JPH10325697A - Capacity regulator for heat exchanger - Google Patents
Capacity regulator for heat exchangerInfo
- Publication number
- JPH10325697A JPH10325697A JP13311997A JP13311997A JPH10325697A JP H10325697 A JPH10325697 A JP H10325697A JP 13311997 A JP13311997 A JP 13311997A JP 13311997 A JP13311997 A JP 13311997A JP H10325697 A JPH10325697 A JP H10325697A
- Authority
- JP
- Japan
- Prior art keywords
- heat exchanger
- water
- water tank
- steam
- drain
- 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
Links
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、水蒸気を加熱源と
する熱交換器の容量調整装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for adjusting the capacity of a heat exchanger using steam as a heating source.
【0002】[0002]
【従来の技術】図3は、化学プラント、発電プラント、
大型の冷凍機等において、水蒸気を加熱源とする熱交換
器として広く用いられているシェル・アンド・チューブ
熱交換器の構成図である。この図において、1は耐圧容
器を構成するシェル、2は伝熱管(チューブ)、3はバ
ッフル、4はヘッダである。水蒸気を用いた加熱器とし
て用いる場合には、図に例示するように、通常、チュー
ブ2の内側に被加熱流体5を流し、シェル1内に水蒸気
6を供給する。また、逆にチューブ内に水蒸気6を流
し、シェル内に被加熱流体5を流す場合もある。なお、
この図で6bはドレントラップであり、凝縮水(ドレ
ン)を排水するようになっている。また、このドレント
ラップに替えて調整弁を使用することもある。2. Description of the Related Art FIG. 3 shows a chemical plant, a power plant,
1 is a configuration diagram of a shell and tube heat exchanger widely used as a heat exchanger using steam as a heating source in a large refrigerator or the like. In this figure, 1 is a shell constituting a pressure-resistant container, 2 is a heat transfer tube (tube), 3 is a baffle, and 4 is a header. When used as a heater using steam, the fluid to be heated 5 is usually flowed inside the tube 2 and steam 6 is supplied into the shell 1 as illustrated in the figure. Conversely, in some cases, steam 6 may flow in the tube and fluid 5 to be heated may flow in the shell. In addition,
In this figure, reference numeral 6b denotes a drain trap which drains condensed water (drain). Further, a regulating valve may be used instead of the drain trap.
【0003】[0003]
【発明が解決しようとする課題】上述した水蒸気を加熱
源とする熱交換器では、図3に例示するように水蒸気供
給ラインに流量調節弁7を備え、被加熱流体5の温度を
温度センサ8で検出し、この温度が所定範囲に入るよう
に流量調節弁7を調節する。この場合、熱交換器におけ
る伝熱量Qは、熱交換器の伝熱基本式(Q=UAΔT)
であらわされる。ここで、Uは熱通過率、Aは伝熱面
積、ΔTはチューブ内外の温度差である。In the heat exchanger using steam as a heating source, the steam supply line is provided with a flow rate control valve 7 as shown in FIG. And the flow control valve 7 is adjusted so that the temperature falls within a predetermined range. In this case, the heat transfer amount Q in the heat exchanger is represented by the heat transfer basic formula (Q = UAΔT) of the heat exchanger.
It is represented by Here, U is the heat transmission coefficient, A is the heat transfer area, and ΔT is the temperature difference between the inside and outside of the tube.
【0004】しかし、かかる熱交換器において、負荷減
少時に伝熱量(負荷)を小さくするために、流量調節弁
7を絞り、供給水蒸気量を小さくしても、熱通過率Uの
蒸気圧力による変化は小さく、蒸気温度もあまり変化し
ないため温度差ΔTの変化も少ない。そのため、流量調
節弁7を絞っても、ドレントラップ6bが閉じて内部に
ドレンが溜まり、伝熱面積Aが小さくなるまで、伝熱量
が小さくならない問題点があった。However, in such a heat exchanger, even if the flow control valve 7 is throttled to reduce the heat transfer amount (load) when the load is reduced and the amount of supplied steam is reduced, the change in the heat transfer rate U due to the steam pressure is reduced. Is small and the temperature difference ΔT does not change much because the steam temperature does not change much. For this reason, even if the flow control valve 7 is throttled, there is a problem that the amount of heat transfer does not decrease until the drain trap 6b closes and the drain accumulates inside and the heat transfer area A decreases.
