JP5973199B2 - Steam heating device - Google Patents
Steam heating device Download PDFInfo
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- JP5973199B2 JP5973199B2 JP2012072738A JP2012072738A JP5973199B2 JP 5973199 B2 JP5973199 B2 JP 5973199B2 JP 2012072738 A JP2012072738 A JP 2012072738A JP 2012072738 A JP2012072738 A JP 2012072738A JP 5973199 B2 JP5973199 B2 JP 5973199B2
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- 238000010438 heat treatment Methods 0.000 title claims description 23
- 239000007788 liquid Substances 0.000 description 26
- 238000005086 pumping Methods 0.000 description 10
- 239000012530 fluid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 108010085603 SFLLRNPND Proteins 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- Jet Pumps And Other Pumps (AREA)
- Machines For Manufacturing Corrugated Board In Mechanical Paper-Making Processes (AREA)
Description
本発明は、段ボールなどを製造する場合に使用するコルゲートマシンの薄型熱盤として使用される蒸気加熱装置に関する。 The present invention relates to a steam heating apparatus used as a thin hot platen of a corrugating machine used when manufacturing corrugated cardboard or the like.
従来の蒸気加熱装置としては、熱交換器の二次側すなわち出口側に切替手段を介在して、エゼクタ式真空ポンプとスチームトラップを設けたもので、複数のバルブで構成する切替手段によって、真空ポンプとスチームトラップとを切り換えて使用するものである。 As a conventional steam heating apparatus, a switching means is interposed on the secondary side of the heat exchanger, that is, an outlet side, and an ejector type vacuum pump and a steam trap are provided. The pump and the steam trap are switched and used.
上記従来の蒸気加熱装置では、正圧蒸気の場合に復水の自圧回収手段へと切り換えるものであるが、蒸気の圧力が大気圧に近いような低圧の場合には、効率良く蒸気加熱装置を加熱することができない問題があった。これは、蒸気加熱装置の内部で加熱用の蒸気の流れが十分に発生しないために、加熱効率が上昇しないのである。 In the above conventional steam heating device, in the case of positive pressure steam, it switches to the condensate self-pressure recovery means, but in the case of a low pressure such that the steam pressure is close to atmospheric pressure, the steam heating device is efficient. There was a problem that could not be heated. This is because the heating efficiency does not increase because the flow of the heating steam is not sufficiently generated inside the steam heating apparatus.
従って本発明が解決しようとする課題は、蒸気加熱装置の内部で十分な蒸気の流れを発生させて、効率良く加熱することのできる蒸気加熱装置を得ることである。 Therefore, the problem to be solved by the present invention is to obtain a steam heating apparatus that can efficiently heat by generating a sufficient flow of steam inside the steam heating apparatus.
本発明は、複数の熱交換器の入口側へそれぞれ圧力調整弁を介して加熱用の蒸気供給管を接続したものにおいて、高圧蒸気による熱交換器の出口側を、低圧蒸気による熱交換器の入口側へ接続すると共に、低圧蒸気による熱交換器の入口側に蒸気エゼクタを配置して、当該蒸気エゼクタの吸込室を、低圧蒸気による熱交換器の出口側と連通したものである。 In the present invention, a steam supply pipe for heating is connected to the inlet sides of a plurality of heat exchangers via pressure regulating valves, respectively, and the outlet side of the heat exchanger using high-pressure steam is connected to the outlet side of the heat exchanger using low-pressure steam. In addition to being connected to the inlet side, a steam ejector is disposed on the inlet side of the heat exchanger using low-pressure steam, and the suction chamber of the steam ejector communicates with the outlet side of the heat exchanger using low-pressure steam.
