JPH08170885A - Steam heater - Google Patents

Steam heater

Info

Publication number
JPH08170885A
JPH08170885A JP33393994A JP33393994A JPH08170885A JP H08170885 A JPH08170885 A JP H08170885A JP 33393994 A JP33393994 A JP 33393994A JP 33393994 A JP33393994 A JP 33393994A JP H08170885 A JPH08170885 A JP H08170885A
Authority
JP
Japan
Prior art keywords
steam
heating
receiver
condensate
heat exchanger
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
JP33393994A
Other languages
Japanese (ja)
Other versions
JP3282004B2 (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 JP33393994A priority Critical patent/JP3282004B2/en
Publication of JPH08170885A publication Critical patent/JPH08170885A/en
Application granted granted Critical
Publication of JP3282004B2 publication Critical patent/JP3282004B2/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

PURPOSE: To obtain a steam heater which can heat a material to be heated with steam at 100 deg.C or so uniformly and precisely. CONSTITUTION: A steam-feeding pipe 2 for heating is connected with a heat- exchanger 1. A condensed water storage part 7 is connected with the lower part of the heat-exchanger 1 through a steam trap 4. A down pipe 8 is provided at a side part of the condensed water storage part 7, and the lower end thereof is allowed to communicate within a receiver 11. An opening and closing valve 13 and an air vent 12 are provided at the upper part of the receiver 11. The lower part of the receiver 11 is connected with a suction port 16 for a circulating pump 15, and a discharge port 17 therefor is connected with the lower end of the condensed water storage part 7 through a pipe line 18.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は熱交換器内の被加熱物を
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
食品の蒸溜装置、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、
少しの温度上昇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 heating an object to be heated in a heat exchanger with steam, and particularly, the heating temperature thereof is 100.
The present invention relates to a steam heating device suitable for a relatively low temperature of about C. Specifically, it is used for steam heating of various reaction kettles used for polymerization reaction, food distilling devices, concentrating devices, sterilizing devices, and the like. The object to be heated in these cases is
In most cases, a slight temperature rise causes thermal damage, 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は例えば図2に示す
ようなものが用いられていた。これは、熱交換器1を加
熱するもので、熱交換器1に加熱用の蒸気供給管2を接
続すると共に、加熱により生じた復水を排出する立下げ
部3とスチ―ムトラップ4とで復水排出装置5を構成し
たもので、蒸気供給管2から比較的低圧力すなわち低温
度の蒸気を熱交換器1へ供給することにより、熱交換器
1内の被加熱物を加熱するものである。熱交換器1内へ
供給された蒸気が加熱により凝縮して熱交換器1内を大
気圧以下程度の低圧力状態に維持することにより、10
0度Cあるいは100度C以下の比較的低温度で蒸気加
熱することができるものである。
2. Description of the Related Art For example, a conventional steam heating device as shown in FIG. 2 has been used. This heats the heat exchanger 1. The steam supply pipe 2 for heating is connected to the heat exchanger 1, and the falling portion 3 and the steam trap 4 for discharging the condensate generated by the heating are used. The condensate discharge device 5 is configured to heat the object to be heated in the heat exchanger 1 by supplying the steam having a relatively low pressure, that is, a low temperature, from the steam supply pipe 2 to the heat exchanger 1. is there. The steam supplied to the inside of the heat exchanger 1 is condensed by heating to maintain the inside of the heat exchanger 1 at a low pressure below atmospheric pressure.
Steam heating can be performed at a relatively low temperature of 0 ° C. or 100 ° C. or less.

【0003】[0003]

【発明が解決しようとする課題】上記従来の蒸気加熱装
置では、加熱用の蒸気に混入している不凝縮ガス例えば
空気等を熱交換器内から排除することができずに、加熱
温度ムラを生じて加熱温度を精度良く維持することがで
きない問題があった。
In the above-described conventional steam heating device, the non-condensable gas such as air mixed in the steam for heating cannot be removed from the heat exchanger, resulting in uneven heating temperature. There was a problem that the heating temperature could not be maintained with high accuracy.

【0004】加熱用の蒸気は少なからず幾らかの空気を
混入しているのであるが、上記従来の蒸気加熱装置で
は、復水排出装置5を立下げ部3とスチ―ムトラップ4
とで構成しているために、復水は立下げ部3に溜った水
頭圧によりスチ―ムトラップ4を通過して排出されるの
であるが、空気等の不凝縮ガスは立下げ部3に溜ること
がなく器外へ排除されないのである。
The heating steam contains some air, but not a little, but in the conventional steam heating apparatus described above, the condensate discharge device 5 is placed in the falling portion 3 and the steam trap 4.
Therefore, the condensate is discharged through the steam trap 4 by the water head pressure accumulated in the falling portion 3, but the non-condensable gas such as air is accumulated in the falling portion 3. There is no such thing and it is not excluded from the outside.

