductive film, electric charge control member and process for producing the semiconductive film
JP2005112942A (en) * 2003-10-06 2005-04-28 Kureha Chem Ind Co Ltd Semi-conductive film, charge control member, and method for producing semi-conductive film
JP4563665B2 (en) * 2003-10-06 2010-10-13 株式会社クレハ Semiconductive film, charge control member, and method for producing semiconductive film
US8283031B2 (en) 2003-10-06 2012-10-09 Kureha Corporation Semiconductive film, electric charge control member and process for producing the semiconductive film
JP2012045804A (en) * 2010-08-26 2012-03-08 Canon Inc Method and apparatus of manufacturing hollow extrusion molded article using thermoplastic resin
JP2016117162A (en) * 2014-12-18 2016-06-30 富士ゼロックス株式会社 Extrusion molding device, and annular member
EP3043215A1 (en) 2015-01-09 2016-07-13 Ricoh Company Ltd. Semiconductive resin composition, member for electrophotography and image forming apparatus
US9891558B2 (en) 2015-01-09 2018-02-13 Ricoh Company, Ltd. Semiconductive resin composition, member for electrophotography and image forming apparatus
US9921526B2 (en) 2015-01-09 2018-03-20 Ricoh Company, Ltd. Semiconductive resin composition, member for electrophotography and image forming apparatus

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