JP4357497B2 - Heat transfer roller - Google Patents

Heat transfer roller Download PDF

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JP4357497B2
JP4357497B2 JP2006116737A JP2006116737A JP4357497B2 JP 4357497 B2 JP4357497 B2 JP 4357497B2 JP 2006116737 A JP2006116737 A JP 2006116737A JP 2006116737 A JP2006116737 A JP 2006116737A JP 4357497 B2 JP4357497 B2 JP 4357497B2
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heat
roller
heat medium
medium flow
temperature
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JP2006207825A (en
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良夫 北野
徹 外村
幸三 岡本
成之 弘田
正信 平郡
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Tokuden Co Ltd Kyoto
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Description

本発明は、流体を熱媒体として樹脂フィルムなどの処理物を加熱又は奪熱処理するローラに関する。   The present invention relates to a roller that heats or heat-treats a processed object such as a resin film using a fluid as a heat medium.

樹脂フィルムなどの処理物をローラに掛け、ローラに当接して通過する間に処理物を所定の温度に加熱したり、高温の処理物を所定の温度にまで奪熱することが行われている。加熱処理する場合、ローラは加熱処理に必要な温度に高められ、奪熱処理する場合、処理物からの奪熱作用によってローラ自体の温度が上昇するので、処理物の冷却に適応する温度までローラを冷却する。いずれの場合も熱を移送する媒体を必要とし、その媒体として流体たとえば油が使用されている。すなわち、適温の流体をローラの内部を通過させ、この流体でローラを加熱又はローラから奪熱する(以下、このようなローラを熱媒通流ローラという。)ようにしている。   A treatment object such as a resin film is placed on a roller, and the treatment object is heated to a predetermined temperature while passing through the roller, or the high temperature treatment object is deprived to a predetermined temperature. . When heat treatment is performed, the roller is heated to a temperature required for the heat treatment. When heat treatment is performed, the temperature of the roller itself increases due to heat removal from the processed material. Cooling. In either case, a medium for transferring heat is required, and a fluid such as oil is used as the medium. That is, a fluid having an appropriate temperature is allowed to pass through the inside of the roller, and the roller is heated or deprived from the roller by this fluid (hereinafter, such a roller is referred to as a heat medium flow roller).

図6はこのような熱媒通流ローラの一例の概略構成を示すもので、図6において、1はロールシェル、2は回転駆動軸、3は中子、4はロータリジョイント、5は貯油タンク、6は油(熱媒流体)、7は加熱又は冷却用熱交換器、8は温度センサ、9はポンプ、10は樹脂フィルムなどの処理物である。ロールシェル1は円筒状をなし、その中空内部に中子3が配置され、中子3の中央部を貫通して熱媒通流路3aが形成されている。熱媒通流路3aは回転駆動軸2内を経てロータリジョイント4の流入口に連結され、ロールシェル1の内周壁と中子3の外周壁との間で形成された熱媒通流路1aは回転駆動軸2内を経てロータリジョイント4の出口に連結されている。   FIG. 6 shows a schematic configuration of an example of such a heat medium flow roller. In FIG. 6, 1 is a roll shell, 2 is a rotary drive shaft, 3 is a core, 4 is a rotary joint, and 5 is an oil storage tank. , 6 is oil (heat medium fluid), 7 is a heat exchanger for heating or cooling, 8 is a temperature sensor, 9 is a pump, and 10 is a processed object such as a resin film. The roll shell 1 has a cylindrical shape, and a core 3 is disposed inside the hollow shell, and a heat medium passage 3 a is formed through the center of the core 3. The heat medium flow path 3 a is connected to the inlet of the rotary joint 4 through the rotary drive shaft 2, and is formed between the inner peripheral wall of the roll shell 1 and the outer peripheral wall of the core 3. Is connected to the outlet of the rotary joint 4 through the rotary drive shaft 2.

