JPH09250705A - Pressure reduction steam generating device - Google Patents

Pressure reduction steam generating device

Info

Publication number
JPH09250705A
JPH09250705A JP8740996A JP8740996A JPH09250705A JP H09250705 A JPH09250705 A JP H09250705A JP 8740996 A JP8740996 A JP 8740996A JP 8740996 A JP8740996 A JP 8740996A JP H09250705 A JPH09250705 A JP H09250705A
Authority
JP
Japan
Prior art keywords
steam
ejector
tank
heat exchanger
pressure reduction
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
Application number
JP8740996A
Other languages
Japanese (ja)
Other versions
JP3751679B2 (en
Inventor
Takayuki Morii
高之 森井
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TLV Co Ltd
Original Assignee
TLV Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by TLV Co Ltd filed Critical TLV Co Ltd
Priority to JP08740996A priority Critical patent/JP3751679B2/en
Publication of JPH09250705A publication Critical patent/JPH09250705A/en
Application granted granted Critical
Publication of JP3751679B2 publication Critical patent/JP3751679B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a pressure reduction steam generating device to eliminate a need for the feed of cooling water for regulating the degree of reduction of a pressure. SOLUTION: A jacket part 5 is connected to a steam feed pipe 3 through a steam ejector 2. The lower part of the jacket part 5 is connected to an ejector 16 of a combination pump 15. The combination pump 15 is comprised by the ejector 16, a tank 17, and a re-circulation pump 18. The upper part of the tank 17 is connected to a suction chamber 8 of the steam ejector 2 through a line 19 and a valve 20. Condensate in the tank 17 is vaporized through the suction force of the steam ejector 2 and condensate is cooled by a heat of vaporization.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、100度C以下程
度の比較的低温の蒸気を発生して被加熱物を加熱するも
のに関し、石油化学工業や合成繊維工業、あるいは、合
成樹脂工業等の各種加熱工程に使用される減圧蒸気発生
装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heater for heating an object to be heated by generating steam at a relatively low temperature of about 100 ° C. or less, and is used in the petrochemical industry, synthetic fiber industry, synthetic resin industry, etc. The present invention relates to a reduced pressure steam generator used in various heating processes.

【0002】[0002]

【従来技術】従来の減圧蒸気発生装置としては、例えば
特公平7−88933号公報に示されているようなもの
が用いられていた。これは、間接加熱容器の一次側に蒸
気供給管を接続し、二次側にエゼクタと開放タンクと渦
巻きポンプから成るエゼクタ式真空ポンプを接続して、
開放タンク内へ冷却水を供給して所定の流体温度とする
ことにより、真空度すなわち減圧度を調整して、被加熱
物を100度C以下程度の比較的低温蒸気でもって加熱
することができるものである。
2. Description of the Related Art As a conventional reduced pressure steam generator, for example, the one disclosed in Japanese Patent Publication No. 7-88933 has been used. This is connected to the steam supply pipe on the primary side of the indirect heating container, and connected to the secondary side is an ejector vacuum pump consisting of an ejector, an open tank and a spiral pump.
By supplying cooling water into the open tank to bring it to a predetermined fluid temperature, the degree of vacuum, that is, the degree of pressure reduction can be adjusted, and the object to be heated can be heated with relatively low-temperature steam of about 100 ° C. or less. It is a thing.

【0003】[0003]

【発明が解決しようとする課題】上記従来の減圧蒸気発
生装置を用いた場合、減圧度を調整するためにタンク内
へ冷却水をほぼ連続的に供給しなければならず、多量の
冷却水を必要とする問題があった。特に、減圧度を高め
るためには、流体温度を極めて低くしなければならない
ために大量の冷却水を供給しなければならなかったので
ある。
When the above conventional reduced pressure steam generator is used, cooling water must be supplied almost continuously into the tank in order to adjust the degree of pressure reduction, and a large amount of cooling water is required. There was a problem I needed. In particular, in order to increase the degree of pressure reduction, it was necessary to supply a large amount of cooling water because the fluid temperature had to be extremely low.

【0004】従って本発明の技術的課題は、タンクへ供
給する冷却水の量が少量かあるいは不要とすることので
きる、減圧蒸気発生装置を得ることである。
Therefore, a technical object of the present invention is to obtain a reduced pressure steam generator capable of reducing the amount of cooling water supplied to a tank or making it unnecessary.

