JP4943224B2 - Vacuum steam heater - Google Patents

Vacuum steam heater Download PDF

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JP4943224B2
JP4943224B2 JP2007129447A JP2007129447A JP4943224B2 JP 4943224 B2 JP4943224 B2 JP 4943224B2 JP 2007129447 A JP2007129447 A JP 2007129447A JP 2007129447 A JP2007129447 A JP 2007129447A JP 4943224 B2 JP4943224 B2 JP 4943224B2
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steam
supply pipe
cooling water
heat exchanger
water supply
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JP2007129447A
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JP2008284424A (en
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速人 喜田
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Tlv Co Ltd
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Tlv Co Ltd
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Description

本発明は、熱交換器内の被加熱物を低圧蒸気で加熱するものに関し、特にその加熱蒸気温度が100℃程度の比較的低温の場合に適した減圧蒸気加熱装置に関する。  The present invention relates to an apparatus for heating an object to be heated in a heat exchanger with low-pressure steam, and more particularly to a reduced-pressure steam heating apparatus suitable when the heating steam temperature is a relatively low temperature of about 100 ° C.

従来の減圧蒸気加熱装置は、熱交換器と、この熱交換器に加熱用の蒸気を供給する蒸気供給管と、熱交換器内の流体を吸引する吸引手段を接続し、蒸気供給管に冷却水供給管を接続して、この冷却水供給管からの冷却水によって加熱用蒸気の過熱度を調節することができるものである。  A conventional vacuum steam heating apparatus is connected to a heat exchanger, a steam supply pipe for supplying steam for heating to the heat exchanger, and a suction means for sucking fluid in the heat exchanger, and cooled to the steam supply pipe. By connecting a water supply pipe, the superheat degree of the heating steam can be adjusted by the cooling water from the cooling water supply pipe.

上記従来の減圧蒸気加熱装置では、蒸気供給管の上部から冷却水を供給するものであるが、蒸気と冷却水の混合を確実に行うことができずに、熱交換器へ供給する加熱用蒸気の全体の過熱度を均一に調節することができない問題があった。
特開平11−319544号公報
In the conventional reduced pressure steam heating device, the cooling water is supplied from the upper part of the steam supply pipe. However, the steam for heating supplied to the heat exchanger cannot be reliably mixed with the steam. There was a problem that the overall degree of superheat of the material could not be adjusted uniformly.
JP 11-319544 A

解決しようとする課題は、熱交換器へ供給する蒸気の全体の過熱度を均一に調節することのできる減圧蒸気加熱装置を得ることである。   The problem to be solved is to obtain a reduced pressure steam heating apparatus capable of uniformly adjusting the overall superheat degree of steam supplied to the heat exchanger.

本発明は、熱交換器と、当該熱交換器に加熱用の蒸気を供給する蒸気供給管と、熱交換器内の流体を吸引する吸引手段を接続し、蒸気供給管に冷却水供給管を接続して、当該冷却水供給管から供給する冷却水によって加熱用蒸気の過熱度を調節するものにおいて、蒸気供給管と冷却水供給管を混合部でそれぞれ反対方向から水平方向に接合させて、蒸気供給管内の蒸気の流れと反対方向に、冷却水供給管から冷却水を供給することにより、蒸気と冷却水が衝突しながら混合されるものである。 The present invention connects a heat exchanger, a steam supply pipe for supplying heating steam to the heat exchanger, and a suction means for sucking a fluid in the heat exchanger, and a cooling water supply pipe is connected to the steam supply pipe. Connecting and adjusting the superheat degree of the heating steam by the cooling water supplied from the cooling water supply pipe , the steam supply pipe and the cooling water supply pipe are joined in the horizontal direction from the opposite direction in the mixing unit, respectively. By supplying the cooling water from the cooling water supply pipe in the opposite direction to the flow of the steam in the steam supply pipe , the steam and the cooling water are mixed while colliding .

本発明は、蒸気供給管内の蒸気の流れと反対方向に、冷却水供給管から冷却水を供給することにより、蒸気と冷却水が互いに衝突しながら混合されることによって、その混合が確実なものとなり、熱交換器へ供給する蒸気の全体の過熱度を均一に調節することができる。   In the present invention, the cooling water is supplied from the cooling water supply pipe in the opposite direction to the flow of the steam in the steam supply pipe, so that the steam and the cooling water are mixed while colliding with each other, thereby ensuring the mixing. Thus, the overall superheat degree of the steam supplied to the heat exchanger can be adjusted uniformly.

