JPH0325113Y2 - - Google Patents

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Publication number
JPH0325113Y2
JPH0325113Y2 JP17017185U JP17017185U JPH0325113Y2 JP H0325113 Y2 JPH0325113 Y2 JP H0325113Y2 JP 17017185 U JP17017185 U JP 17017185U JP 17017185 U JP17017185 U JP 17017185U JP H0325113 Y2 JPH0325113 Y2 JP H0325113Y2
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JP
Japan
Prior art keywords
cylinder
burner
drying
annular
annular boiler
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
Application number
JP17017185U
Other languages
Japanese (ja)
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JPS6184493U (en
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Filing date
Publication date
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Priority to JP17017185U priority Critical patent/JPH0325113Y2/ja
Publication of JPS6184493U publication Critical patent/JPS6184493U/ja
Application granted granted Critical
Publication of JPH0325113Y2 publication Critical patent/JPH0325113Y2/ja
Expired legal-status Critical Current

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Description

【考案の詳細な説明】 本考案は、例えば経糸糊付乾燥機内に備える糊
付経糸の乾燥シリンダや織布、紙、フイルムなど
の乾燥シリンダドラムに関し、この乾燥シリンダ
を熱効率良く均等加熱するように改良したもので
ある。
[Detailed description of the invention] The present invention relates to a cylinder drum for drying sizing warp yarns and a drying cylinder drum for woven fabric, paper, film, etc., provided in a warp sizing dryer, for example. This is an improved version.

例えば、経糸糊付機や染色布の乾燥工程におい
ては、特公昭57−19211、同57−43651、実公昭56
−24392(ボイラは図示されていない)に見るよ
う、外部配置のボイラによつて発生する加熱蒸気
でシリンダを加熱し、このシリンダに巻き掛けた
経糸や布を乾燥させている。この蒸気でシリンダ
を加熱する方式の欠点は、蒸気発生までのウオ
ーミングアツプに多くの時間(1〜2時間)と熱
エネルギを必要とする。蒸気もれによる熱効率
の低下や運転費の増大と蒸気もれ箇所の修理費及
び膨大な修理時間を要すること、熱交換効率の
低いことによる燃費の増大や大規模なボイラ設備
とその管理技術の必要性、設備機械の大型化に
よる広いフロアスペースの必要性、保守、点検
の困難さなどがある、等である。
For example, in the warp sizing machine and the drying process of dyed cloth,
-24392 (the boiler is not shown), the cylinder is heated with heated steam generated by an external boiler, and the warp and cloth wound around the cylinder are dried. The disadvantage of this method of heating the cylinder with steam is that it requires a lot of time (1 to 2 hours) and thermal energy for warming up before steam generation. Decreased thermal efficiency and increased operating costs due to steam leaks; repair costs and time required for steam leaks; increased fuel consumption due to low heat exchange efficiency; and large-scale boiler equipment and its management technology. These include the need for larger floor spaces due to larger equipment, and the difficulty of maintenance and inspection.

このように、蒸気式の乾燥シリンダの加熱装置
は、多くの欠点をもち、ウオーミングアツプ時間
の短縮やランニングコストの低いものをはじめと
した省エネ、省力化、設備費の低減、熱効率の高
いものなどの要求が強く、この要求を満足する乾
燥シリンダ加熱装置の開発が切望されている。
As described above, steam-type drying cylinder heating devices have many drawbacks, such as shortened warming-up time, low running costs, energy saving, labor saving, reduced equipment costs, and high thermal efficiency. There is a strong demand for the development of a dry cylinder heating device that satisfies this demand.