すなわち、貯油タンク5の油6は加熱又は冷却用熱交換器7を通り、所定の温度にされ、ポンプ9によってロールシェル1内に送られ、熱媒通流路3aおよび1aを通流した油6は貯油タンク5へ排出される。主として熱媒通流路1aを通流する間にロールシェル1は所定の温度に維持され、ロールシェル1の表面に当接した処理物10を加熱又は奪熱する。   That is, the oil 6 in the oil storage tank 5 passes through the heat exchanger 7 for heating or cooling, is brought to a predetermined temperature, is sent into the roll shell 1 by the pump 9, and flows through the heat medium passages 3a and 1a. 6 is discharged to the oil storage tank 5. The roll shell 1 is maintained at a predetermined temperature while mainly flowing through the heat medium passage 1a, and heats or removes the processed material 10 that is in contact with the surface of the roll shell 1.

ところで、このような熱媒通流ローラでは、ローラ(ロールシェルに回転駆動軸を連結したもの)内に流入する熱媒流体の温度と処理物の加熱後または奪熱後に流出する熱媒流体の温度との間に温度差が発生し、その温度差はローラの表面に現れるため、ローラの表面に当接した処理物のローラの軸心に沿う長手方向に対し、均一な熱処理ができないという問題がある。この問題を解消するために、従来はこの温度差を減らすために、温度差に応じてローラ内を通流する熱媒流体の流量を増加するようにしている。 そのために加熱又は冷却用熱交換器やポンプが大型化せざるを得ないという問題があった。   By the way, in such a heat-medium flow roller, the temperature of the heat-medium fluid that flows into the roller (the roll shell connected to the rotary drive shaft) and the temperature of the heat-medium fluid that flows out after heating or removing the processed material Since a temperature difference occurs between the temperature and the temperature difference appears on the surface of the roller, there is a problem in that a uniform heat treatment cannot be performed in the longitudinal direction along the axis of the roller of the processed material in contact with the roller surface. There is. In order to eliminate this problem, conventionally, in order to reduce this temperature difference, the flow rate of the heat transfer fluid flowing through the roller is increased in accordance with the temperature difference. Therefore, there has been a problem that the heat exchanger or pump for heating or cooling has to be enlarged.

本発明は、このような問題を解消すべくなされたもので処理物の均一な熱処理を可能にするとともに、熱交換器やポンプを小型化することのできる熱媒通流ローラを提供することを目的とする。   The present invention has been made to solve such a problem, and provides a heat-medium flow roller that enables uniform heat treatment of a processed material and can reduce the size of a heat exchanger and a pump. Objective.

本発明は、熱媒通流路を有し、前記熱媒通流路を流れる熱媒流体により表面に当接する処理物を加熱又は奪熱処理する熱媒通流ローラであって、前記ローラの肉厚内部に、該ローラの長手方向に伸びる気液2相の熱媒体を封入する密閉室をローラの外周面に沿って複数設けると共に、隣り合う前記密閉室間に熱媒通流路となる熱媒通流貫通孔を設け、また、前記ローラの中空内に電磁発熱機構を設けたことを特徴とする。 The present invention is a heat medium flow roller that has a heat medium flow channel and heats or heat-treats a processed material that comes into contact with the surface by a heat medium fluid flowing through the heat medium flow channel. A plurality of sealed chambers that enclose a gas-liquid two-phase heat medium extending in the longitudinal direction of the roller are provided along the outer circumferential surface of the roller, and heat that serves as a heat medium passage between the adjacent sealed chambers. A medium flow through hole is provided, and an electromagnetic heating mechanism is provided in the hollow of the roller .

