JP2003053740A - Steam vulcanization apparatus - Google Patents
Steam vulcanization apparatusInfo
- Publication number
- JP2003053740A JP2003053740A JP2001243217A JP2001243217A JP2003053740A JP 2003053740 A JP2003053740 A JP 2003053740A JP 2001243217 A JP2001243217 A JP 2001243217A JP 2001243217 A JP2001243217 A JP 2001243217A JP 2003053740 A JP2003053740 A JP 2003053740A
- Authority
- JP
- Japan
- Prior art keywords
- steam
- vulcanization
- supply pipe
- vulcanizing
- container
- 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
Links
Landscapes
- Heating, Cooling, Or Curing Plastics Or The Like In General (AREA)
Abstract
Description
【発明の詳細な説明】
【0001】
【発明の属する技術分野】本発明は未加硫物を蒸気で加
硫するものに関し、特に未加硫物の全体が均一な所定温
度で加熱され、その結果、未加硫物の全体を均一に加硫
することのできる蒸気加硫装置に関する。
【0002】
【従来の技術】従来の蒸気加硫装置として、例えばゴム
ロールを加硫するものが特開昭50−3483号公報に
示されている。これは、ゴム原料を圧延してシート状に
し、心材のまわりに積層した後、心材の内部にパイプ
5,12から熱蒸気を供給して加硫するものである。
【0003】
【発明が解決しようとする課題】上記従来のものでは、
心材の空胴内にただ単にパイプを通して熱蒸気を供給す
るものであるために、心材の空胴の全体に且つ均一に熱
蒸気が行き渡らず、未加硫物の全体を均一に加硫できな
い問題があった。特に、空胴部の容積が大きな場合や形
状が複雑な場合は、熱蒸気が全体に且つ均一に行き渡ら
ないことが多い。
【0004】従って本発明の課題は、容器の大きさや形
状がどのようなものであっても、容器の全体に且つ均一
に蒸気を供給できるようにして、未加硫物の全体を均一
に加硫することのできる蒸気加硫装置を得ることであ
る。
【0005】
【課題を解決するための手段】上記の課題を解決するた
めに講じた手段は、ゴムの未加硫物を密閉状容器内に配
置し、当該容器内に蒸気供給管から蒸気を供給して未加
硫物を加硫するものにおいて、蒸気供給管の容器側端部
に複数のスプレーノズルを取り付けて、当該複数のスプ
レーノズルの入口側に開閉弁を設けたものである。
【0006】
【発明の実施の形態】蒸気供給管の容器側端部に開閉弁
を介して複数のスプレーノズルを取り付けたことによ
り、開閉弁を任意に開閉制御して、複数のスプレーノズ
ルから順次に容器内へ蒸気を供給することにより、容器
内の流体の対流を任意にコントロールすることができ
る。
【0007】蒸気を含む流体が対流することによって、
容器内の全体に且つ均一に蒸気が行き渡り、未加硫物の
全体を均一に加硫することができる。
【0008】
【実施例】本実施例においては、蒸気と共に空気を供給
して加硫する例を説明する。図1において、密閉状容器
としての加硫缶1と蒸気供給管2と圧縮空気供給管3、
及び、複数のスプレーノズル22,23,24,25,
26とで蒸気加硫装置を構成する。
【0009】加硫缶1は、横長円筒状で内部に未加硫物
としての図示しないゴムロール等を戴置する棚4を取り
付ける。加硫缶1の側部には一部球形状の蓋5を開閉自
在に取り付ける。加硫開始時に蓋5を開いて棚4の上に
ゴムロールを戴置するものである。
【0010】加硫缶1の上部には蒸気供給管2と圧縮空
気供給管3を接続する。蒸気供給管2は、バルブ6と調
節弁7と開閉弁32,33,34を介して加硫缶1の上
部のスプレーノズル22,23,24と接続する。蒸気
供給管2は分岐管21によって分岐して、開閉弁35,
36を介して下部のスプレーノズル25,26とも接続
する。圧縮空気供給管3は、バルブ9と調節弁10を介
して加硫缶1と接続する。
【0011】本実施例においては、スプレーノズル22
〜26を加硫缶1の上下に合計5個取り付けた例を示し
たが、加硫缶1の大きさや形状によっては2個だけで済
む場合もあり、また、加硫缶1の上下のみならず左右に
も取り付けることができる。
【0012】開閉弁32〜36は、電磁弁や電動弁とし
て、図示しない開閉制御部から任意に且つ自動的に開閉
できるようにする。
【0013】加硫缶1の上部には、内部の圧力を検出す
る圧力センサ12と、温度を検出する温度センサ13を
取り付ける。圧力センサ12は開閉制御部を介して調節
弁7,10及び開閉弁32〜36と電気的に接続する。
それぞれの弁7,10,32〜36は全閉したり、ある
いは、弁開度を大きくしたり、小さくすることによっ
て、蒸気や圧縮空気の通過量を調節してそれぞれの分圧
を任意に制御することができるものである。
【0014】温度センサ13は同じく開閉制御部を介し
て調節弁7及び開閉弁32〜36と電気的に接続する。
飽和蒸気の圧力と温度は一義的に定まるために、蒸気の
圧力を所定値に制御すれば温度も所定値に維持できる。
従って、本実施例においては、温度センサ13は補助的
に使用するものである必ずしも必要ではない。
【0015】加硫缶1の右側部にはバルブ14を介して
大気連通管15を接続する。また、加硫缶1の下部に
は、蒸気が凝縮した復水を外部に排除するための復水排
除管16を接続する。復水排除管16にはバルブ17
と、復水だけを出口側に排出するスチームトラップ18
を並列に取り付ける。
【0016】棚4上に戴置した図示しないゴムロール等
を加硫する場合、まず、圧縮空気供給管3から調節弁1
0を介して加硫缶1の内部に所定圧力、例えば3.2K
Gの圧縮空気を供給する。加硫缶1内部の圧縮空気圧力
が3.2KGに到達すると、続いて蒸気供給管2とスプ
レーノズル22〜26を介して所定圧力、例えば5.0
KGの蒸気を供給することによって、加硫缶1の内部に
は圧縮空気との圧力差に基づく1.8KGの蒸気が注入
される。
【0017】3.2KGの圧縮空気と1.8KGの蒸気
を供給することによって、加硫缶1内の圧力は5.0K
Gとなる。5.0KGとなった時点でバルブ9を閉弁し
