JP2000356304A - Steam heater - Google Patents

Steam heater

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Publication number
JP2000356304A
JP2000356304A JP11167647A JP16764799A JP2000356304A JP 2000356304 A JP2000356304 A JP 2000356304A JP 11167647 A JP11167647 A JP 11167647A JP 16764799 A JP16764799 A JP 16764799A JP 2000356304 A JP2000356304 A JP 2000356304A
Authority
JP
Japan
Prior art keywords
condensate
heating
steam
condensate recovery
header
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.)
Pending
Application number
JP11167647A
Other languages
Japanese (ja)
Inventor
Tetsuya Mita
哲也 見田
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 JP11167647A priority Critical patent/JP2000356304A/en
Publication of JP2000356304A publication Critical patent/JP2000356304A/en
Pending legal-status Critical Current

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  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain a steam heater which does not stagnate condensate generat ed in a steam consuming device. SOLUTION: A steam supply pipe 3 is connected to a jacket 2. A plurality of condensate recovery devices 16, 36 are connected to the lower port of the jacket 2 through a header 25. Condensate generated in the jacket 2 is flowed down to the header 25 and continuously discharged outside of the system by alternate force-feed of the plurality of condensate recovery devices 16, 36.

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】本発明は熱交換器内に収容し
た被加熱物を加熱用の蒸気で加熱するものに関し、特に
その加熱温度が100度C程度の比較的低温の場合に適
した蒸気加熱装置に関する。具体的には重合反応等に用
いられる各種反応釜や食品の蒸留装置、濃縮装置、ある
いは、殺菌装置等の蒸気加熱に用いるものである。これ
らの場合の被加熱物は、僅かな温度変化によって熱損傷
を生じてしまう場合が多く、加熱温度を精度良く維持す
る必要がある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for heating an object to be heated housed in a heat exchanger with steam for heating, and more particularly, to a steam suitable for a case where the heating temperature is relatively low at about 100.degree. It relates to a heating device. Specifically, it is used for steam heating of various reaction vessels used for a polymerization reaction or the like, a food distillation apparatus, a concentration apparatus, or a sterilization apparatus. In these cases, the object to be heated often causes thermal damage due to a slight change in temperature, and it is necessary to maintain the heating temperature with high accuracy.

【0002】[0002]

【従来の技術】従来の蒸気加熱装置としては例えば特開
平7−35310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、加熱手段に外気と遮断される蒸
気圧スペースを設け、該蒸気圧スペース内に大気圧より
低い圧力の飽和蒸気を圧力制御しつつ供給し、蒸気スペ
ース内に生じて来るドレン水即ち復水を圧力により作動
するポンプを介して外部へ排出するものであり、100
度C程度の比較的低温の蒸気によって被加熱物を加熱す
ることができるものである。
2. Description of the Related Art As a conventional steam heating device, for example, a device as disclosed in Japanese Patent Application Laid-Open No. 7-35310 has been used. In this method, a steam pressure space is provided in the heating means so as to be cut off from the outside air, and saturated steam having a pressure lower than the atmospheric pressure is supplied into the steam pressure space while controlling the pressure. Water is discharged to the outside through a pump operated by pressure.
The object to be heated can be heated by relatively low temperature steam of about C degrees.

【0003】[0003]

【発明が解決しようとする課題】上記従来のものは、1
台のポンプを介して所定量溜まった復水を間欠的に外部
へ排出するために、加熱部からの復水の排出も間欠的と
なり、ポンプの作動サイクルによって加熱部内に復水を
滞留してしまう問題があった。加熱部に復水を滞留する
と、復水は蒸気と比べると保有する熱量が極めて小さい
ために、被加熱物の全体が均一に加熱されず加熱ムラを
生じてしまうのである。
SUMMARY OF THE INVENTION The above-mentioned prior art has the following problems.
In order to intermittently discharge the condensed water collected by a predetermined amount to the outside through the two pumps, the discharge of the condensed water from the heating unit also becomes intermittent, and the condensed water stays in the heating unit due to the operation cycle of the pump. There was a problem. If the condensed water stays in the heating section, the condensed water has an extremely small amount of heat as compared with steam, so that the entire object to be heated is not uniformly heated, resulting in uneven heating.