本発明によれば、高圧蒸気による熱交換器の出口側を、低圧蒸気による熱交換器の入口側へ接続したことで、高圧蒸気の熱交換器の内部で十分な蒸気の流れを発生させ、また、低圧蒸気による熱交換器の入口側に蒸気エゼクタを配置して、この蒸気エゼクタの吸込室を、低圧蒸気による熱交換器の出口側と連通したことで、低圧蒸気の熱交換器の内部で十分な蒸気の流れを発生させ、効率良く加熱する蒸気加熱装置とすることができる。 According to the present invention, by connecting the outlet side of the high pressure steam heat exchanger to the inlet side of the low pressure steam heat exchanger, a sufficient steam flow is generated inside the high pressure steam heat exchanger, In addition, a steam ejector is arranged on the inlet side of the heat exchanger using low-pressure steam, and the suction chamber of this steam ejector is connected to the outlet side of the heat exchanger using low-pressure steam, so that the inside of the low-pressure steam heat exchanger Therefore, a steam heating device that generates a sufficient steam flow and efficiently heats the steam can be obtained.
本発明は、蒸気エゼクタを用いるものであるが、この蒸気エゼクタは、蒸気を駆動流体として、吸込室で吸引力を発生するものであれば従来公知のものを使用することができる。 The present invention uses a steam ejector. Any known steam ejector may be used as long as it generates suction force in the suction chamber using steam as a driving fluid.
本実施例においては、熱交換器としてコルゲートマシンの薄型熱盤1,2を用いた例を示す。図1において、熱盤1に接続した高圧蒸気供給管3と、熱盤2に接続した低圧蒸気供給管4と、低圧蒸気供給管4に配置した蒸気エゼクタ5とで蒸気加熱装置を構成する。 In this embodiment, an example is shown in which thin heat plates 1 and 2 of a corrugating machine are used as a heat exchanger. In FIG. 1, a high-pressure steam supply pipe 3 connected to the hot platen 1, a low-pressure steam supply pipe 4 connected to the hot platen 2, and a steam ejector 5 arranged in the low-pressure steam supply pipe 4 constitute a steam heating device.
熱盤1への高圧蒸気供給管3には圧力調整弁6を取り付ける。熱盤1の出口管7には蒸気トラップ8を取り付けてヘッダータンク9と接続する。出口管7を分岐した管路10によって、熱盤2の入口側の低圧蒸気供給管4と接続する。 A pressure regulating valve 6 is attached to the high pressure steam supply pipe 3 to the hot platen 1. A steam trap 8 is attached to the outlet pipe 7 of the hot platen 1 and connected to the header tank 9. The outlet pipe 7 is connected to the low-pressure steam supply pipe 4 on the inlet side of the hot platen 2 by a pipe line 10 branched from the outlet pipe 7.
低圧蒸気供給管4に圧力調整弁11と蒸気エゼクタ5を介在して熱盤2と接続する。熱盤2の出口側には、蒸気トラップ12とバイパス・バルブ13を並列に配置して、管路14によりヘッダータンク9と接続する。ヘッダータンク9の左上部に管路15を取り付けて、蒸気エゼクタ5の吸込室16と接続する。
The pressure control valve 11 and the steam ejector 5 are interposed in the low pressure steam supply pipe 4 and connected to the hot platen 2. A steam trap 12 and a bypass valve 13 are arranged in parallel on the outlet side of the hot platen 2 and connected to the header tank 9 by a pipe line 14. A
ヘッダータンク9の下部に管路18を取り付けて、液体圧送部材17の液体流入口19と接続する。管路18には逆止弁20を取り付ける。この逆止弁20は、ヘッダータンク9から液体圧送部材17側への液体の通過を許容し、逆方向の液体の通過は許容しないものである。 A pipe line 18 is attached to the lower part of the header tank 9 and connected to the liquid inlet 19 of the liquid pumping member 17. A check valve 20 is attached to the pipe line 18. The check valve 20 allows the passage of liquid from the header tank 9 to the liquid pressure feeding member 17 side, and does not allow the passage of liquid in the reverse direction.
液体圧送部材17の液体圧送口21にも逆止弁22を介して液体圧送管路23を接続する。この逆止弁22は液体圧送部材17から液体圧送管路23側へのみ液体を通過させるものである。 A liquid pressure feed line 23 is also connected to the liquid pressure feed port 21 of the liquid pressure feed member 17 via a check valve 22. This check valve 22 allows the liquid to pass only from the liquid pumping member 17 to the liquid pumping line 23 side.