そこで、例えば、実公昭56−55585(シリンダが
乾燥室になつている)や実公昭55−52313(バーナ
がヒーターに置き替えられている紙乾燥用のドラ
ムヒータである)の如く、直火式ガスバーナでシ
リンダ内に火炎を吹き込み、効率良く加熱する方
法が考えられる。しかし、この方式ではシリンダ
表面が均等に加熱されないばかりか、経糸や布、
紙、フイルム等の乾燥シリンダとして使用中にシ
リンダの回転がとめられると、シリンダ表面温度
が急上昇し、経糸などを焼き切るという問題があ
つて採用されにくい方式である。また、シリンダ
軸受部の過熱で軸受不良を発生することがある。
Therefore, for example, direct-fire type models such as Utility Model No. 56-55585 (in which the cylinder serves as a drying chamber) and Utility Model No. 55-52313 (which is a drum heater for paper drying in which the burner is replaced with a heater) are available. One possible method is to use a gas burner to blow flame into the cylinder to heat it efficiently. However, with this method, not only the cylinder surface is not evenly heated, but also the warp, cloth,
This method is difficult to adopt because if the rotation of the cylinder is stopped during use as a drying cylinder for paper, film, etc., the surface temperature of the cylinder will rise rapidly and the warp threads will be burned out. Furthermore, overheating of the cylinder bearing may cause bearing failure.

本考案は、従来の蒸気式加熱装置及び直火式バ
ーナ加熱装置等のもつ欠点をすべて解消した新規
な乾燥シリンダの均等加熱装置を提供せんとする
ものである。
The present invention aims to provide a new uniform heating device for drying cylinders that eliminates all the drawbacks of conventional steam heating devices, direct flame heating devices, etc.

即ち、本考案のシリンダ加熱装置は、加熱源に
直火式バーナ(ガス又はオイルバーナのことで、
以下単にバーナという)の採用と熱交換器に蒸気
管群の採用で熱効率を飛躍的に向上させたこと
と、シリンダ全表面を均一温度に加熱すべく、シ
リンダ内にバーナと蒸気管で蒸気を発生する環状
ボイラ筒を内蔵し、この真空中の環状ボイラ筒内
で発生した加熱蒸気を真空構造とした乾燥シリン
ダに送り込んでシリンダを均等加熱させ、ここで
復水した水は、シリンダの回動運動の利用で再び
ボイラ内へ戻され、再加熱されるようにした。こ
れにより、シリンダが迅速に均等加熱されるほ
か、シリンダ表面温度が真空中に於ける蒸気温度
の為に(60〜160℃)に制御可能となり、また、
シリンダの表面温度も均等に加熱される利点があ
り、断熱軸受で軸受部の断熱効率を向上させるこ
とに成功した。
That is, the cylinder heating device of the present invention uses a direct flame burner (gas or oil burner) as a heat source.
Thermal efficiency has been dramatically improved by adopting a burner (hereinafter simply referred to as a burner) and a group of steam pipes in the heat exchanger. The heated steam generated in the annular boiler cylinder in a vacuum is sent to a vacuum-structured drying cylinder to uniformly heat the cylinder, and the water condensed here is absorbed by the rotation of the cylinder. By using motion, it was returned to the boiler and reheated. As a result, the cylinder is heated quickly and evenly, and the cylinder surface temperature can be controlled to (60 to 160℃) due to the steam temperature in a vacuum.
This has the advantage that the surface temperature of the cylinder is evenly heated, and we succeeded in improving the heat insulation efficiency of the bearing section with the heat insulated bearing.

以下、図面の実施例で本考案を説明する。第1
図は経糸糊付乾燥機Kの一実施例を示し、ビーム
スタンドに軸架した所要数のビーム1より繰出し
た各経糸列2を糊槽3にあるローラ4、絞りロー
ラ5を介して糊付けしたのち、乾燥室6に送る。
この乾燥室6内で糊付け湿潤した経糸列2を順次
乾燥させ、上部に備えた多数の乾燥シリンダ10
…で上下に屈曲させつゝそのシリンダ表面で乾燥
させる。このシリンダ10…の表面温度は60〜
160℃の範囲内に温度管理されており、その温度
分布が均等であることを要求される。本考案にお
いては、上記経糸糊付乾燥機Kや布、紙、フイル
ム用に適用される。この乾燥シリンダ10…を均
等加熱させる加熱装置を提供する(後記)。乾燥
済みの経糸列2は筬(図示なし)を通して織機ビ
ーム9に捲取る。
Hereinafter, the present invention will be explained with reference to the embodiments shown in the drawings. 1st
The figure shows an embodiment of the warp sizing dryer K, in which each warp row 2 let out from a required number of beams 1 mounted on a beam stand is sized via rollers 4 and squeezing rollers 5 in a sizing tank 3. Afterwards, it is sent to the drying room 6.
The warp rows 2 that have been glued and moistened are dried one after another in this drying chamber 6, and a large number of drying cylinders 10 provided at the upper part
...and bend it up and down and dry it on the surface of the cylinder. The surface temperature of this cylinder 10... is 60~
The temperature is controlled within a range of 160℃, and the temperature distribution is required to be uniform. The present invention is applied to the warp sizing dryer K, cloth, paper, and film. A heating device for uniformly heating the drying cylinders 10 is provided (described later). The dried warp row 2 is passed through a reed (not shown) and wound onto a loom beam 9.