て圧縮空気の供給は停止する。一方、蒸気の供給は、加
硫缶1内の圧力が5.0KGを維持するように継続して
行うことによって、1.8KGの飽和蒸気の温度は13
0度Cであるために、加硫缶1内の未加硫物のゴムロー
ルは5.0KG、130度Cの圧力、温度条件で加硫さ
れる。
【0018】蒸気供給管2から加硫缶1内へ蒸気を供給
する場合、開閉弁32〜36を任意のタイミングで開閉
することによって、加硫缶1内への蒸気の流れを任意に
コントロールすることができる。
【0019】例えば、開閉弁32を1分間開弁した後閉
弁すると同時に、開閉弁33を開弁して1分間維持して
閉弁して順次開閉弁34〜36を開閉弁することによっ
て、加硫缶1内の蒸気の流れをコントロールすることが
できる。
【0020】また、例えば、開閉弁32,33,34を
1分間開弁して閉弁し、続いて開閉弁35,36を1分
間開弁して閉弁することによって、加硫缶1内の蒸気の
流れをコントロールすることができる。そして、蒸気の
流れを任意にコントロールすることにより、加硫缶1内
の全体に蒸気が行き渡る。
【0021】本実施例のように、蒸気と圧縮空気を加硫
缶1内に供給して加硫を行う場合は、しばらく時間が経
つと、蒸気と圧縮空気が分離して加硫缶1内の温度のバ
ラツキが大きくなるが、開閉弁32〜36の開閉のタイ
ミングを制御して、スプレーノズル22〜26から供給
される蒸気で対流を促進して蒸気と圧縮空気を攪拌、混
合することによって、加硫缶1内の温度分布のバラツキ
をより小さなものとすることができる。
【0022】
【発明の効果】上記のように本発明によれば、開閉弁を
任意に開閉制御して複数のスプレーノズルから順次に容
器内へ蒸気を供給することにより、容器内の蒸気、及
び、容器内に存在する蒸気以外の流体も任意に対流させ
ることによって、容器の大きさや形状がどのようなもの
であっても全体に且つ均一に蒸気を供給でき、未加硫物
の全体を均一に加硫することができる。Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for vulcanizing an unvulcanized product with steam, and more particularly, to heating an unvulcanized product as a whole at a uniform predetermined temperature. As a result, the present invention relates to a steam vulcanizing apparatus capable of uniformly vulcanizing the entire unvulcanized product. 2. Description of the Related Art As a conventional steam vulcanizing apparatus, for example, an apparatus for vulcanizing a rubber roll is disclosed in Japanese Patent Application Laid-Open No. 50-3483. In this method, a rubber material is rolled into a sheet, laminated around a core material, and then vulcanized by supplying hot steam from the pipes 5 and 12 into the core material. [0003] In the above conventional device,
Since heat steam is simply supplied through a pipe into the core material cavity, the heat steam does not spread evenly and uniformly throughout the core material cavity, and the entire unvulcanized product cannot be uniformly vulcanized. was there. In particular, when the volume of the cavity portion is large or the shape is complicated, the heat steam often does not spread all over and uniformly. Accordingly, an object of the present invention is to provide a method for uniformly supplying steam to the entire container, regardless of the size and shape of the container, so that the entire unvulcanized product is uniformly vulcanized. The purpose is to obtain a steam vulcanizing device that can be vulcanized. [0005] Means taken to solve the above problem is to arrange an unvulcanized rubber material in a closed container, and to supply steam from a steam supply pipe into the container. In the vulcanizing method for supplying and vulcanizing an unvulcanized product, a plurality of spray nozzles are attached to a container side end of a steam supply pipe, and an opening / closing valve is provided on an inlet side of the plurality of spray nozzles. A plurality of spray nozzles are attached to an end of a steam supply pipe on a container side via an on-off valve, so that the on-off valve is arbitrarily opened and closed, and the plurality of spray nozzles are sequentially started from the plurality of spray nozzles. By supplying steam into the container, the convection of the fluid in the container can be arbitrarily controlled. [0007] By the convection of a fluid containing steam,