本発明では、ローラの肉厚内部にローラの長手方向に伸びる気液2相の熱媒体を封入する密閉室を設け、その密閉室と並んでローラの肉厚内部に熱媒通流路を設けているので、ローラ内に流入する熱媒流体の温度と処理物の加熱後または奪熱後に流出する熱媒流体の温度との間に温度差が発生しても、気液2相の熱媒体の潜熱の移動により、ローラの軸心に沿う長手方向の表面温度が均一化し、また熱媒流体の伝熱も速く、これによって熱媒流体の流量を大幅に低減することができ、小さい配管およびポンプの採用によって設備費を削減することが可能となり、 配管の放熱量の低減とポンプ容量の低下によって、省エネルギーを達成することができる。   In the present invention, there is provided a sealed chamber for enclosing a gas-liquid two-phase heat medium extending in the longitudinal direction of the roller in the wall thickness of the roller, and a heat medium passage is provided in the wall thickness of the roller along with the sealed chamber. Therefore, even if a temperature difference occurs between the temperature of the heat transfer fluid flowing into the roller and the temperature of the heat transfer fluid flowing out after heating or removing the processed material, the gas-liquid two-phase heat transfer medium Due to the movement of the latent heat, the surface temperature in the longitudinal direction along the axial center of the roller is made uniform, and the heat transfer of the heat transfer fluid is also fast, which can greatly reduce the flow rate of the heat transfer fluid. The adoption of a pump makes it possible to reduce equipment costs, and energy saving can be achieved by reducing the heat radiation of the piping and the pump capacity.

処理物の均一な熱処理を可能にするとともに、熱交換器やポンプを小型化することのできる熱媒通流ローラを提供する目的を、中空ローラの肉厚内に気液2相の熱媒体を封入する密閉室と、その密閉室と並んでローラの肉厚内部に熱媒通流路を設けるとともに、中空ローラの内部に電磁発熱機構を設けることのより実現した。 The purpose of providing a heat-medium flow roller that enables uniform heat treatment of the processed material and that can reduce the size of the heat exchanger and pump is to provide a gas-liquid two-phase heat medium within the wall thickness of the hollow roller. a sealed chamber enclosing, the sealed chamber and alongside the roller thick inside provided heat medium flow path Rutotomoni was realized from Kotono providing electromagnetic heating system inside the hollow roller.

まず、本発明の基本構成について図を参照して説明する。図1は基本構成に係る熱媒通流ローラの縦断面図、図2は部分的に示す同横断面図、図3は動作説明図であり、(a)は加熱時、(b)は奪熱時を示す。なお、図6に示すロータリジョイント4、貯油タンク5、加熱又は冷却用熱交換器7、温度センサ8およびポンプ9からなる油(熱媒流体)の循環経路については図では省略している。 First, it will be described with reference to FIG. About the basic configuration of the present invention. FIG. 1 is a longitudinal sectional view of a heat medium flow roller according to a basic configuration , FIG. 2 is a partial sectional view of the same, FIG. 3 is an operation explanatory view, (a) is a heating time, (b) is a deprivation. Indicates hot time. Note that the circulation path of oil (heating medium fluid) including the rotary joint 4, the oil storage tank 5, the heat exchanger 7 for heating or cooling, the temperature sensor 8, and the pump 9 shown in FIG. 6 is omitted in the drawing.

図1ないし図3において、10は樹脂フィルムなどの処理物(図3参照)、 11はロールシェル、12は回転駆動軸、13は密閉室、14は熱媒通流管、15は気液2相を形成する熱媒体である。   In FIGS. 1 to 3, 10 is a processed material such as a resin film (see FIG. 3), 11 is a roll shell, 12 is a rotary drive shaft, 13 is a sealed chamber, 14 is a heat medium flow pipe, and 15 is a gas-liquid 2. It is a heat medium that forms a phase.