【0005】[0005]

【課題を解決するための手段】上記の課題を解決するた
めに講じた本発明の手段は、熱交換器の一次側に蒸気供
給管を接続し、熱交換器の二次側にエゼクタとタンクと
循環ポンプを有する吸引手段を連設したものにおいて、
蒸気供給管にスチ―ムエゼクタを配置して、当該スチ―
ムエゼクタの入口側を蒸気供給管と接続すると共に、出
口側を熱交換器と接続し、スチ―ムエゼクタの吸引室を
タンク上部と接続したものである。
Means for Solving the Problems The means of the present invention taken to solve the above-mentioned problems is to connect a steam supply pipe to the primary side of a heat exchanger and to connect an ejector and a tank to the secondary side of the heat exchanger. And a suction means having a circulation pump connected in series,
Place a steam ejector in the steam supply pipe to
The inlet side of the mue ejector is connected to the steam supply pipe, the outlet side is connected to the heat exchanger, and the suction chamber of the steam ejector is connected to the upper part of the tank.

【0006】[0006]

【発明の実施の形態】スチ―ムエゼクタを蒸気供給管と
接続し、その出口側を熱交換器と接続したことにより、
熱交換器へ加熱用の蒸気を供給する場合に必ずスチ―ム
エゼクタの吸引室では吸引力を生じる。一方、この吸引
室とタンクの上部を接続したことにより、吸引力はタン
クにも及ぶ。タンクへは熱交換器で被加熱物を加熱して
凝縮した蒸気の復水が流下するが、タンク内はスチ―ム
エゼクタの吸引力により減圧状態であるために、復水は
盛んに蒸発してその気化熱によって冷却される。蒸発し
た蒸気はスチ―ムエゼクタに吸引されて加熱用の蒸気と
混合されて再度熱交換器へ供給される。
BEST MODE FOR CARRYING OUT THE INVENTION By connecting a steam ejector to a steam supply pipe and connecting its outlet side to a heat exchanger,
When supplying steam for heating to the heat exchanger, a suction force is always generated in the suction chamber of the steam ejector. On the other hand, the suction force extends to the tank by connecting the suction chamber and the upper part of the tank. Condensate of steam that has condensed by heating the object to be heated by the heat exchanger flows into the tank, but since the pressure inside the tank is reduced due to the suction force of the steam ejector, the condensed water evaporates vigorously. It is cooled by the heat of vaporization. The vaporized vapor is sucked by the steam ejector, mixed with the vapor for heating, and supplied again to the heat exchanger.

【0007】[0007]

【実施例】本実施例においては熱交換器として反応釜1
を用いた例を示す。反応釜1の一次側にスチ―ムエゼク
タ2を介して蒸気供給管3を接続すると共に、スチ―ム
エゼクタ2の出口側を管路4を介して反応釜1のジャケ
ット部5と接続する。蒸気供給管3には開閉弁6と圧力
調節弁7を取り付けてスチ―ムエゼクタ2の吸引室8内
のノズル部と接続し、ディフュ―ザ9を管路4と接続す
る。管路4には開閉弁10を取り付けると共に、分岐管
11と開閉弁12を取り付けて大気と連通可能にする。
EXAMPLE In this example, a reaction vessel 1 was used as a heat exchanger.
Here is an example using. A steam supply pipe 3 is connected to the primary side of the reaction kettle 1 via a steam ejector 2, and an outlet side of the steam ejector 2 is connected to a jacket portion 5 of the reaction kettle 1 via a pipe line 4. An opening / closing valve 6 and a pressure control valve 7 are attached to the steam supply pipe 3 and connected to the nozzle portion in the suction chamber 8 of the steam ejector 2, and the diffuser 9 is connected to the pipe line 4. An on-off valve 10 is attached to the pipe line 4, and a branch pipe 11 and an on-off valve 12 are attached to enable communication with the atmosphere.