【0005】従って本発明の技術的課題は、熱交換器内
に混入した空気等の不凝縮ガスを排除することができ、
加熱温度を精度良く維持することのできる蒸気加熱装置
を提供することである。
Therefore, the technical problem of the present invention is to eliminate non-condensable gas such as air mixed in the heat exchanger,
An object of the present invention is to provide a steam heating device capable of maintaining a heating temperature with high accuracy.

【0006】[0006]

【課題を解決するための手段】上記の技術的課題を解決
するために講じた本発明の技術的手段は、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すると共に、
加熱により生じた復水を排出する復水排出装置を接続し
たものにおいて、復水排出装置に復水溜部を接続して、
当該復水溜部に所望の長さを有する立下がり部を介して
レシ―バ―を接続すると共に、当該レシ―バ―と復水溜
部とを循環ポンプを介して連通したものである。
The technical means of the present invention taken to solve the above technical problems is to form a heating part in a heat exchanger to connect a steam supply pipe for heating, and
In the case where a condensate discharge device for discharging condensed water generated by heating is connected, a condensate reservoir is connected to the condensate discharge device,
A receiver is connected to the condensate reservoir via a falling part having a desired length, and the receiver and the condensate reservoir are connected via a circulation pump.

【0007】[0007]

【作用】上記の技術的手段の作用は下記の通りである。
熱交換器へ供給された加熱用の蒸気は被加熱物を加熱す
ることにより凝縮して復水となり復水溜部に至る。復水
溜部と立下がり部とレシ―バ―に溜った復水を循環ポン
プで強制的に再度復水溜部へ循環させることにより、復
水溜部に流下してきた空気等の不凝縮ガスは復水の循環
流に混入してレシ―バ―に至る。
The operation of the above technical means is as follows.
The heating steam supplied to the heat exchanger condenses by heating the object to be heated and becomes condensed water, which reaches the condensed water reservoir. Non-condensable gas such as air that has flowed down to the condensate reservoir is condensed by forcibly circulating the condensate collected in the condensate reservoir, the falling part and the receiver to the condensate reservoir again. It mixes with the circulation flow of the water and reaches the receiver.

【0008】レシ―バ―内の不凝縮ガスは、ガスの発生
量が少ない場合はレシ―バ―内に溜め置き、加熱工程が
完了後に手動で外部に排除したり、あるいは、不凝縮ガ
スの存在をフロ―ト等で検知して弁口から不凝縮ガスだ
けを自動的に排出するエア―ベント等をレシ―バ―に取
り付けることにより外部に排除することができる。
The non-condensable gas in the receiver is stored in the receiver when the amount of gas generated is small, and is manually removed to the outside after the heating process is completed, or the non-condensed gas is discharged. It can be excluded to the outside by installing an air vent or the like, which detects the presence by a float or the like and automatically discharges only the non-condensable gas from the valve port, to the receiver.

【0009】[0009]

【実施例】上記の技術的手段の具体例を示す実施例を図
1に基き説明する。本実施例において従来技術と同一部
材には同一符号を付す。蒸気加熱装置としての熱交換器
1に蒸気供給管2を圧力調整弁6を介して接続する。熱
交換器1の下部には復水排出装置としてのスチ―ムトラ
ップ4を取り付ける。スチ―ムトラップ4の下部に復水
溜部7を接続する。復水溜部7は断面円筒状でその側部
に所定の長さを有する立下がり部8を取り付ける。立下
がり部8の上部には開閉弁9を取り付けると共に、その
下端10をレシ―バ―11内に開口して配置する。レシ
―バ―11も円筒状のタンクとして上部にエア―ベント
12と開閉弁13を取り付け、下部には水を補給するた
めの補給水管14を接続すると共に、循環ポンプ15の
吸込口16を接続する。循環ポンプ15の吐出口17は
管路18を介して復水溜部7の下端と接続する。
EXAMPLE An example showing a concrete example of the above technical means will be described with reference to FIG. In this embodiment, the same members as those in the conventional technique are designated by the same reference numerals. A steam supply pipe 2 is connected to a heat exchanger 1 as a steam heating device via a pressure adjusting valve 6. A steam trap 4 as a condensate discharge device is attached to the lower part of the heat exchanger 1. A condensate reservoir 7 is connected to the bottom of the steam trap 4. The condensate reservoir portion 7 has a cylindrical cross section, and a falling portion 8 having a predetermined length is attached to the side portion thereof. An opening / closing valve 9 is attached to the upper portion of the falling portion 8 and a lower end 10 thereof is opened in the receiver 11. The receiver 11 is also a cylindrical tank with an air vent 12 and an opening / closing valve 13 attached to the upper part, a makeup water pipe 14 for replenishing water is connected to the lower part, and a suction port 16 of a circulation pump 15 is connected. To do. The outlet 17 of the circulation pump 15 is connected to the lower end of the condensate reservoir 7 via a pipe line 18.