本発明は、蒸気供給管からの蒸気と冷却水を衝突させて混合するものであるが、蒸気供給管内全体に冷却水を供給するために、冷却水スプレーノズルを用いることが望ましい。   In the present invention, the steam from the steam supply pipe collides with the cooling water, and it is desirable to use a cooling water spray nozzle in order to supply the cooling water to the entire inside of the steam supply pipe.

図1において、熱交換器としての反応釜1と吸引手段2と加熱用蒸気供給管3、及び、冷却水供給管6とで減圧蒸気加熱装置を構成する。蒸気供給管3と冷却水供給管6は、混合部4でそれぞれ反対方向から水平方向に接合させる。   In FIG. 1, a reduced pressure steam heating apparatus is constituted by a reaction kettle 1 as a heat exchanger, a suction means 2, a heating steam supply pipe 3 and a cooling water supply pipe 6. The steam supply pipe 3 and the cooling water supply pipe 6 are joined to each other in the horizontal direction from the opposite direction in the mixing unit 4.

蒸気供給管3は図示しないボイラー等の蒸気源と接続すると共に、蒸気圧力調節弁7と開閉弁8を取り付けて、混合部4を介して熱交換器としての反応釜1のジャケット部11と接続する。  The steam supply pipe 3 is connected to a steam source such as a boiler (not shown), and a steam pressure control valve 7 and an on-off valve 8 are attached to the steam supply pipe 3 and connected to the jacket portion 11 of the reaction kettle 1 as a heat exchanger via the mixing portion 4. To do.

反応釜1のジャケット部11の下端を、蒸気トラップ12とバルブ13を介して吸引手段2のエゼクタ14と接続する。吸引手段2は、エゼクタ14とタンク5と循環ポンプ15に循環路16を介して接続した組み合わせポンプとして構成する。エゼクタ14はタンク5内の循環水を循環ポンプ15で循環して通過させることにより、その液体温度に応じた吸引力を生じるものである。なお、タンク5の上部には冷却水補給管21を接続する。  The lower end of the jacket portion 11 of the reaction kettle 1 is connected to the ejector 14 of the suction means 2 through a steam trap 12 and a valve 13. The suction means 2 is configured as a combination pump connected to the ejector 14, the tank 5, and the circulation pump 15 via the circulation path 16. The ejector 14 circulates the circulating water in the tank 5 through the circulation pump 15 to generate a suction force corresponding to the liquid temperature. A cooling water supply pipe 21 is connected to the upper part of the tank 5.

循管路16を分岐して、余剰水排出管9と冷却水供給管6を連通する。余剰水排出管9には開閉弁10を取り付けて、図示しないタンク5内のレベル計と連動してタンク5内の液位を所定レベルに維持する。  The circulation path 16 is branched and the surplus water discharge pipe 9 and the cooling water supply pipe 6 are communicated. An open / close valve 10 is attached to the surplus water discharge pipe 9 to maintain the liquid level in the tank 5 at a predetermined level in conjunction with a level meter in the tank 5 (not shown).

冷却水供給管6は、組み合わせポンプ2の循環水の一部を混合部4へ供給するものであり、冷却水供給管6の混合部4側の端部に図示しないスプレーノズルを内蔵して、蒸気供給管3から供給される過熱蒸気と冷却水が衝突することによって、過熱蒸気の全体が均一な温度まで減温されるものである。混合部4で所定温度まで減温された蒸気は、管路17を介してジャケット部11へ供給される。  The cooling water supply pipe 6 supplies a part of the circulating water of the combination pump 2 to the mixing unit 4. A spray nozzle (not shown) is incorporated in the end of the cooling water supply pipe 6 on the mixing unit 4 side, When the superheated steam supplied from the steam supply pipe 3 collides with the cooling water, the temperature of the whole superheated steam is reduced to a uniform temperature. The steam reduced to a predetermined temperature by the mixing unit 4 is supplied to the jacket unit 11 via the pipe line 17.

本実施例においては冷却水供給管6を、吸引手段2の循環流体の一部を分岐して供給するものとして示したが、冷却水供給管6の水は、循環流体に限る必要はなく、別途の温度の冷却水を用いることもできる。  In the present embodiment, the cooling water supply pipe 6 is shown as a part of the circulating fluid of the suction means 2 that is branched and supplied. However, the water in the cooling water supply pipe 6 is not limited to the circulating fluid, Cooling water at a separate temperature can also be used.