【0005】そのため、従来の熱交換器では、その負荷
を減じてゆくとき、例えば、ドレンが溜まるまで30分
〜1時間以上もかかることがあり、その間被加熱側が過
熱されてしまい、負荷低減時の制御性が極めて悪い問題
点があった。また、負荷低減のために流量調節弁7を完
全に全閉にしてしまうと、残留した水蒸気の凝縮に伴い
内部が負圧化し、外気から空気が侵入し、熱交換器の機
能を阻害するおそれがあった。[0005] Therefore, in the conventional heat exchanger, when the load is reduced, for example, it may take 30 minutes to 1 hour or more until the drain accumulates, during which time the heated side is overheated and the load is reduced. There is a problem that the controllability of the device is extremely poor. Further, if the flow control valve 7 is completely closed to reduce the load, the inside becomes negative pressure due to the condensation of the remaining water vapor, and air may enter from the outside air and hinder the function of the heat exchanger. was there.
【0006】本発明はかかる問題点を解決するために創
案されたものである。すなわち、本発明の目的は、内部
に負圧を発生させることなく水蒸気を加熱源とする熱交
換器の負荷低減時の応答性を大幅に高めることができる
容量調整装置を提供することにある。The present invention has been made to solve such a problem. That is, an object of the present invention is to provide a capacity adjusting device capable of greatly increasing the responsiveness of a heat exchanger using steam as a heating source when the load is reduced without generating a negative pressure inside.
【0007】[0007]
【課題を解決するための手段】上述した水蒸気を加熱源
とするこの種の熱交換器では、低負荷への対応は、ドレ
ンによって伝熱面積を制御する手段が最も効果的であ
り、この手段を迅速に行うことがポイントである。本発
明はかかる新規の着想に基づくものである。In this type of heat exchanger using steam as a heating source, the means for controlling the heat transfer area by drain is the most effective in responding to a low load. The point is to do it quickly. The present invention is based on such a new idea.
【0008】すなわち、第1の本発明によれば、水蒸気
を加熱源とする伝熱面をもった熱交換器の水蒸気室容量
よりも大きい保有水量を有する水タンクと、水蒸気室下
部と水タンク下部を連通するドレン配管と、水タンクの
所定のレベルからの溢流水を排水する排水ラインとを備
え、前記水タンクの設置高さは、定格水蒸気圧力におい
て熱交換器内の水位が伝熱面より低くなるように設定さ
れている、ことを特徴とする熱交換器の容量調整装置が
提供される。That is, according to the first aspect of the present invention, a water tank having a larger amount of water than a steam chamber capacity of a heat exchanger having a heat transfer surface using steam as a heating source, a lower portion of the steam chamber, and a water tank It has a drain pipe communicating with the lower part, and a drain line for draining overflow water from a predetermined level in the water tank, and the installation height of the water tank is such that the water level in the heat exchanger at the rated steam pressure is a heat transfer surface. There is provided a heat exchanger capacity adjusting device, which is set to be lower.
【0009】この第1の発明は、加圧水蒸気圧力が低い
場合に特に適している。すなわち上記本発明の構成によ
れば、熱交換器のドレンの排水側を高く配置し、かつそ
こに十分な保有量を有する水タンクを設置し、定格水蒸
気圧力において熱交換器内の水位が伝熱面より低くなる
ように設定されているので、定格負荷時には定格水蒸気
圧力により熱交換器内の水位が十分低く、全伝熱面積を
そのまま有効に活用することができる。The first invention is particularly suitable when the pressure of the pressurized steam is low. That is, according to the configuration of the present invention, the drain side of the drain of the heat exchanger is arranged at a high position, and a water tank having a sufficient storage amount is installed therein, and the water level in the heat exchanger is transmitted at the rated steam pressure. Since it is set to be lower than the hot surface, the water level in the heat exchanger is sufficiently low due to the rated steam pressure at the rated load, and the entire heat transfer area can be effectively used as it is.
【0010】また、負荷減少時には加熱用水蒸気流量が
絞られ凝縮圧力が低下するので、水タンク内の水圧によ
り水を逆に熱交換器に送り込んで伝熱面積を小さくする
ことができる。この際、水タンクの水位は十分高いた
め、この差圧によって自動的に水が熱交換器側に送り込
まれ、負荷に見合った伝熱面積となる水位でバランスす
る。水配管(ドレン配管)を十分な太さにしておけば、
流れ抵抗は低く水は速やかに移動するため負荷低減時の
応答性を大幅に高め、応答遅れは無視できるほど小さく
できる。In addition, when the load is reduced, the flow rate of the steam for heating is reduced and the condensing pressure is reduced. Therefore, water can be sent to the heat exchanger in reverse by the water pressure in the water tank to reduce the heat transfer area. At this time, since the water level in the water tank is sufficiently high, water is automatically sent to the heat exchanger side by this differential pressure, and the water level is balanced with a heat transfer area corresponding to the load. If the water pipe (drain pipe) is made thick enough,
Since the flow resistance is low and the water moves quickly, the responsiveness at the time of load reduction is greatly enhanced, and the response delay can be made negligibly small.