ロールシェル11は円筒状を成し、長手方向の両側の端部は回転駆動軸12のフランジ12aに連結固定されている。密閉室13はロールシェル11の肉厚内に、たとえばロールシェル11の長手方向の端縁からその長手方向にドリルで孔を形成し、その孔に気液2相の熱媒体となる適量の水15などを注入して開口部を閉塞することにより形成され、図2に示すように適宜間隔を隔ててローラの外周面に沿って複数個設けられている。   The roll shell 11 has a cylindrical shape, and both end portions in the longitudinal direction are connected and fixed to the flange 12 a of the rotary drive shaft 12. The sealed chamber 13 is formed with a hole in the wall thickness of the roll shell 11, for example, from the longitudinal edge of the roll shell 11 by a drill in the longitudinal direction, and an appropriate amount of water serving as a gas-liquid two-phase heat medium in the hole. 15 is injected to close the opening, and a plurality are provided along the outer peripheral surface of the roller at an appropriate interval as shown in FIG.

熱媒通流管14は密閉室13の内部を長手方向に沿って貫通し、ロールシェル11の長手方向の両側の端縁に伸びている。回転駆動軸12およびそのフランジ12aには熱媒通流孔が形成され熱媒通流管14はこの熱媒通流孔と連通している。すなわち、図示しない加熱又は冷却用熱交換器、ポンプおよびロータリジョイントを経て送り込まれたロールシェル11を加熱し、または奪熱するための油などの熱媒流体は、一方の回転駆動軸12およびそのフランジ12aの熱媒通流孔を経て熱媒通流管14を通り、他方のフランジ12aおよび回転駆動軸12の熱媒通流孔およびロータリジョイントを経て貯油タンクへ排出される。   The heat medium flow pipe 14 penetrates the inside of the sealed chamber 13 along the longitudinal direction, and extends to both edges of the roll shell 11 in the longitudinal direction. A heat medium flow hole is formed in the rotary drive shaft 12 and its flange 12a, and the heat medium flow pipe 14 communicates with the heat medium flow hole. That is, a heating medium fluid such as oil for heating or depriving the roll shell 11 fed through a heating or cooling heat exchanger, a pump and a rotary joint (not shown) It passes through the heat medium flow pipe 14 through the heat medium flow hole of the flange 12a, and is discharged to the oil storage tank through the heat transfer hole and the rotary joint of the other flange 12a and the rotary drive shaft 12.

樹脂フィルムなどの処理物10を加熱する場合、所定の温度に加熱した熱媒流体を用いるが、この熱媒流体が熱媒通流管14を通過すると、図3(a)に示すように密閉室13内の熱媒体15が加熱気化し、その熱はロールシェル11を介して処理物10を加熱する。熱を奪われた気体は液化し、再び熱媒流体により加熱され加熱気化し、その熱はロールシェル11を介して処理物10を加熱する。この動作が繰り返される。処理物10を加熱する際、加熱気化した熱は処理物10が当接している温度の低い側へと移動し、熱媒流体の流入側の温度が高く、流出側の温度が低いという温度差が発生しても、処理物10をローラの軸心に沿う長手方向に対して均一な加熱処理ができる。   When heating the processed object 10 such as a resin film, a heat medium fluid heated to a predetermined temperature is used. When the heat medium fluid passes through the heat medium flow pipe 14, it is sealed as shown in FIG. The heat medium 15 in the chamber 13 is heated and vaporized, and the heat heats the processing object 10 through the roll shell 11. The gas that has been deprived of heat is liquefied and heated again by the heat transfer fluid to be vaporized by heating, and the heat heats the processed material 10 via the roll shell 11. This operation is repeated. When heating the processed object 10, the heat vaporized heat moves to the lower temperature side where the processed object 10 abuts, and the temperature difference is such that the temperature on the inflow side of the heat transfer fluid is high and the temperature on the outflow side is low. Even if this occurs, the processed object 10 can be uniformly heat-treated in the longitudinal direction along the axis of the roller.