【0010】復水溜部7の上部には管路20と開閉弁2
1を取り付ける。開閉弁21を開弁状態とすることによ
り復水溜部7内を大気と連通状態とし、閉弁状態とする
ことにより大気と遮断状態とするものである。
A conduit 20 and an on-off valve 2 are provided above the condensate reservoir 7.
Attach 1. The open / close valve 21 is opened to bring the inside of the condensate reservoir portion 7 into communication with the atmosphere, and the valve closed state is cut off from the atmosphere.

【0011】立下がり部8の長さは、復水溜部7内の圧
力が熱交換器1内で必要とする圧力よりもわずかに低く
なるように設定することができる。例えば、熱交換器1
内で360ミリメ―トル水銀柱の圧力が必要である場
合、復水溜部7内の圧力は復水等が流下するためにはそ
れより低い値でなければならず、例えば、290ミリメ
―トル水銀柱であるとすると、立下がり部8の長さは、
760−290=470ミリメ―トル水銀柱以上即ち
6.4メ―トル以上は必要となり、通常10メ―トル程
度の長さとするのが望ましい。
The length of the falling portion 8 can be set so that the pressure in the condensate reservoir 7 is slightly lower than the pressure required in the heat exchanger 1. For example, heat exchanger 1
In the case where the pressure of 360 mm mercury column is required, the pressure in the condensate reservoir part 7 must be a lower value for condensate to flow down. For example, in the case of 290 mm mercury column. If there is, the length of the falling portion 8 is
760-290 = 470 millimeters Mercury column or more, that is, 6.4 meters or more is required, and it is usually desirable to set the length to about 10 meters.

【0012】次に作用を説明する。熱交換器1で加熱を
行う前に復水溜部7内の残存空気を除去しておく必要が
ある場合は、まず開閉弁21を開弁状態として、循環ポ
ンプ15を駆動してレシ―バ―11内の水を復水溜部7
に供給し、開閉弁21から残存空気を除去した後開閉弁
21を閉弁状態にし水がレシ―バ―11内へ自重で流下
することにより、復水溜部7の上部に所定の真空圧力域
を形成してから加熱を行う。加熱の前に残存空気の除去
が必要でない場合は上記操作は必要無い。
Next, the operation will be described. If it is necessary to remove the residual air in the condensate reservoir 7 before heating with the heat exchanger 1, first the open / close valve 21 is opened and the circulation pump 15 is driven to receive the receiver. Condensate reservoir 7
After the residual air is removed from the on-off valve 21, the on-off valve 21 is closed and the water flows down into the receiver 11 by its own weight, so that a predetermined vacuum pressure range is provided above the condensate reservoir 7. Is formed and then heated. If it is not necessary to remove residual air before heating, the above operation is not necessary.

【0013】蒸気供給管2から圧力調整弁6を経て供給
された低圧の加熱用蒸気は、熱交換器1内で図示しない
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4から復水溜部7内へ流下する。復水溜
部7内に溜った復水は循環ポンプ15から供給されたレ
シ―バ―11内の循環流体の一部と共に立下がり部8を
流下してレシ―バ―11内へ至る。この場合、加熱用の
蒸気に混入してきた空気等の不凝縮ガスは、復水と共に
復水溜部7内に至り、循環流体に巻込まれて立下がり部
を流下してレシ―バ―11の上部に溜り、エア―ベント
12または開閉弁13を経て外部に排除される。
The low-pressure heating steam supplied from the steam supply pipe 2 through the pressure regulating valve 6 is condensed in the heat exchanger 1 by heating an object to be heated (not shown) to be condensed water, and the steam trap is formed. From 4 to the condensate reservoir 7. Condensed water accumulated in the condensate reservoir 7 flows down the falling portion 8 together with a part of the circulating fluid in the receiver 11 supplied from the circulation pump 15 and reaches the inside of the receiver 11. In this case, the non-condensable gas such as air that has been mixed in the steam for heating reaches the inside of the condensate reservoir 7 together with the condensate, is entrained by the circulating fluid and flows down the falling part, and the upper part of the receiver 11 is reached. And is discharged to the outside through the air vent 12 or the open / close valve 13.