【0004】従って本発明の課題は、熱交換器の加熱部
で発生した復水を確実に吸引することができるようにし
て、復水を滞留することのない、従って、加熱ムラを生
じることのない蒸気加熱装置を得ることである。
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to make sure that the condensate generated in the heating section of the heat exchanger can be sucked, so that the condensate does not stay. There is no steam heating device to get.

【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、熱交換器に加熱部を形成し
て加熱用の蒸気供給管を接続し、加熱により生じた復水
を加熱部から排出する復水回収装置を接続したものにお
いて、復水回収装置を複数台配置して、当該複数台の復
水回収装置の少なくとも1台が交互に加熱部からの復水
回収を連続的に行なうものである。
In order to solve the above-mentioned problems, the means of the present invention is to form a heating section in a heat exchanger, connect a steam supply pipe for heating, and recover the heat generated by heating. In the case where a condensate recovery device that discharges water from the heating unit is connected, a plurality of condensate recovery devices are arranged, and at least one of the plurality of condensate recovery devices alternately collects condensate from the heating unit. Is performed continuously.

【0006】[0006]

【発明の実施の形態】複数台の復水回収装置を配置し
て、少なくとも1台が交互に加熱部からの復水回収を連
続的に行なうことによって、加熱部で発生した復水を滞
留することなく排除することができる。
BEST MODE FOR CARRYING OUT THE INVENTION A plurality of condensate recovery devices are arranged, and at least one of them continuously collects condensate from a heating unit alternately, so that the condensate generated in the heating unit stays. Can be eliminated without the need.

【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の外周に加熱部としてのジ
ャケット部2を形成して蒸気供給管3を接続する。蒸気
供給管3には、順次、開閉弁4と圧力調節弁5を接続し
てジャケット部2と連通する。
EXAMPLE In this example, a reactor 1 was used as a heat exchanger.
Here is an example using. A jacket section 2 as a heating section is formed on the outer periphery of the reaction vessel 1 and a steam supply pipe 3 is connected thereto. The on-off valve 4 and the pressure control valve 5 are sequentially connected to the steam supply pipe 3 to communicate with the jacket portion 2.

【0008】ジャケット部2の上部には大気連通管10
と開閉弁11を取り付ける。ジャケット部2の下部に管
路12を接続して、ヘッダー25と管路26、27で複
数の復水回収装置16、36の復水流入口15、35と
接続する。管路12には開閉弁13を取り付け、管路2
6にはヘッダー25から復水回収装置16側のみへの流
体の通過を許容する逆止弁14を取り付け、同様に管路
27にも逆止弁24を取り付ける。
At the upper part of the jacket part 2, an atmosphere communication pipe 10 is provided.
And the on-off valve 11 are attached. The pipe 12 is connected to the lower part of the jacket portion 2 and connected to the condensate inlets 15 and 35 of the plurality of condensate recovery devices 16 and 36 by the header 25 and the pipes 26 and 27. An on-off valve 13 is attached to the pipe 12, and the pipe 2
A check valve 14 is attached to 6 to allow fluid to pass only from the header 25 to the condensate recovery device 16, and a check valve 24 is similarly attached to the pipe 27.

【0009】復水回収装置16、36の復水流出口1
7、37には、逆止弁18、38を介して回収管19、
39を接続する。逆止弁18、38は、復水回収装置1
6、36から回収管19、39側のみへの流体の通過を
許容するものである。
The condensate outlet 1 of the condensate recovery devices 16 and 36
7 and 37, the recovery pipe 19 through the check valves 18 and 38,
39 is connected. The check valves 18 and 38 are provided in the condensate recovery device 1.
The passage of the fluid from the tubes 6 and 36 to only the recovery pipes 19 and 39 is allowed.