また、樹脂フィルムなどの高温の処理物10を所定の温度に奪熱する場合、より温度の低下を防ぐために所定の温度に加熱した熱媒流体を用いるが、この熱媒流体が熱媒通流管14を通過すると、図3(b)に示すように処理物10により加熱されたロールシェル11の熱は密閉室13内の気液2相の熱媒体に伝達され、熱媒通流管14を通過する熱媒流体により所定の温度に冷却される。この場合、熱媒流体の流入側の温度が低く、流出側の温度が高いという温度差が発生しても気体の熱は低い方に移動し、処理物10をローラの軸心に沿う長手方向に対して均一な奪熱処理ができる。   In addition, when the high-temperature processed object 10 such as a resin film is deprived of heat at a predetermined temperature, a heat transfer fluid heated to a predetermined temperature is used in order to prevent a decrease in temperature. When passing through the tube 14, the heat of the roll shell 11 heated by the processed material 10 is transmitted to the gas-liquid two-phase heat medium in the sealed chamber 13 as shown in FIG. 3B, and the heat medium flow tube 14. It is cooled to a predetermined temperature by the heat transfer fluid passing through. In this case, even if a temperature difference occurs such that the temperature on the inflow side of the heat transfer fluid is low and the temperature on the outflow side is high, the heat of the gas moves to the lower side, and the processed material 10 moves in the longitudinal direction along the axis of the roller. For uniform heat treatment.

なお、この基本構成では、熱媒流体の流路が直接にロールシェル11に接しないことからロールシェル11の熱膨張差による機械的精度の劣化を抑制することができ、また、必要な加熱部および奪熱部に有効的に作用させることができる。 In this basic configuration , since the flow path of the heat transfer fluid does not directly contact the roll shell 11, it is possible to suppress deterioration in mechanical accuracy due to the thermal expansion difference of the roll shell 11, and a necessary heating unit And can effectively act on the heat sink.

以上の基本構成は、熱媒通流管14を密閉室13の内部を長手方向に沿って貫通させて熱媒流体の流路を形成しているが、本発明に係る実施例では、熱媒流体の流路は、図4に示すように気液2相の熱媒体を収納する密閉室13の間に、密閉室13と平行してロールシェル11の肉厚内を貫通して熱媒通流孔16を形成している。このように構成した熱媒通流ローラでは、ロールシェル11の熱を、熱媒通流孔16を通過する熱媒流体により直接に加熱または奪熱するものである。なお、密閉室13内の気液2相の熱媒体の潜熱移動により図1および図2に示す熱媒通流ローラと同様に、処理物をローラの軸心に沿う長手方向に対して均一な加熱および奪熱処理ができる。 In the above basic configuration, the heat medium flow pipe 14 is made to penetrate the inside of the sealed chamber 13 along the longitudinal direction to form a flow path of the heat medium fluid. In the embodiment according to the present invention, the heat medium As shown in FIG. 4, the fluid flow path passes through the inside of the wall thickness of the roll shell 11 in parallel with the sealed chamber 13 between the sealed chamber 13 that stores the gas-liquid two-phase heat medium. to form a Nagareana 16. In thus constituted heat medium passing roller, the heat of the roll shell 11, Ru der those directly heated or ablative heat by heat transfer fluid passing through the Netsunakadachidori Nagareana 16. Similarly to the heating medium passing roller shown in FIGS. 1 and 2 by the latent heat movement of the gas-liquid two-phase heating medium in tight closed from 13, uniform with respect to the longitudinal direction along the treated product to the axis of the roller Heating and heat treatment can be performed.

以上のように構成した熱媒通流ローラについて、ロールの直径310mm、ロール面長1110mm、ファン負荷運転、流体流量2.4m/h、流体比重841kg/m 、流体比熱0.42kcal/kg、流体入り口温度178℃、流体出口温度168℃、流体出入口温度差10℃で、流体の出口側から入り口までほぼ等間隔に14点の温度センサをロールシェル11の表面に配置して、計測した。 About the heat medium flow roller configured as described above, the roll diameter is 310 mm, the roll surface length is 1110 mm, the fan load operation, the fluid flow rate is 2.4 m 3 / h, the fluid specific gravity is 841 kg / m 3 , and the fluid specific heat is 0.42 kcal / kg. The temperature was measured by arranging 14 temperature sensors on the surface of the roll shell 11 at almost equal intervals from the fluid outlet side to the inlet at a fluid inlet temperature of 178 ° C., a fluid outlet temperature of 168 ° C., and a fluid inlet / outlet temperature difference of 10 ° C. .