反応釜1内の図示しない被加熱物を加熱する場合、蒸気供給管3から加熱用の蒸気をジャケット部11に供給すると共に、循環ポンプ15を駆動してエゼクタ14で吸引力を発生させる。  When heating an object (not shown) in the reaction kettle 1, heating steam is supplied from the steam supply pipe 3 to the jacket portion 11, and the circulation pump 15 is driven to generate a suction force by the ejector 14.

この場合、加熱用の蒸気は蒸気圧力調節弁7で所定の圧力まで減圧されるが、圧力が減圧されても保有している熱量はほとんど減少することが無いために、減圧蒸気は過熱蒸気となる。しかしながら、冷却水供給管6から吸引手段2の循環水の一部が混合部4から過熱蒸気中に供給されることによって、過熱蒸気は飽和温度蒸気まで減温される。冷却水供給管6から供給される冷却水の量は、弁手段19の開度を適宜調整することにより、制御することができる。 In this case, the steam for heating is depressurized to a predetermined pressure by the steam pressure control valve 7, but even if the pressure is depressurized, the amount of heat possessed hardly decreases, so that the depressurized steam is superheated steam. Become. However, when a part of the circulating water of the suction means 2 is supplied from the cooling water supply pipe 6 into the superheated steam from the mixing unit 4, the superheated steam is reduced to the saturated temperature steam. The amount of cooling water supplied from the cooling water supply pipe 6 can be controlled by appropriately adjusting the opening degree of the valve means 19.

本発明に係る減圧蒸気加熱装置の実施例を示す構成図。The block diagram which shows the Example of the pressure reduction steam heating apparatus which concerns on this invention.

符号の説明Explanation of symbols

1 反応釜
2 吸引手段
3 蒸気供給管
4 混合部
5 タンク
6 冷却水供給管
11 ジャケット部
14 エゼクタ
15 循環ポンプ
16 循環路
17 管路
19 弁手段
DESCRIPTION OF SYMBOLS 1 Reaction kettle 2 Suction means 3 Steam supply pipe 4 Mixing part 5 Tank 6 Cooling water supply pipe 11 Jacket part 14 Ejector 15 Circulation pump 16 Circulation path 17 Pipe line 19 Valve means

Claims (1)

熱交換器と、当該熱交換器に加熱用の蒸気を供給する蒸気供給管と、熱交換器内の流体を吸引する吸引手段を接続し、蒸気供給管に冷却水供給管を接続して、当該冷却水供給管から供給する冷却水によって加熱用蒸気の過熱度を調節するものにおいて、蒸気供給管と冷却水供給管を混合部でそれぞれ反対方向から水平方向に接合させて、蒸気供給管内の蒸気の流れと反対方向に、冷却水供給管から冷却水を供給することにより、蒸気と冷却水が衝突しながら混合されることを特徴とする減圧蒸気加熱装置。 A heat exchanger, a steam supply pipe for supplying steam for heating to the heat exchanger, a suction means for sucking a fluid in the heat exchanger, and a cooling water supply pipe connected to the steam supply pipe; In the case where the superheat degree of the heating steam is adjusted by the cooling water supplied from the cooling water supply pipe, the steam supply pipe and the cooling water supply pipe are joined in the horizontal direction from opposite directions in the mixing section, A reduced pressure steam heating apparatus , wherein steam and cooling water are mixed while colliding by supplying cooling water from a cooling water supply pipe in a direction opposite to the flow of steam.
JP2007129447A 2007-05-15 2007-05-15 Vacuum steam heater Expired - Fee Related JP4943224B2 (en)

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JP4943224B2 true JP4943224B2 (en) 2012-05-30

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011062597A (en) * 2009-09-15 2011-03-31 Tlv Co Ltd Steam heater
CN102908966B (en) * 2012-10-11 2015-04-08 四川省精细化工研究设计院 Environment-friendly liquid circulation reactor

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10300016A (en) * 1997-04-30 1998-11-13 Mitsubishi Heavy Ind Ltd Steam desuperheater
JPH11319544A (en) * 1998-05-15 1999-11-24 Tlv Co Ltd Reduced-pressure vapor heating device

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