The steam spreads uniformly throughout the container, and the entire unvulcanized product can be uniformly vulcanized. In this embodiment, an example in which air is supplied together with steam to perform vulcanization will be described. In FIG. 1, a vulcanizing can 1 as a closed container, a steam supply pipe 2, a compressed air supply pipe 3,
And a plurality of spray nozzles 22, 23, 24, 25,
26 together form a steam vulcanizing apparatus. The vulcanizing can 1 has a horizontally long cylindrical shape and has a shelf 4 on which a rubber roll (not shown) as an unvulcanized material is placed. A partially spherical lid 5 is attached to the side of the vulcanizing can 1 so as to be freely opened and closed. At the start of vulcanization, the lid 5 is opened and a rubber roll is placed on the shelf 4. A steam supply pipe 2 and a compressed air supply pipe 3 are connected to the upper part of the vulcanizer 1. The steam supply pipe 2 is connected to the spray nozzles 22, 23, 24 on the upper part of the vulcanizing can 1 via the valve 6, the control valve 7, and the on-off valves 32, 33, 34. The steam supply pipe 2 is branched by a branch pipe 21, and the on-off valve 35,
It is also connected to lower spray nozzles 25 and 26 via. The compressed air supply pipe 3 is connected to the vulcanization can 1 via a valve 9 and a control valve 10. In this embodiment, the spray nozzle 22
Although the example which attached a total of five to 26 above and below the vulcanized can 1 was shown, depending on the size and shape of the vulcanized can 1, only two pieces may be sufficient. It can also be attached to the left and right. The on-off valves 32 to 36 can be arbitrarily and automatically opened and closed by an on-off control unit (not shown) as electromagnetic valves or electric valves. A pressure sensor 12 for detecting the internal pressure and a temperature sensor 13 for detecting the temperature are mounted on the upper part of the vulcanizing can 1. The pressure sensor 12 is electrically connected to the control valves 7, 10 and the on-off valves 32-36 via the on-off control unit.
Each of the valves 7, 10, 32 to 36 is fully closed, or the valve opening is increased or decreased to adjust the amount of passage of steam or compressed air to arbitrarily control the respective partial pressures. Is what you can do. The temperature sensor 13 is also electrically connected to the control valve 7 and the on-off valves 32 to 36 via the on-off control unit.
Since the pressure and temperature of the saturated steam are uniquely determined, the temperature can be maintained at a predetermined value by controlling the steam pressure to a predetermined value.