液体圧送部材17の上部に、圧送流体としての高圧蒸気供給管24と接続した高圧蒸気導入口25を設ける。高圧蒸気導入口25の左側方に高圧蒸気の排出口26を設ける。排出口26には高圧蒸気の排出管27を接続する。 A high-pressure steam inlet 25 connected to a high-pressure steam supply pipe 24 as a pressure-feeding fluid is provided on the liquid pressure-feeding member 17. A high-pressure steam outlet 26 is provided on the left side of the high-pressure steam inlet 25. A high pressure steam discharge pipe 27 is connected to the discharge port 26.
液体圧送部材17は、内部に配置した図示しないフロートが下方部に位置する場合に、高圧蒸気の導入口25が閉口され、一方、排出口26が開口されて、ヘッダータンク9に溜まった復水が、管路18と逆止弁20を通って液体圧送部材17内へ流下する。 When the float (not shown) arranged inside is located at the lower part, the liquid pressure feeding member 17 is closed in the high-pressure steam inlet 25 while the outlet 26 is opened, and the condensate collected in the header tank 9 However, it flows down into the liquid pumping member 17 through the pipe line 18 and the check valve 20.
液体圧送部材17内に液体が溜まって図示しないフロートが所定の上方部に位置すると、排出口26が閉口され、一方、高圧蒸気の導入口25が開口されて、高圧蒸気供給管24から高圧蒸気が液体圧送部材17内に流入し、内部に溜まった液体を圧送口21と逆止弁22及び液体圧送管路23を経て液体圧送先へ圧送するものである。 When liquid accumulates in the liquid pressure feeding member 17 and a float (not shown) is positioned at a predetermined upper portion, the discharge port 26 is closed, while the high pressure steam inlet 25 is opened, and the high pressure steam supply pipe 24 opens the high pressure steam. Flows into the liquid pumping member 17, and the liquid accumulated inside is pumped to the liquid pumping destination through the pumping port 21, the check valve 22 and the liquid pumping line 23.
液体が圧送されて液体圧送部材17内の液位が低下すると、再度、高圧蒸気の導入口25が閉口され、排出口26が開口されることにより、液体流入口19から復水が圧送部材17内へ流下してくる。このような作動サイクルを繰り返すことにより、液体圧送部材17は、ヘッダータンク9内の復水を圧送するものである。 When the liquid is pumped and the liquid level in the liquid pumping member 17 is lowered, the high pressure steam inlet 25 is closed again and the outlet 26 is opened, so that the condensate is pumped from the liquid inlet 19. It flows down inside. By repeating such an operation cycle, the liquid pumping member 17 pumps the condensate in the header tank 9.
熱盤1,2へ蒸気を供給して加熱する場合は、高圧蒸気供給管3から熱盤1へ高圧蒸気を供給すると共に、低圧蒸気供給管4から熱盤2へ低圧蒸気を供給する。 When the steam is supplied to the heating plates 1 and 2 and heated, the high pressure steam is supplied from the high pressure steam supply pipe 3 to the heating plate 1 and the low pressure steam is supplied from the low pressure steam supply pipe 4 to the heating plate 2.
熱盤1を加熱して発生した復水と残余の蒸気は、出口管7を流下して蒸気トラップ8から復水がヘッダータンク9へ流入し、残余の蒸気は管路10から熱盤2の低圧蒸気供給管4へ流入する。このように、管路10によって熱盤1の残余の蒸気を、熱盤2へ供給することによって、熱盤1内で蒸気の流れを確実に発生させて熱効率を向上することができる。 Condensate generated by heating the heating platen 1 and the remaining steam flow down the outlet pipe 7, the condensed water flows from the steam trap 8 into the header tank 9, and the remaining steam flows from the pipe 10 to the heating plate 2. It flows into the low pressure steam supply pipe 4. In this way, by supplying the remaining steam of the hot platen 1 to the hot platen 2 through the pipe line 10, it is possible to reliably generate a steam flow in the hot platen 1 and improve the thermal efficiency.