【0014】レシ―バ―11内の復水の量が所定以上に
達すると図示しない排出管から外部へ排出したり、循環
ポンプ15の吐出口17を分岐した同じく図示しない分
岐管から外部へ排出する。また、循環流体の温度が所定
以上に達して循環ポンプ15に悪影響を及ぼす可能性が
生じた場合は、補給水管14から冷却水を供給して所望
温度とすることができる。
When the amount of condensed water in the receiver 11 reaches a predetermined amount or more, it is discharged to the outside from a discharge pipe (not shown) or to the outside from a branch pipe (not shown) that branches the discharge port 17 of the circulation pump 15. To do. Further, when the temperature of the circulating fluid reaches a predetermined temperature or higher and may adversely affect the circulation pump 15, cooling water can be supplied from the makeup water pipe 14 to reach the desired temperature.

【0015】[0015]

【発明の効果】上記のように本発明によれば、熱交換器
に復水溜部と立下がり部とレシ―バ―と循環ポンプを順
次接続して復水溜部の復水を強制的に循環することによ
り、復水と共に空気等の不凝縮ガスもレシ―バ―まで流
下させることができ、従って、熱交換器内の不凝縮ガス
を循環流で排除して、熱交換器内で加熱ムラを生じるこ
とがない。
As described above, according to the present invention, the condensate reservoir, the falling portion, the receiver and the circulation pump are sequentially connected to the heat exchanger to forcibly circulate the condensate in the condensate reservoir. By doing so, the non-condensable gas such as air can be made to flow down to the receiver together with the condensate. Therefore, the non-condensable gas in the heat exchanger is eliminated by the circulation flow, and the heating unevenness in the heat exchanger is eliminated. Does not occur.

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

【図1】本発明の蒸気加熱装置の実施例の構成図であ
る。
FIG. 1 is a configuration diagram of an embodiment of a steam heating device of the present invention.

【図2】蒸気加熱装置の従来例を示す構成図である。FIG. 2 is a configuration diagram showing a conventional example of a steam heating device.

【符号の説明】[Explanation of symbols]

1 熱交換器 2 蒸気供給管 4 スチ―ムトラップ 7 復水溜部 8 立下がり部 11 レシ―バ― 15 循環ポンプ 1 Heat Exchanger 2 Steam Supply Pipe 4 Steam Trap 7 Condensate Reservoir 8 Falling Part 11 Reciever 15 Circulation Pump

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
気供給管を接続すると共に、加熱により生じた復水を排
出する復水排出装置を接続したものにおいて、復水排出
装置に復水溜部を接続して、当該復水溜部に所望の長さ
を有する立下がり部を介してレシ―バ―を接続すると共
に、当該レシ―バ―と復水溜部とを循環ポンプを介して
連通したことを特徴とする蒸気加熱装置。
1. A condensate discharge device in which a heating part is formed in a heat exchanger, a steam supply pipe for heating is connected, and a condensate discharge device for discharging condensed water generated by heating is connected. Connect the condensate reservoir, connect the receiver to the condensate reservoir via a falling part having a desired length, and connect the receiver and the condensate reservoir via a circulation pump. A steam heating device characterized by communication.
JP33393994A 1994-12-15 1994-12-15 Steam heating device Expired - Fee Related JP3282004B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33393994A JP3282004B2 (en) 1994-12-15 1994-12-15 Steam heating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33393994A JP3282004B2 (en) 1994-12-15 1994-12-15 Steam heating device

Publications (2)

Publication Number Publication Date
JPH08170885A true JPH08170885A (en) 1996-07-02
JP3282004B2 JP3282004B2 (en) 2002-05-13

Family

ID=18271671

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33393994A Expired - Fee Related JP3282004B2 (en) 1994-12-15 1994-12-15 Steam heating device

Country Status (1)

Country Link
JP (1) JP3282004B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003078904A1 (en) * 2002-03-19 2003-09-25 Takahiro Agata Heat exchange structure body for atmospheric pressure steam and heat exchange method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003078904A1 (en) * 2002-03-19 2003-09-25 Takahiro Agata Heat exchange structure body for atmospheric pressure steam and heat exchange method

Also Published As

Publication number Publication date
JP3282004B2 (en) 2002-05-13

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