続いて、本考案の乾燥シリンダ均等加熱装置1
00の実施例を説明する。例えば、ステンレス鋼
材等の不錆性材金属で作られた乾燥シリンダ10
及びこの両端フランジ13a,13aは、小径軸支
筒14,14′のボス(フランジ)14a,14′a
にボルトで気密に連結され、空気層を形成した軸
受部材11′,12′で断熱的に承持されている。
即ち、排気側の小径軸支筒14には、奥端をリン
グ14bで閉塞した断熱筒20が挿入され、この
断熱筒20からの排気圧によつて生じる間隙X内
の熱い負圧空気が小孔イからの低い温度の空気導
入によつて排出され、間隙Xの断熱作用が発揮さ
れる。また、バーナ(オイル又はガスバーナ)
BO側の小径軸支筒14′についても、バーナのフ
アンからの燃焼のための冷風を流通させるドラフ
トチユーブに小穴14′bを刻設し、これで軸受1
1′への断熱作用を発揮させている。2重構造の
断面リング状の環状ボイラ筒13は、バーナ側が
フランジ13aの内壁に連結され、排気側が内筒
13′の尾端に連結した熱膨張吸収21を介して
フランジ内壁14aに連結した円板22に支持さ
れている。これで、環状ボイラ筒13がバーナで
過熱されたときに生じる熱膨張を吸収する。尚、
シリンダ10内の空間Sは真空とされ、且環状ボ
イラ筒S′内には蒸気発生用の水Wが1/3程度入つ
ており、排気側の端面13aには多数の蒸気吹出
し用の連絡孔13b…が穿たれている。上記環状
ボイラ筒13の円筒13′内側における加熱空間
S″の排気側半分には、環状の加熱蒸気管23…
がその両端をリング状の真空空間S′内へ気密に進
入させており、各蒸気管23…は90゜ずつその管
端23aをずらせて多数配設されている。このた
め、シリンダ10を時計方向へ回動させると、各
蒸気管23の管端23a…が空間S′の底部の水W
を管内23へ汲み揚げ(第5図参照)、管内に流
入した水Wはバーナによる加熱でたちまち熱効率
良く加熱蒸気a…となり管端23a…から水Wの
ない部分の空間S′へ吹き出し、反バーナ側に設け
た連絡孔13b…からシリンダ10内の空間Sへ
蒸気aが広く送られる。ここでシリンダ10を均
等加熱した蒸気は復水Dとなつてシリンダ底部に
溜められる。尚、24は火炎fが効果良く各蒸気
管23を加熱するための円錘ガイド筒であり、円
筒13の内壁側中心に支持されている。
Next, the drying cylinder uniform heating device 1 of the present invention
An example of 00 will be explained. For example, the drying cylinder 10 is made of rust-resistant metal such as stainless steel.
The flanges 13 a and 13 a at both ends are the bosses (flanges) 14 a and 14' a of the small diameter shaft support tubes 14 and 14 '.
The bearing members 11' and 12' are airtightly connected to each other by bolts, and are adiabatically supported by bearing members 11' and 12' in which an air layer is formed.
That is, an insulating cylinder 20 whose rear end is closed with a ring 14b is inserted into the small diameter shaft support cylinder 14 on the exhaust side, and hot negative pressure air in the gap X generated by the exhaust pressure from this insulating cylinder 20 is The air is discharged by introducing low temperature air through the small hole A, and the heat insulating effect of the gap X is exerted. Also, burner (oil or gas burner)
For the small-diameter shaft support tube 14' on the B O side, a small hole 14'b is also carved in the draft tube through which cold air for combustion from the burner fan flows, and this allows the bearing 1
1' exerts a heat insulating effect. The annular boiler cylinder 13, which has a ring-shaped cross section and has a double structure, has a burner side connected to the inner wall of the flange 13a , and an exhaust side connected to the flange inner wall 14a via a thermal expansion absorber 21 connected to the tail end of the inner cylinder 13 ' . It is supported by a circular plate 22. This absorbs the thermal expansion that occurs when the annular boiler cylinder 13 is overheated by the burner. still,
The space S inside the cylinder 10 is made vacuum, and the annular boiler cylinder S' is filled with about 1/3 of the water W for steam generation, and the end surface 13a on the exhaust side has a large number of connections for blowing out steam. Holes 13b ... are bored. Heating space inside the cylinder 13' of the annular boiler cylinder 13
On the exhaust side half of S'', an annular heating steam pipe 23...
has both ends hermetically entered into the ring-shaped vacuum space S', and a large number of steam pipes 23 are arranged with their pipe ends 23 a shifted by 90 degrees. Therefore, when the cylinder 10 is rotated clockwise, the pipe ends 23 a of each steam pipe 23...
is pumped up into the pipe 23 (see Fig. 5), and the water W flowing into the pipe is heated by the burner and immediately becomes heated steam a with thermal efficiency and is blown out from the pipe end 23 a into the space S' where there is no water W. Steam a is widely sent to the space S inside the cylinder 10 from communication holes 13 b provided on the side opposite to the burner. Here, the steam that uniformly heated the cylinder 10 becomes condensate D and is stored at the bottom of the cylinder. Note that 24 is a conical guide tube through which the flame f effectively heats each steam pipe 23, and is supported at the center of the inner wall of the cylinder 13.