その結果、流体の出口側から順に、146.8 148.8 [150.6 150.8 150.9 150.9 150.9 150.8 150.6 150.7 150.5 150.3] 149.4 147.8であった。[]内の温度が気液2相の熱媒体を収納した密閉室の有効長かつ処理物幅の有効長960mmである。この範囲での温度差は0.6℃であり、流体出入口温度差10℃にかかわらず良好な温度分布を呈している。なお、[]外の温度は密閉室の有効外のロール有効長外部分であり、熱が回転駆動軸に奪われて温度が若干低下している。 As a result, 146.8 148.8 [150.6 150.8 150.9 150.9 150.9 150.8 150.6 150.7 150.5 150.3] 149. 4 147.8. The temperature in [] is the effective length of the sealed chamber containing the gas-liquid two-phase heat medium and the effective length of the treatment width 960 mm. The temperature difference in this range is 0.6 ° C., and a good temperature distribution is exhibited regardless of the fluid inlet / outlet temperature difference of 10 ° C. In addition, the temperature outside [] is a portion outside the effective roll length outside the effective chamber, and the temperature is slightly lowered due to heat being taken away by the rotary drive shaft.

ロールが放出する熱量を求めると、Q(kcal/h)=10×2.4×841×0.42=8477kcal/h=9.86Kwである。ここで、気液2相の熱媒体を収納した密閉室を設けずに、この温度差0.6℃を得るときの流量Vを求めると、V(m/h)=8477/(0.6×841×0.42)=40(m/h)となる。これは気液2相の熱媒体を収納した密閉室を設けた場合に比べ約16.7倍の流体流量が必要であることを意味する。 The amount of heat released by the roll is calculated as Q (kcal / h) = 10 × 2.4 × 841 × 0.42 = 8477 kcal / h = 9.86 Kw. Here, when the flow rate V when obtaining this temperature difference of 0.6 ° C. is obtained without providing a sealed chamber containing the gas-liquid two-phase heat medium, V (m 3 / h) = 8477 / (0. 6 × 841 × 0.42) = 40 (m 3 / h). This means that a fluid flow rate of about 16.7 times as much as that required when a sealed chamber containing a gas-liquid two-phase heat medium is provided.

したがって、気液2相の熱媒体を収納した密閉室を設けた場合には1/16.7倍の流体流量で済み、この場合、配管およびロータリージョイントの断面積を1/16.7とすることが可能であり、配管およびロータリージョイントに要するコストを低減することができる。また、流体流量の低減は、配管工数および設置スペースの低減につながり、コスト低減として大きなメリットがあり、さらに流路の断面積が1/16.7となることは配管表面積が約1/4となり、配管放熱が1/4になって省エネルギーとすることができる。流体の流量が少なくすめば流体を供給するポンプも小さくてよく、流量が1/16.7であればポンプの容量は通常1/10程度で十分である。   Therefore, when a sealed chamber containing a gas-liquid two-phase heat medium is provided, the fluid flow rate is 1 / 16.7 times higher, and in this case, the cross-sectional area of the piping and the rotary joint is 1 / 16.7. It is possible to reduce the cost required for the piping and the rotary joint. In addition, the reduction of the fluid flow rate leads to a reduction in piping man-hours and installation space, and there is a great merit as a cost reduction. Furthermore, the fact that the cross-sectional area of the flow path becomes 1 / 16.7 means that the piping surface area is about 1/4. The heat radiation of the pipe can be reduced to ¼ to save energy. If the flow rate of the fluid is small, the pump supplying the fluid may be small. If the flow rate is 1 / 16.7, the capacity of the pump is usually about 1/10.