【0008】ジャケット部5の下部に開閉弁13とスチ
―ムトラップ14を並列に介して、吸引手段としての組
み合わせポンプ15のエゼクタ16と接続する。組み合
わせポンプ15は、エゼクタ16とタンク17と循環ポ
ンプ18で形成する。タンク17内の液体を循環ポンプ
18で循環路21内を循環させて、エゼクタ16部で吸
引力を生じるものである。タンク17の上部とスチ―ム
エゼクタ2の吸引室8を管路19と弁20を介して接続
する。タンク17上部には循環水を補給するための補給
水管22と、弁23を開弁することによりオ―バ―フロ
―を行うオ―バ―フロ―管24を取り付ける。
An opening / closing valve 13 and a steam trap 14 are connected in parallel to the lower portion of the jacket portion 5 and are connected to an ejector 16 of a combination pump 15 as suction means. The combination pump 15 includes an ejector 16, a tank 17 and a circulation pump 18. The liquid in the tank 17 is circulated in the circulation passage 21 by the circulation pump 18, and suction force is generated in the ejector 16 part. The upper part of the tank 17 and the suction chamber 8 of the steam ejector 2 are connected to each other via a conduit 19 and a valve 20. A replenishment water pipe 22 for replenishing circulating water and an overflow pipe 24 for performing an overflow by opening a valve 23 are attached to the upper part of the tank 17.

【0009】循環路21を分岐して余剰水排出管25を
取り付ける。循環ポンプ18の吸込口と吐出口にはそれ
ぞれ開閉弁26,27を取り付ける。
The circulation path 21 is branched and a surplus water discharge pipe 25 is attached. On-off valves 26 and 27 are attached to the suction port and the discharge port of the circulation pump 18, respectively.

【0010】蒸気供給管3の開閉弁6を開弁してスチ―
ムエゼクタ2から反応釜1のジャケット部5へ加熱用の
蒸気を供給する。この場合、圧力調節弁7により所望の
圧力すなわち温度となるように調節する。ジャケット部
5へ供給された蒸気は反応釜1内の被加熱物を加熱する
ことにより凝縮して復水となり、スチ―ムトラップ14
から組み合わせポンプ15のエゼクタ16へ吸引され、
タンク17へ至る。
The opening / closing valve 6 of the steam supply pipe 3 is opened to open the steam pipe.
Steam for heating is supplied from the mue ejector 2 to the jacket 5 of the reaction kettle 1. In this case, the pressure control valve 7 adjusts the pressure to a desired value, that is, the temperature. The steam supplied to the jacket portion 5 is condensed by heating the object to be heated in the reaction kettle 1 to become condensed water, and the steam trap 14
Is sucked into the ejector 16 of the combination pump 15,
Reach tank 17.

【0011】タンク17はスチ―ムエゼクタ2により吸
引されているために、タンク17内の復水の一部は蒸発
しその気化熱によって冷却される。所定の温度となりタ
ンク17内に滞留した復水は、循環ポンプ18に吸引さ
れて循環路21からエゼクタ16へ至りジャケット部5
内の復水を吸引する。
Since the tank 17 is sucked by the steam ejector 2, a part of the condensed water in the tank 17 evaporates and is cooled by its heat of vaporization. The condensate that has reached a predetermined temperature and has accumulated in the tank 17 is sucked by the circulation pump 18 and reaches the ejector 16 from the circulation path 21 to reach the jacket portion 5.
Aspirate the condensate inside.

【0012】エゼクタ16で生じる吸引力は、エゼクタ
16内を流下する流体の温度に対する飽和圧力となるた
めに、流体の温度を低くすれば吸引力は増し、高くすれ
ば吸引力は低下する。
Since the suction force generated by the ejector 16 becomes a saturated pressure with respect to the temperature of the fluid flowing in the ejector 16, the suction force increases when the temperature of the fluid is lowered, and the suction force decreases when the temperature of the fluid is raised.

【0013】蒸気供給管3からジャケット部5へ蒸気を
供給する前に、スチ―ムエゼクタ2に蒸気を供給しつ
つ、開閉弁12を開弁し、開閉弁10を閉弁し、及び、
開閉弁13を開弁することにより、スチ―ムエゼクタ2
の吸引力でジャケット部5内及びタンク17内の残留空
気を分岐管11から蒸気と共に大気中に排出することが
でき、ジャケット部5内及びタンク17内を所定の減圧
状態としておくことができる。
Before supplying steam from the steam supply pipe 3 to the jacket part 5, while supplying steam to the steam ejector 2, the opening / closing valve 12 is opened and the opening / closing valve 10 is closed, and
The steam ejector 2 is opened by opening the on-off valve 13.
With this suction force, the residual air in the jacket portion 5 and the tank 17 can be discharged into the atmosphere together with the steam from the branch pipe 11, and the inside of the jacket portion 5 and the tank 17 can be kept in a predetermined depressurized state.