最後に、シリンダ10内の底部に溜つた復水D
を環状ボイラ筒13内の真空空間S′へ戻す返還部
材の構成に関し、バーナ側のシリンダ端内に湾曲
した3本のくみ揚げ管160…が放射状に配設さ
れ、第3図の如くその管160の外端がシリンダ
10の内壁に接触し、内端が環状ボイラ筒13の
外周壁に気密に連接して真空空間S′内へ進入して
いる。上記くみ揚げ管160の内端開口部は、真
空空間S′内に120゜間隔で配置した接続箱25…に
連絡しており、この各接続箱25からは第4図の
如く真空空間S′内を円周方向に約130゜前後(各範
囲に亘つて)ずつ位置をずらせて配置した供給管
26…と接続されて、その先端口26a…から真
空空間S′内へ復水Dを排出する構成となつてい
る。即ち、乾燥シリンダ10を時計方向(矢印方
向)へ回動させると、底部の復水Dをくみ揚げ管
160がすくい上げて管内へ導入する。この管内
へ導入された復水Dはシリンダ10の回動がさら
に進んでロからハの回動位置となると、接続箱2
5から供給管26へ復水Dが進み、その先端口2
aから環状ボイラ筒13の外周側となる真空空
間S′内へ供給されるポンプ作用をする。尚、上記
くみ揚げ管160…及び供給管26…の向きで
は、シリンダ10が時計方向の回転に限定される
から、反時計方向用のシリンダとするには、各管
160,26の方向を逆向きとすればよい。ま
た、この実施例によるときは、環状ボイラ筒13
の内周側に加熱蒸気管23…を配置したから、熱
変換効率が非常に高く、更に蒸気吹き出し孔13
…を高温となる環状ボイラ筒の排気側(反バー
ナ側)に設け、復水Dのくみ揚げ管160を低温
となる環状ボイラ筒の外周側であるバーナ側に設
けたから、蒸気及び復水の流水(供給)が良好で
ある。
Finally, the condensate D accumulated at the bottom of the cylinder 10
Regarding the structure of the return member that returns the water to the vacuum space S' in the annular boiler cylinder 13, three curved lifting pipes 160 are arranged radially within the end of the cylinder on the burner side, and as shown in Fig. The outer end of the cylinder 160 contacts the inner wall of the cylinder 10, and the inner end thereof is airtightly connected to the outer circumferential wall of the annular boiler cylinder 13 and enters the vacuum space S'. The inner end opening of the pumping pipe 160 is connected to connection boxes 25 arranged at 120° intervals within the vacuum space S', and each connection box 25 connects to the vacuum space S' as shown in FIG. The inside is connected to the supply pipes 26, which are arranged at positions shifted by about 130 degrees in the circumferential direction (over each range), and the condensate D is introduced into the vacuum space S' from the tip port 26a ... It is configured to discharge. That is, when the drying cylinder 10 is rotated clockwise (in the direction of the arrow), the condensate D at the bottom is scooped up by the lift pipe 160 and introduced into the pipe. When the rotation of the cylinder 10 progresses further and the condensate D introduced into this pipe reaches the rotational position from B to C, the condensate D enters the junction box 2.
5 to the supply pipe 26, and its tip port 2
6a acts as a pump to be supplied into the vacuum space S' on the outer peripheral side of the annular boiler cylinder 13. In addition, since the cylinder 10 is limited to clockwise rotation due to the orientation of the pumping pipes 160 and the supply pipes 26, the direction of each of the pipes 160 and 26 must be reversed to create a counterclockwise cylinder. It is sufficient if it is facing the direction. Further, according to this embodiment, the annular boiler cylinder 13
Since the heating steam pipes 23 are arranged on the inner circumferential side of the
b ... is installed on the exhaust side (anti-burner side) of the annular boiler cylinder where the temperature is high, and the pumping pipe 160 for condensate D is installed on the burner side which is the outer peripheral side of the annular boiler cylinder where the temperature is low. There is good running water (supply).