【0011】更に、水蒸気の凝縮により水量が増加した
場合には、水タンクの所定のレベルから排水ラインを介
して溢流水を排水することができ、内部の保有水水量を
一定の範囲に自動的に調節することができる。従って、
背圧を一定範囲内に維持でき、凝縮圧力をほぼ一定に保
持できる。特に、この容量調整装置では、負荷減少に伴
う凝縮圧力の低下が応じて水が送り込まれるため、特別
な制御装置は不要であり、高い信頼性を得ることができ
る。Further, when the amount of water increases due to the condensation of water vapor, overflow water can be drained from a predetermined level in the water tank through a drain line, and the amount of water retained inside is automatically adjusted to a certain range. Can be adjusted. Therefore,
The back pressure can be maintained within a certain range, and the condensing pressure can be kept almost constant. In particular, in this capacity adjusting device, since water is fed in accordance with a decrease in condensing pressure due to a decrease in load, a special control device is not required, and high reliability can be obtained.
【0012】また第2の本発明によれば、水蒸気を加熱
源とする伝熱面をもった熱交換器の水蒸気室容量よりも
大きい保有水量を有する水タンクと、水蒸気室下部と水
タンク下部を連通するドレン配管と、ドレン配管から排
水する排水ラインとを備え、前記水タンクはガスで加圧
された気密タンクであり、該内部圧は、熱交換器の定格
水蒸気圧力において熱交換器内の水位が伝熱面より低く
なるように設定されている、ことを特徴とする熱交換器
の容量調整装置が提供される。本発明の好ましい実施形
態によれば、水タンク内の水位を検出する水位センサ
と、排水ラインを開閉する排水弁とを備え、水位センサ
により排水弁を操作して水タンク内の水位を所定の範囲
に調節するようになっている。According to the second aspect of the present invention, there is provided a water tank having a larger water holding capacity than a steam chamber capacity of a heat exchanger having a heat transfer surface using steam as a heating source, a lower steam chamber section and a lower water tank section. And a drain line for draining from the drain pipe, wherein the water tank is an airtight tank pressurized with gas, and the internal pressure of the heat exchanger at the rated steam pressure of the heat exchanger. Wherein the water level is set lower than the heat transfer surface. According to a preferred embodiment of the present invention, a water level sensor for detecting a water level in a water tank and a drain valve for opening and closing a drain line are provided, and the water level sensor operates the drain valve to set the water level in the water tank to a predetermined level. Adjusts to the range.
【0013】第2の発明は、加圧水蒸気の圧力(及び温
度)が高い場合に、特に適している。この発明では、水
タンクがガスで加圧された気密タンクであり、その内部
圧が、熱交換器の定格水蒸気圧力において熱交換器内の
水位が伝熱面より低くなるように設定されているので、
加圧水蒸気の圧力が例えば10atg以上の場合でも、
水タンクを低い位置に設置したままで、第1の発明と同
様に機能することができる。すなわち負荷が減少すれ
ば、凝縮圧力が下がり、水タンクから水が送り込まれて
伝熱面積が制御されると共に、水タンク液位も低下する
ことによってドレン排水弁も閉じる。負荷が増大すれば
水位が上昇して排水弁が開き、ドレンを排水する。従っ
て、水タンクの内部圧を定格水蒸気圧力に応じて一定に
保持するだけで、特別な制御装置は不要であり、高い信
頼性を得ることができる。またドレンの排水を、簡単な
水タンクの液位制御で行うことができ、保有水を適正範
囲に調節することができる。The second invention is particularly suitable when the pressure (and temperature) of the pressurized steam is high. In the present invention, the water tank is an airtight tank pressurized with gas, and the internal pressure thereof is set so that the water level in the heat exchanger is lower than the heat transfer surface at the rated steam pressure of the heat exchanger. So
Even when the pressure of the pressurized steam is, for example, 10 atg or more,
With the water tank installed at a low position, it can function similarly to the first invention. That is, when the load is reduced, the condensing pressure is lowered, water is fed from the water tank to control the heat transfer area, and the drain tank valve is closed by the water tank liquid level dropping. If the load increases, the water level rises and the drain valve opens to drain the drain. Therefore, only maintaining the internal pressure of the water tank constant according to the rated steam pressure does not require a special control device, and high reliability can be obtained. In addition, drainage can be performed by simple liquid level control of the water tank, and the retained water can be adjusted to an appropriate range.
【0014】従って、第1及び第2の発明により、被加
熱流体の過熱や、凝縮圧力の負圧化も発生せず、低負荷
(理論的には0%)まで安定した運転状態が得られ、熱
交換器の負荷低減時の応答性を大幅に高めることができ
る。Therefore, according to the first and second aspects of the present invention, overheating of the fluid to be heated and negative pressure of the condensing pressure do not occur, and a stable operating state up to a low load (theoretical 0%) can be obtained. In addition, the responsiveness of the heat exchanger when the load is reduced can be greatly increased.