【0014】[0014]

【発明の効果】上記のように本発明によれば、スチ―ム
エゼクタの吸引力によりタンク内の流体の温度を低下さ
せることができるために、別途冷却水を供給することは
不要となる。
As described above, according to the present invention, since the temperature of the fluid in the tank can be lowered by the suction force of the steam ejector, it is not necessary to separately supply cooling water.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の減圧蒸気発生装置の実施例を示す構成
図である。
FIG. 1 is a configuration diagram showing an embodiment of a reduced pressure steam generator of the present invention.

【符号の説明】[Explanation of symbols]

1 反応釜 2 スチ―ムエゼクタ 3 蒸気供給管 5 ジャケット部 8 吸引室 15 組み合わせポンプ 16 エゼクタ 17 タンク 18 循環ポンプ 19 管路 1 Reactor 2 Steam Ejector 3 Steam Supply Pipe 5 Jacket 8 Suction Chamber 15 Combination Pump 16 Ejector 17 Tank 18 Circulation Pump 19 Pipeline

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 熱交換器の一次側に蒸気供給管を接続
し、熱交換器の二次側にエゼクタとタンクと循環ポンプ
を有する吸引手段を連設したものにおいて、蒸気供給管
にスチ―ムエゼクタを配置して、当該スチ―ムエゼクタ
の入口側を蒸気供給管と接続すると共に、出口側を熱交
換器と接続し、スチ―ムエゼクタの吸引室をタンク上部
と接続したことを特徴とする減圧蒸気発生装置。
1. A steam supply pipe is connected to a primary side of a heat exchanger, and a suction means having an ejector, a tank and a circulation pump is connected to a secondary side of the heat exchanger. A decompression characterized in that a mue ejector is arranged, the inlet side of the steam ejector is connected to the steam supply pipe, the outlet side is connected to a heat exchanger, and the suction chamber of the steam ejector is connected to the upper part of the tank Steam generator.
JP08740996A 1996-03-15 1996-03-15 Vacuum steam generator Expired - Fee Related JP3751679B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP08740996A JP3751679B2 (en) 1996-03-15 1996-03-15 Vacuum steam generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP08740996A JP3751679B2 (en) 1996-03-15 1996-03-15 Vacuum steam generator

Publications (2)

Publication Number Publication Date
JPH09250705A true JPH09250705A (en) 1997-09-22
JP3751679B2 JP3751679B2 (en) 2006-03-01

Family

ID=13914089

Family Applications (1)

Application Number Title Priority Date Filing Date
JP08740996A Expired - Fee Related JP3751679B2 (en) 1996-03-15 1996-03-15 Vacuum steam generator

Country Status (1)

Country Link
JP (1) JP3751679B2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001113182A (en) * 1999-10-15 2001-04-24 Tlv Co Ltd Steam heater
JP2001113183A (en) * 1999-10-15 2001-04-24 Tlv Co Ltd Steam heater
JP2001116470A (en) * 1999-10-15 2001-04-27 Tlv Co Ltd Steam heating device
JP2002370237A (en) * 2001-06-15 2002-12-24 Tlv Co Ltd Steam vulcanizing equipment
JP2003053739A (en) * 2001-08-10 2003-02-26 Tlv Co Ltd Steam vulcanization apparatus
JP2016214130A (en) * 2015-05-19 2016-12-22 新光産業株式会社 Food liquid heating sterilization method and device

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001113182A (en) * 1999-10-15 2001-04-24 Tlv Co Ltd Steam heater
JP2001113183A (en) * 1999-10-15 2001-04-24 Tlv Co Ltd Steam heater
JP2001116470A (en) * 1999-10-15 2001-04-27 Tlv Co Ltd Steam heating device
JP2002370237A (en) * 2001-06-15 2002-12-24 Tlv Co Ltd Steam vulcanizing equipment
JP2003053739A (en) * 2001-08-10 2003-02-26 Tlv Co Ltd Steam vulcanization apparatus
JP2016214130A (en) * 2015-05-19 2016-12-22 新光産業株式会社 Food liquid heating sterilization method and device

Also Published As

Publication number Publication date
JP3751679B2 (en) 2006-03-01

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