本考案の乾燥シリンダ10は上述の如くであ
り、その作用を説明する。先ず、乾燥シリンダを
ウオーミングアツプするには、直火式バーナBO
を点火し、センサ(図示なし)からの信号に基づ
き、コントローラ(図示なし)で運転を司どる。
乾燥シリンダの表面温度は、60〜160℃の温度範
囲に制御されるべく、センサからの検出値でバー
ナBOの火炎が調節される。上記乾燥シリンダ内
の環状ボイラ筒13は、燃焼ガスfによりその水
Wをたちまち加熱蒸気aとし、これが右端の連絡
孔13b…を介して乾燥シリンダ10の空間S内
に走り、その全表面を均等な温度で急速加熱す
る。加熱を終えた蒸気は温度低下して復水し、シ
リンダ10の底部にドレンDとして溜められる。
このドレンDは、シリンダ10の時計方向回転で
くみ揚げ管160…が第3,5図の如くくみ揚
げ、その接続部25、供給管26から環状ボイラ
筒13の基端側空間S′へ回収し、再び加熱蒸気a
とすべく、バーナBOによつて再加熱される熱サ
イクルを繰り返す。
The drying cylinder 10 of the present invention is as described above, and its operation will be explained below. First, to warm up the drying cylinder, turn on the open flame burner B O
A controller (not shown) controls operation based on signals from a sensor (not shown).
The flame of burner B O is adjusted based on the detected value from the sensor so that the surface temperature of the drying cylinder is controlled within a temperature range of 60 to 160°C. The annular boiler cylinder 13 in the drying cylinder immediately converts the water W into heated steam a by the combustion gas f, and this runs into the space S of the drying cylinder 10 through the communication hole 13 b at the right end, and spreads over its entire surface. Heat quickly and at an even temperature. After heating, the steam decreases in temperature and condenses, and is stored as a drain D at the bottom of the cylinder 10.
This drain D is pumped up by the pumping pipe 160 as shown in FIGS. 3 and 5 by the clockwise rotation of the cylinder 10, and is collected from the connecting portion 25 and the supply pipe 26 into the base end side space S' of the annular boiler cylinder 13. and heated steam a again
In order to achieve this, a thermal cycle of reheating by burner B O is repeated.