【0010】復水回収装置16、36の上部に、圧送流
体流入口20、40と排気口21、41を設けて、圧送
流体流入口20、40を管路22を介して蒸気供給管3
と接続する。圧送流体排気口21、41はそれぞれ大気
に開放する。
[0010] Pumping fluid inlets 20 and 40 and exhaust ports 21 and 41 are provided above the condensate recovery devices 16 and 36, and the pumping fluid inlets 20 and 40 are connected to the steam supply pipe 3 through a pipe 22.
Connect with Each of the pumping fluid exhaust ports 21 and 41 is open to the atmosphere.

【0011】復水回収装置16、36は従来技術のもの
と同一であり、復水流入口15、35から流入してきた
復水が内部に溜りその水位が上昇すると図示しないフロ
ートを上昇させ、所定位置に達するとスナップ移動し
て、圧送流体流入口20、40に取り付けた圧送弁を開
弁すると共に、排気口21、41に取り付けた排気弁を
閉弁して、蒸気供給管3から高圧の蒸気が復水回収装置
16、36内部に供給されて溜まっていた復水を復水流
出口17、37から回収管19、39を介して回収先へ
圧送するものである。
The condensate recovery devices 16 and 36 are the same as those of the prior art. When the condensate flowing in from the condensate inlets 15 and 35 accumulates therein and the water level rises, the float (not shown) is raised to a predetermined position. When the pressure reaches the pressure-supplying fluid inlets 20 and 40, the pressure-feeding valves are opened, and the exhaust valves attached to the exhaust ports 21 and 41 are closed. Is to condense the condensed water supplied and accumulated inside the condensate recovery devices 16 and 36 from the condensate outlets 17 and 37 to the collection destination via the recovery pipes 19 and 39.

【0012】複数の復水回収装置16、36は、ヘッダ
ー25からの立ち下げ管路長さを変えることにより、少
なくとも1台が交互にヘッダー25即ちジャケット部2
からの復水回収を連続的に行なうことができるものであ
る。本実施例においては、立ち下げ管路の長い復水回収
装置36にまず復水が流下して、所定量溜まって復水回
収装置36がその溜まった復水を圧送している関に、立
ち下げ管路の短いもう一方の復水回収装置16にヘッダ
ー25から復水が流下するものである。
At least one of the plurality of condensate recovery devices 16 and 36 alternately has a header 25, that is, a jacket portion 2 by changing the length of the falling pipe from the header 25.
, And the condensate can be continuously collected. In the present embodiment, the condensate first flows down to the condensate recovery device 36 having a long falling pipe, and the condensate is collected by a predetermined amount. The condensate flows down from the header 25 to the other condensate recovery device 16 having a shorter downcomer.

【0013】復水回収装置16、36内の復水が圧送さ
れるに連れて、図示しないフロートが降下して、所定の
液位まで低下するとスナップ移動して、圧送流体流入口
20、40の圧送弁を閉弁すると共に、排気口21、4
1に取り付けた排気弁が開弁して、ヘッダー25から復
水が流下してくるものである。
As the condensate in the condensate recovery devices 16 and 36 is pumped, the float (not shown) descends and snaps when it drops to a predetermined liquid level. While closing the pressure feed valve, the exhaust ports 21 and 4
The exhaust valve attached to 1 opens, and condensate flows down from the header 25.

【0014】蒸気供給管3から反応釜1のジャケット部
2へ加熱用の蒸気を供給することにより、反応釜1内の
被加熱物が加熱される。加熱蒸気温度は圧力調節弁5に
よって蒸気圧力を調節することにより、蒸気、厳密には
飽和蒸気、の圧力と温度は1対1の関係があるために、
任意に調節することができる。加熱により熱を奪われた
蒸気は凝縮して復水となる。
By supplying steam for heating from the steam supply pipe 3 to the jacket portion 2 of the reaction vessel 1, an object to be heated in the reaction vessel 1 is heated. The heating steam temperature is adjusted by adjusting the steam pressure by the pressure control valve 5, so that the pressure and the temperature of the steam, more specifically, the saturated steam, have a one-to-one relationship.
It can be adjusted arbitrarily. The steam deprived of heat by heating condenses and becomes condensed water.