Therefore, in this embodiment, the temperature sensor 13 is not necessarily required to be used as an auxiliary. An atmosphere communicating pipe 15 is connected to the right side of the vulcanizing can 1 via a valve 14. Further, a condensate rejection pipe 16 for rejecting condensate in which steam is condensed to the outside is connected to a lower portion of the vulcanizing can 1. The condensate drain pipe 16 has a valve 17
And a steam trap 18 that discharges only condensate water to the outlet side
Are attached in parallel. When vulcanizing a rubber roll or the like (not shown) placed on the shelf 4, first, the control valve 1 is passed through the compressed air supply pipe 3.
0, a predetermined pressure, for example, 3.2 K
G compressed air is supplied. When the compressed air pressure inside the vulcanizing can 1 reaches 3.2 KG, the predetermined pressure, for example, 5.0, is passed through the steam supply pipe 2 and the spray nozzles 22 to 26.
By supplying KG steam, 1.8 KG steam based on the pressure difference with the compressed air is injected into the inside of the vulcanizing can 1. By supplying 3.2 KG of compressed air and 1.8 KG of steam, the pressure in the vulcanization can 1 becomes 5.0K.
G. When it reaches 5.0 KG, the valve 9 is closed and the supply of compressed air is stopped. On the other hand, the steam is continuously supplied so that the pressure in the vulcanizing can 1 maintains 5.0 KG, so that the temperature of the saturated steam of 1.8 KG becomes 13
Since the temperature is 0 ° C., the unvulcanized rubber roll in the vulcanizing can 1 is vulcanized under the conditions of 5.0 kg, a pressure of 130 ° C. and a temperature. When steam is supplied from the steam supply pipe 2 into the vulcanizing can 1, the flow of the steam into the vulcanizing can 1 is arbitrarily controlled by opening and closing the on-off valves 32 to 36 at an arbitrary timing. be able to. For example, by opening and closing the on-off valve 32 for 1 minute and then closing it, simultaneously opening the on-off valve 33, maintaining it for 1 minute and closing it, and sequentially opening and closing the on-off valves 34 to 36, The flow of steam in the vulcanizing can 1 can be controlled. For example, by opening and closing the on-off valves 32, 33, 34 for one minute and then closing and opening the on-off valves 35, 36 for one minute, Control of the steam flow. By controlling the flow of the steam arbitrarily, the steam is distributed throughout the inside of the vulcanizing can 1. When vulcanization is performed by supplying steam and compressed air into the vulcanizing can 1 as in the present embodiment, after a while, the steam and compressed air are separated into the vulcanizing can 1. However, by controlling the timing of opening and closing the on-off valves 32 to 36, the convection is promoted by the steam supplied from the spray nozzles 22 to 26, and the steam and the compressed air are stirred and mixed. In addition, variation in the temperature distribution in the vulcanizing can 1 can be reduced. According to the present invention, as described above, the on-off valve is controlled to open and close arbitrarily to supply steam from a plurality of spray nozzles to the inside of the container in sequence. By arbitrarily convection of fluids other than steam present in the container, steam can be supplied to the whole and uniformly regardless of the size and shape of the container, and the entire unvulcanized product can be uniformly dispersed. Can be vulcanized.