尚、本考案の乾燥シリンダ均等加熱装置は、上
記一実施例に限定されることなく、各部の設計変
更が自由に出来るし、乾燥機も経糸糊付機に限定
されることなく、布染色機の乾燥機や製紙薄板ベ
ニヤ等の帯体物の乾燥機にも適用できる。また、
シリンダ表面温度制御も、シリンダー内部の蒸気
温度をもつて制御するか、もしくは、シリンダ内
圧を検出し、これを一定圧力とするようにバーナ
火力を調節してもよい。
The drying cylinder uniform heating device of the present invention is not limited to the above-mentioned embodiment, and the design of each part can be changed freely, and the dryer is not limited to a warp sizing machine, but can also be used as a cloth dyeing machine. It can also be applied to dryers for paper-making thin veneers and other band products. Also,
The cylinder surface temperature may also be controlled using the steam temperature inside the cylinder, or the cylinder internal pressure may be detected and the burner firepower may be adjusted so as to maintain the pressure at a constant level.

本考案の乾燥シリンダ均等加熱装置によるとき
は、両端の軸支筒を、空気層を形成した断熱軸受
部材で回転自在に承持した乾燥シリンダ内に、二
重構造の環状ボイラ筒を一体気密に承持して上記
乾燥シリンダ、環状ボイラ筒内及び外周を真空構
造となし、この環状ボイラ筒の内周側に火炎を送
るバーナを上記軸支筒の片側に設け、前記環状ボ
イラ筒の内周側の排気側配置した環状加熱蒸気管
はその両端を環状ボイラ筒の外周側に開口させ、
この加熱蒸気管内の加熱蒸気を乾燥シリンダ内へ
送る連絡孔を反バーナ側の端面に穿ち、乾燥シリ
ンダ内で復水したドレン(水)を環状ボイラ筒内
へ戻す返還部材のくみ揚げ管と接続箱、供給管を
バーナ側の乾燥シリンダ内端面及び環状ボイラ筒
の外周側に設けた乾燥シリンダ均等加熱装置とし
たから、加熱源にバーナの採用と蒸気管群の採用
で熱効率を飛躍的に向上させると共に、加熱蒸気
を真空とした乾燥シリンダ内に広く走らせること
で、シリンダ表面が急速且均等温度に加熱される
と共に、その表面温度も蒸気温度以上に上昇する
ことがなくシリンダ内で復水となつたドレンはシ
リンダの回転を利用してボイラ内へ回収されるか
ら、ランニングコストが低く、また、シリンダや
バーナ等の保守、点検の容易化を図ることができ
る。而して、低い設備費とコンパクト化等で経糸
糊付乾燥機や布染色の乾燥機用シリンダとしての
適用性に優れているなど、多くの効果を発揮する
ものである。また、シリンダ軸受部材の断熱性を
向上させる効果もある。
When using the drying cylinder uniform heating device of the present invention, a double-structured annular boiler cylinder is integrally and airtightly placed inside a drying cylinder whose shaft support cylinders at both ends are rotatably supported by insulated bearing members with an air layer formed therein. The drying cylinder, the inside and outer periphery of the annular boiler cylinder are supported by a vacuum structure, and a burner is provided on one side of the shaft support cylinder to send a flame to the inner periphery of the annular boiler cylinder, and the inner periphery of the annular boiler cylinder is The annular heating steam pipe placed on the side exhaust side opens both ends to the outer circumferential side of the annular boiler cylinder,
A communication hole for sending the heated steam in this heated steam pipe into the drying cylinder is bored in the end face on the side opposite to the burner, and connected to the pumping pipe of the return member that returns the condensed water (water) in the drying cylinder to the annular boiler cylinder. The drying cylinder uniform heating device is installed with the box and supply pipes installed on the inner end surface of the drying cylinder on the burner side and on the outer periphery of the annular boiler cylinder.Thermal efficiency is dramatically improved by using a burner and a group of steam pipes as the heating source. At the same time, by running the heated steam widely inside the vacuumed drying cylinder, the cylinder surface is rapidly and uniformly heated, and the surface temperature does not rise above the steam temperature, preventing condensation inside the cylinder. Since the waste drain is collected into the boiler using the rotation of the cylinder, running costs are low, and maintenance and inspection of the cylinder, burner, etc. can be facilitated. Therefore, it exhibits many effects such as low equipment cost and compactness, making it excellent in applicability as a cylinder for a warp sizing dryer or a cloth dyeing dryer. It also has the effect of improving the heat insulation of the cylinder bearing member.