【0015】ジャケット部2で発生した復水はヘッダー
25に流下して、複数の復水回収装置16、36を介し
て滞留することなく系外へ排出される。
The condensed water generated in the jacket portion 2 flows down to the header 25 and is discharged out of the system via the plurality of condensed water collecting devices 16 and 36 without being accumulated.

【0016】[0016]

【発明の効果】上記のように本発明によれば、複数台の
復水回収装置を配置して少なくとも1台が交互に加熱部
からの復水回収を連続的に行なうことによって、加熱部
に復水を滞留することがなく、熱交換器の被加熱物に加
熱温度ムラを生じることもなく均一に加熱することがで
きる。
As described above, according to the present invention, a plurality of condensate recovery devices are arranged, and at least one of the devices continuously performs condensate recovery from the heating unit alternately, so that the heating unit The condensate does not stay, and the object to be heated of the heat exchanger can be heated uniformly without causing uneven heating temperature.

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

【図1】本発明の蒸気加熱装置の実施例を示す構成図。FIG. 1 is a configuration diagram showing an embodiment of a steam heating device of the present invention.

【符号の説明】[Explanation of symbols]

1 反応釜 2 ジャケット部 3 蒸気供給管 15 復水流入口 16 復水回収装置 17 復水流出口 20 圧送流体流入口 21 排気口 25 ヘッダー 35 復水流入口 36 復水回収装置 37 復水流出口 DESCRIPTION OF SYMBOLS 1 Reactor 2 Jacket part 3 Steam supply pipe 15 Condensate inlet 16 Condensate recovery device 17 Condensate outlet 20 Pumping fluid inlet 21 Exhaust port 25 Header 35 Condensate inlet 36 Condensate recovery device 37 Condensate outlet

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 熱交換器に加熱部を形成して加熱用の蒸
気供給管を接続し、加熱により生じた復水を加熱部から
排出する復水回収装置を接続したものにおいて、復水回
収装置を複数台配置して、当該複数台の復水回収装置の
少なくとも1台が交互に加熱部からの復水回収を連続的
に行なうことを特徴とする蒸気加熱装置。
1. A condensate recovery apparatus comprising a heat exchanger, a heating section formed therein, a steam supply pipe for heating connected thereto, and a condensate recovery apparatus for discharging condensate generated by heating from the heating section connected thereto. A steam heating device, wherein a plurality of devices are arranged, and at least one of the plurality of condensate recovery devices continuously performs condensate recovery from the heating unit alternately.
JP11167647A 1999-06-15 1999-06-15 Steam heater Pending JP2000356304A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11167647A JP2000356304A (en) 1999-06-15 1999-06-15 Steam heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11167647A JP2000356304A (en) 1999-06-15 1999-06-15 Steam heater

Publications (1)

Publication Number Publication Date
JP2000356304A true JP2000356304A (en) 2000-12-26

Family

ID=15853653

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11167647A Pending JP2000356304A (en) 1999-06-15 1999-06-15 Steam heater

Country Status (1)

Country Link
JP (1) JP2000356304A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011085325A (en) * 2009-10-16 2011-04-28 Tlv Co Ltd Condensate recovery device
JP2011085326A (en) * 2009-10-16 2011-04-28 Tlv Co Ltd Condensate recovery device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011085325A (en) * 2009-10-16 2011-04-28 Tlv Co Ltd Condensate recovery device
JP2011085326A (en) * 2009-10-16 2011-04-28 Tlv Co Ltd Condensate recovery device

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