熱盤2へ供給された蒸気は、一部が復水となり蒸気トラップ12からヘッダータンク9へ流入し、残余の蒸気はバイパス・バルブ13からヘッダータンク9へ流入する。ヘッダータンク9内の蒸気は、管路15を介して蒸気エゼクタ5の吸込室16へ吸引されることによって、熱盤2内で蒸気の流れを確実に発生させて熱効率を向上することができる。
Part of the steam supplied to the hot platen 2 becomes condensate and flows from the steam trap 12 to the header tank 9, and the remaining steam flows from the bypass valve 13 to the header tank 9. The steam in the header tank 9 is sucked into the suction chamber 16 of the steam ejector 5 through the
本発明は、段ボールなどを製造する場合に使用するコルゲートマシンの薄型熱盤としての蒸気加熱装置に利用することができる。 INDUSTRIAL APPLICABILITY The present invention can be used for a steam heating device as a thin hot plate of a corrugating machine used when manufacturing corrugated cardboard or the like.
1 熱盤
2 熱盤
3 高圧蒸気供給管
4 低圧蒸気供給管
5 蒸気エゼクタ
7 出口管
8 蒸気トラップ
9 ヘッダータンク
10 管路
16 吸込室
17 液体圧送部材
DESCRIPTION OF SYMBOLS 1 Hot plate 2 Hot plate 3 High pressure steam supply pipe 4 Low pressure steam supply pipe 5 Steam ejector 7 Outlet pipe 8 Steam trap 9 Header tank 10 Pipe line 16 Suction chamber 17 Liquid pressure feeding member
Claims (1)
前記第1熱交換器の出口側の出口管を分岐した一方を前記第2熱交換器の入口側へ直接接続すると共に、その他方をヘッダータンクに接続し、
前記第2熱交換器の入口側に前記低圧蒸気で駆動する蒸気エゼクタの出口側を接続し、
前記蒸気エゼクタの吸込室を、前記ヘッダータンクを介して前記第2熱交換器の出口側と連通したこと
を特徴とする蒸気加熱装置。 A steam heating apparatus using a first heat exchanger to which high-pressure steam is supplied and a second heat exchanger to which low-pressure steam is supplied ,
While directly connecting one of the outlet pipes on the outlet side of the first heat exchanger to the inlet side of the second heat exchanger, the other is connected to the header tank,
Connecting the outlet side of the steam ejector driven by the low-pressure steam to the inlet side of the second heat exchanger;
Steam heating apparatus, wherein a suction chamber of the steam ejector, in communication with the outlet side of the second heat exchanger via the header tank.
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JP2012072738A JP5973199B2 (en) | 2012-03-28 | 2012-03-28 | Steam heating device |
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JP2012072738A JP5973199B2 (en) | 2012-03-28 | 2012-03-28 | Steam heating device |
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JP2013204880A JP2013204880A (en) | 2013-10-07 |
JP5973199B2 true JP5973199B2 (en) | 2016-08-23 |
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CN108534123A (en) * | 2018-05-09 | 2018-09-14 | 江苏省宜兴中等专业学校 | A kind of thermal energy conversion kinetic energy apparatus |
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DE3037293A1 (en) * | 1980-10-02 | 1982-05-27 | Helmut 7100 Heilbronn Bälz | TELEVISION SYSTEM WITH COMMON CONDENSATE RETURN AND METHOD FOR CONDENSATE RETURN |
JP2589602B2 (en) * | 1991-04-15 | 1997-03-12 | 株式会社テイエルブイ | Steam heating device |
JPH08247406A (en) * | 1995-02-17 | 1996-09-27 | Spirax Sarco Ltd | Drain recovering system of steam plant circuit |
JPH09196305A (en) * | 1996-01-12 | 1997-07-29 | Tlv Co Ltd | Condensation recovery device |
JPH09196304A (en) * | 1996-01-12 | 1997-07-29 | Tlv Co Ltd | Condensation recovery device |
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