なお、以上は流体出入口温度差10℃とした場合であるが、流体出入口温度差10℃とした理由は、処理物を均一に熱処理しようとするとロールの有効長における温度分布精度が通常5℃未満である必要がある。つまり流体出入口温度差5℃未満とする必要があり、流体出入口温度差5℃以上となる場合には、流体出入口温度差にしたがい流量を増加しなければ均一に熱処理することができない。
しかし、気液2相の熱媒体を収納した密閉室を設けることにより、流体出入口温度差5℃以上であっても流量を増加することなく十分に均一な熱処理が果たせることを示すためである。すなわち、流体出入口温度差10℃でロールの有効長における温度分布精度が0.6℃であることは、ロールの有効長における温度分布精度が5℃未満までとすれば、流体出入口温度差は、5/0.6×10=83.3℃と大幅な温度差とすることができ、配管、ロータリージョイントおよびポンプなどを小型化することができる顕著な効果が得られる。
The above is the case where the fluid inlet / outlet temperature difference is 10 ° C. The reason why the fluid inlet / outlet temperature difference is 10 ° C. is that the temperature distribution accuracy in the effective length of the roll is usually less than 5 ° C. Need to be. That is, the fluid inlet / outlet temperature difference needs to be less than 5 ° C., and when the fluid inlet / outlet temperature difference is 5 ° C. or more, the heat treatment cannot be uniformly performed unless the flow rate is increased according to the fluid inlet / outlet temperature difference.
However, by providing a sealed chamber containing a gas-liquid two-phase heat medium, it is possible to perform sufficiently uniform heat treatment without increasing the flow rate even if the fluid inlet / outlet temperature difference is 5 ° C. or more. That is, the temperature distribution accuracy in the effective length of the roll at a fluid inlet / outlet temperature difference of 10 ° C is 0.6 ° C. If the temperature distribution accuracy in the effective length of the roll is less than 5 ° C, the fluid inlet / outlet temperature difference is A significant temperature difference of 5 / 0.6 × 10 = 83.3 ° C. can be obtained, and a remarkable effect can be obtained in which piping, rotary joints, pumps, and the like can be reduced in size.

ところで、奪熱によってローラ(厳密にはロールシェル)の表面温度が変動する際、それを熱媒流体の温度を制御することでローラの表面温度を一定に制御するが、熱媒流体の温度制御は比較的に安定的にできるのに比べ、流路壁面との熱伝達率が小さいためにローラの温度は追従せず時間遅れが発生する。この遅れを解消するために、ローラ自体をジュール発熱させる誘導発熱機構を付加している。 By the way, when the surface temperature of the roller (strictly speaking, roll shell) fluctuates due to heat removal, the surface temperature of the roller is controlled to be constant by controlling the temperature of the heat transfer fluid. Since the heat transfer coefficient with the flow path wall surface is small compared to the case where the roller temperature is relatively stable, the roller temperature does not follow and a time delay occurs. In order to eliminate this delay, an induction heating mechanism for adding Joule heat to the roller itself is added .

図5は熱媒通流ローラの中空部に誘導コイルと鉄心とからなる誘導発熱機構18を配置した熱媒通流ローラを示すもので、このように誘導発熱機構を設けると、処理物の処理温度を変更した場合に迅速に対応することができる。なお、図5では図1に示す熱媒通流ローラに設けているが、図4に示す熱媒通流ローラの中空内部に配置することもできる。   FIG. 5 shows a heat medium flow roller in which an induction heat generating mechanism 18 composed of an induction coil and an iron core is arranged in the hollow portion of the heat medium flow roller. When the temperature is changed, it is possible to respond quickly. In FIG. 5, the heat medium flow roller shown in FIG. 1 is provided. However, the heat medium flow roller shown in FIG.