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

第1図は本考案乾燥シリンダ群を備えた経糸糊
付乾燥機の縦断側面図、第2図は本考案乾燥シリ
ンダとその加熱装置の断面図、第3図は第2図の
A−A線断面図、第4図は部分斜視図、第5図は
第2図のB−B線断面図である。 BO……バーナ、a……加熱蒸気、W……水、
D……ドレン、10……乾燥シリンダ、10a
…軸支筒、11′,12′……軸受部材、13……
環状ボイラ筒、13b……連絡孔、13C……小
孔、14,14′……小径軸支筒、S,S′……空
間、f……火炎、20……断熱筒、23……加熱
蒸気管、26……供給管、160……くみ揚げ
管、25……接続箱、100……乾燥シリンダ均
等加熱装置。
Fig. 1 is a longitudinal side view of a warp sizing dryer equipped with a group of drying cylinders of the present invention, Fig. 2 is a sectional view of the drying cylinder of the present invention and its heating device, and Fig. 3 is a line taken along line A-A in Fig. 2. 4 is a partial perspective view, and FIG. 5 is a sectional view taken along the line B--B in FIG. 2. B O ...Burner, a...Heating steam, W...Water,
D...Drain, 10...Drying cylinder, 10a ...
...Shaft support tube, 11', 12'...Bearing member, 13...
Annular boiler cylinder, 13 b ...Communication hole, 13 C ...Small hole, 14, 14'...Small diameter shaft support tube, S, S'...Space, f...Flame, 20...Insulation tube, 23... ... Heating steam pipe, 26 ... Supply pipe, 160 ... Lifting pipe, 25 ... Connection box, 100 ... Drying cylinder uniform heating device.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 両端の軸支筒を、空気層を形成した断熱軸受部
材で回転自在に承持した乾燥シリンダ内に、二重
構造の環状ボイラ筒を一体気密に承持して上記乾
燥シリンダと環状ボイラ筒内及び外周を真空構造
となし、この環状ボイラ筒の内周側に火炎を送る
バーナを上記軸支筒の片側に設け、前記環状ボイ
ラ筒の内周側の排気側に配置した環状加熱蒸気管
はその両端を環状ボイラ筒の外周側に開口させ、
この加熱蒸気管内の加熱蒸気を乾燥シリンダ内へ
送る連絡孔を反バーナ側の端面に穿ち、乾燥シリ
ンダ内で復水したドレン(水)を環状ボイラ筒内
へ戻す反還部材のくみ揚げ管と接続箱、供給管を
バーナ側の乾燥シリンダ内端面及び環状ボイラ筒
の外周側に設けたことを特徴とする乾燥シリンダ
均等加熱装置。
A double-structured annular boiler cylinder is integrally and airtightly supported in a drying cylinder in which shaft support cylinders at both ends are rotatably supported by heat-insulating bearing members with an air layer formed inside the drying cylinder and the annular boiler cylinder. and an annular heating steam pipe whose outer periphery has a vacuum structure, a burner that sends a flame to the inner periphery of the annular boiler cylinder is provided on one side of the shaft support cylinder, and is arranged on the exhaust side of the inner periphery of the annular boiler cylinder. Both ends are opened on the outer circumferential side of the annular boiler cylinder,
A communication hole for sending the heated steam in the heating steam pipe into the drying cylinder is bored in the end face on the side opposite to the burner, and the drain pipe of the recirculation member returns the condensed water (water) in the drying cylinder to the annular boiler cylinder. A drying cylinder uniform heating device characterized in that a connection box and a supply pipe are provided on the inner end surface of the drying cylinder on the burner side and on the outer circumferential side of the annular boiler cylinder.
JP17017185U 1985-11-05 1985-11-05 Expired JPH0325113Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17017185U JPH0325113Y2 (en) 1985-11-05 1985-11-05

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17017185U JPH0325113Y2 (en) 1985-11-05 1985-11-05

Publications (2)

Publication Number Publication Date
JPS6184493U JPS6184493U (en) 1986-06-03
JPH0325113Y2 true JPH0325113Y2 (en) 1991-05-31

Family

ID=30727879

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17017185U Expired JPH0325113Y2 (en) 1985-11-05 1985-11-05

Country Status (1)

Country Link
JP (1) JPH0325113Y2 (en)

Also Published As

Publication number Publication date
JPS6184493U (en) 1986-06-03

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