【図面の簡単な説明】 【図1】本発明の蒸気加硫装置の実施例を示す構成図。 【符号の説明】 1 加硫缶 2 蒸気供給管 3 圧縮空気供給管 7 調節弁 10 調節弁 16 復水排除管 22,23,24,25,26 スプレーノズル 32,33,34,35,36 開閉弁 [Brief description of the drawings] FIG. 1 is a configuration diagram showing an embodiment of a steam vulcanizing apparatus of the present invention. [Explanation of symbols] 1 vulcanizing can 2 Steam supply pipe 3 Compressed air supply pipe 7 Control valve 10 Control valve 16 Condensate drain pipe 22,23,24,25,26 Spray nozzle 32, 33, 34, 35, 36 on-off valve
Claims (1)
し、当該容器内に蒸気供給管から蒸気を供給して未加硫
物を加硫するものにおいて、蒸気供給管の容器側端部に
複数のスプレーノズルを取り付けて、当該複数のスプレ
ーノズルの入口側に開閉弁を設けたことを特徴とする蒸
気加硫装置。Claims: 1. An unvulcanized rubber material is placed in a closed container, and steam is supplied from a steam supply pipe into the container to vulcanize the unvulcanized material. A steam vulcanizing apparatus comprising: a plurality of spray nozzles attached to an end of a steam supply pipe on a container side; and an on-off valve provided on an inlet side of the plurality of spray nozzles.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001243217A JP4672207B2 (en) | 2001-08-10 | 2001-08-10 | Steam vulcanizer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001243217A JP4672207B2 (en) | 2001-08-10 | 2001-08-10 | Steam vulcanizer |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2003053740A true JP2003053740A (en) | 2003-02-26 |
JP4672207B2 JP4672207B2 (en) | 2011-04-20 |
Family
ID=19073351
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2001243217A Expired - Fee Related JP4672207B2 (en) | 2001-08-10 | 2001-08-10 | Steam vulcanizer |
Country Status (1)
Country | Link |
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JP (1) | JP4672207B2 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006138585A (en) * | 2004-11-15 | 2006-06-01 | Tlv Co Ltd | Heat exchanging device |
JP2006136850A (en) * | 2004-11-15 | 2006-06-01 | Tlv Co Ltd | Heat exchanger |
KR101029635B1 (en) | 2009-07-10 | 2011-04-15 | 엘에스전선 주식회사 | Cable crosslinking apparatus and crosslinking method of the cable using the same |
JP2012153133A (en) * | 2010-11-26 | 2012-08-16 | Ashida Mfg Co Ltd | Autoclave molding method and autoclave molding apparatus |
JP2018069609A (en) * | 2016-10-31 | 2018-05-10 | 横浜ゴム株式会社 | Tire vulcanizing system and method for vulcanizing |
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JPS63111017A (en) * | 1986-10-28 | 1988-05-16 | Bridgestone Corp | Control method for type vulcanization |
JPH0452107A (en) * | 1990-06-20 | 1992-02-20 | Tokai Rubber Ind Ltd | Method and equipment for vulcanizing rubber hose |
JPH10165153A (en) * | 1996-12-10 | 1998-06-23 | Kisaburo Yukimura | Steam type stertlizer |
JPH10328026A (en) * | 1997-06-03 | 1998-12-15 | Ishikawa Shokuhin Kk | Retort pot |
JP2003025341A (en) * | 2001-07-13 | 2003-01-29 | Tlv Co Ltd | Steam vulcanization apparatus |
JP2003053737A (en) * | 2001-08-10 | 2003-02-26 | Tlv Co Ltd | Steam vulcanization apparatus |
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2001
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JPS49125874U (en) * | 1973-02-26 | 1974-10-28 | ||
JPS6343935A (en) * | 1986-08-12 | 1988-02-25 | Kanegafuchi Chem Ind Co Ltd | Production of pre-expanded particle of thermo-plastic resin |
JPS63111017A (en) * | 1986-10-28 | 1988-05-16 | Bridgestone Corp | Control method for type vulcanization |
JPH0452107A (en) * | 1990-06-20 | 1992-02-20 | Tokai Rubber Ind Ltd | Method and equipment for vulcanizing rubber hose |
JPH10165153A (en) * | 1996-12-10 | 1998-06-23 | Kisaburo Yukimura | Steam type stertlizer |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006138585A (en) * | 2004-11-15 | 2006-06-01 | Tlv Co Ltd | Heat exchanging device |
JP2006136850A (en) * | 2004-11-15 | 2006-06-01 | Tlv Co Ltd | Heat exchanger |
JP4545561B2 (en) * | 2004-11-15 | 2010-09-15 | 株式会社テイエルブイ | Heat exchanger |
KR101029635B1 (en) | 2009-07-10 | 2011-04-15 | 엘에스전선 주식회사 | Cable crosslinking apparatus and crosslinking method of the cable using the same |
JP2012153133A (en) * | 2010-11-26 | 2012-08-16 | Ashida Mfg Co Ltd | Autoclave molding method and autoclave molding apparatus |
EP2457708B1 (en) * | 2010-11-26 | 2014-07-02 | Kabushiki Kaisha Ashida Seisakusho | Autoclave molding method |
JP2018069609A (en) * | 2016-10-31 | 2018-05-10 | 横浜ゴム株式会社 | Tire vulcanizing system and method for vulcanizing |
Also Published As
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---|---|
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