以上の実施例では、密閉室に気液2相の熱媒体となる適量の水15などを注入しているが、密閉室にヒートパイプを挿入するようにしてもよい。また、複数の密閉室はそれぞれ独立しているが、たとえば密閉室の両側の端部で互いに連通するようにしてもよい。その連通路を回転駆動軸のフランジ内に設けるようにしてもよい。   In the above embodiment, an appropriate amount of water 15 or the like serving as a gas-liquid two-phase heat medium is injected into the sealed chamber, but a heat pipe may be inserted into the sealed chamber. Further, the plurality of sealed chambers are independent from each other, but may be communicated with each other at, for example, end portions on both sides of the sealed chamber. The communication path may be provided in the flange of the rotary drive shaft.

本発明の基本構成に係る熱媒通流ローラを示す縦断面図である。It is a longitudinal cross-sectional view which shows the heat-medium flowing roller which concerns on the basic composition of this invention. 図1に示す熱媒通流ローラの一部の横断面図である。It is a cross-sectional view of a part of the heat medium flow roller shown in FIG. 図1に示す熱媒通流ローラの動作説明図である。It is operation | movement explanatory drawing of the heat-medium flow roller shown in FIG. 本発明の実施例に係る熱媒通流ローラの一部の横断面図である。It is a cross-sectional view of a part of the heat medium flow roller according to the embodiment of the present invention. 本発明の実施例に係る熱媒通流ローラの縦断面図である。It is a longitudinal cross-sectional view of the heat-medium flow roller which concerns on the Example of this invention. 従来の熱媒通流ローラを示す縦断面図である。It is a longitudinal cross-sectional view which shows the conventional heat-medium flow roller.

符号の説明Explanation of symbols

4 ロータリジョイント
5 貯油タンク
7 加熱又は冷却用熱交換器
8 温度センサ
9 ポンプ
10 処理物
11 ロールシェル
12 回転駆動軸
13 密閉室
14 熱媒通流管
15 気液2相を形成する熱媒体
16 熱媒通流孔
18 誘導発熱機構
DESCRIPTION OF SYMBOLS 4 Rotary joint 5 Oil storage tank 7 Heat exchanger for heating or cooling 8 Temperature sensor 9 Pump 10 Processed object 11 Roll shell 12 Rotation drive shaft 13 Sealed chamber 14 Heat medium flow pipe 15 Heat medium which forms two phases of gas and liquid 16 Heat Medium flow hole
18 Induction heating mechanism

Claims (1)

熱媒通流路を有し、前記熱媒通流路を流れる熱媒流体により表面に当接する処理物を加熱又は奪熱処理する熱媒通流ローラであって、前記ローラの肉厚内部に、該ローラの長手方向に伸びる気液2相の熱媒体を封入する密閉室をローラの外周面に沿って複数設けると共に、隣り合う前記密閉室間に熱媒通流路となる熱媒通流貫通孔を設け、また、前記ローラの中空内に電磁発熱機構を設けたことを特徴とする熱媒通流ローラ。 A heat medium flow roller that has a heat medium flow channel and heats or heat-treats the processed material that comes into contact with the surface by the heat medium fluid flowing through the heat medium flow channel, and inside the wall thickness of the roller, A plurality of sealed chambers for enclosing a gas-liquid two-phase heat medium extending in the longitudinal direction of the roller are provided along the outer peripheral surface of the roller, and a heat medium flow through that serves as a heat medium flow path between the adjacent sealed chambers is provided. A heat medium flow roller characterized in that a hole is provided and an electromagnetic heating mechanism is provided in the hollow of the roller.
JP2006116737A 2006-04-20 2006-04-20 Heat transfer roller Expired - Fee Related JP4357497B2 (en)

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JP5501063B2 (en) * 2010-03-29 2014-05-21 リンテック株式会社 Press roller and pressing method
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