【0015】[0015]
【発明の実施の形態】以下、図面に基づいて、本発明の
一実施形態を説明する。なお、各図において共通する部
分には同一の符号を付し説明の重複を省略する。図1
は、本発明の第1実施形態を示す熱交換器の容量調整装
置の構成図である。この図において、熱交換器10は、
シェル1内を通る伝熱管(チューブ)2を有し、チュー
ブ2の内側に被加熱流体5を流し、シェル1内に蒸気ラ
イン6aを介して水蒸気6を供給して被加熱流体5を加
熱するようになっている。従って、伝熱管2が伝熱面で
あり、シェル1の一部が水蒸気室10aとなる。また、
蒸気ライン6aには流量調節弁11が設けられており、
被加熱流体5の温度を検出する温度センサ12の出力が
設定温度になるように、流量調節弁11を調節するよう
になっている。また、13は負荷を調整するための流量
調節弁である。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. In the drawings, common portions are denoted by the same reference numerals, and redundant description is omitted. FIG.
1 is a configuration diagram of a heat exchanger capacity adjusting device according to a first embodiment of the present invention. In this figure, the heat exchanger 10
It has a heat transfer tube (tube) 2 that passes through the inside of the shell 1, flows the fluid to be heated 5 inside the tube 2, and supplies steam 6 into the shell 1 via a steam line 6 a to heat the fluid 5 to be heated. It has become. Therefore, the heat transfer tube 2 is a heat transfer surface, and a part of the shell 1 is a steam chamber 10a. Also,
The steam line 6a is provided with a flow control valve 11,
The flow rate control valve 11 is adjusted so that the output of the temperature sensor 12 for detecting the temperature of the fluid 5 to be heated becomes the set temperature. Reference numeral 13 denotes a flow control valve for adjusting a load.
【0016】なお、熱交換器10は、シェル・アンド・
チューブ熱交換器であるのが好ましいが、本発明はこれ
に限定されず、水蒸気を加熱源とする伝熱面をもった間
接加熱方式である限りで、その他の形式の熱交換器であ
ってもよい。また、熱交換器10内には通常のシェル・
アンド・チューブ熱交換器と相違しバッフルがないか、
ある場合でも通気孔を有し、内部に溜まったドレン水が
バッフルを通して自由に連通するようになっているのが
よい。更に、この図では横型の熱交換器を示している
が、縦型であってもよい。Note that the heat exchanger 10 is a shell and
Although a tube heat exchanger is preferable, the present invention is not limited to this, and other types of heat exchangers may be used as long as they are indirect heating systems having a heat transfer surface using steam as a heating source. Is also good. In the heat exchanger 10, a normal shell
Whether there is no baffle unlike the and tube heat exchanger,
Even in some cases, it is preferable that a vent hole is provided so that drain water accumulated inside can freely communicate through the baffle. Further, although this figure shows a horizontal heat exchanger, it may be a vertical heat exchanger.
【0017】図1において、本発明の容量調整装置14
は、水タンク15、ドレン配管16及び排水ライン17
を備えている。水タンク15は、熱交換器10の水蒸気
室10aの容量よりも大きい保有水量を有し、かつ図に
示すように高い位置に設置されている。ドレン配管16
は、水蒸気室10aの下部と水タンク15の下部を連通
している。排水ライン17は、水タンク15の所定のレ
ベルからの溢流水を排水するようになっている。水タン
ク15は、上部が大気と連通し大気圧になるようになっ
ている。In FIG. 1, the capacity adjusting device 14 of the present invention is shown.
Is a water tank 15, a drain pipe 16 and a drain line 17
It has. The water tank 15 has a larger amount of water than the capacity of the steam chamber 10a of the heat exchanger 10, and is installed at a high position as shown in the figure. Drain piping 16
Communicates the lower part of the water vapor chamber 10a and the lower part of the water tank 15. The drain line 17 drains overflow water from a predetermined level in the water tank 15. The upper part of the water tank 15 communicates with the atmosphere so that the water tank 15 is at atmospheric pressure.
【0018】更に、水タンク15の設置高さHは、熱交
換器10の定格水蒸気圧力において熱交換器内の水位が
伝熱面より低くなるように設定されている。すなわち、
熱交換器10内の水位9が水蒸気室10aの下部より低
くなるレベル(図に0で示す)から、水タンク15から
水が溢流するレベルまでのヘッド差Hmが、熱交換器1
0の定格水蒸気圧力Pにほぼ一致するように設定されて
いる。Further, the installation height H of the water tank 15 is set such that the water level in the heat exchanger is lower than the heat transfer surface at the rated steam pressure of the heat exchanger 10. That is,
The head difference Hm from the level at which the water level 9 in the heat exchanger 10 is lower than the lower part of the steam chamber 10a (shown by 0 in the figure) to the level at which water overflows from the water tank 15 is the heat exchanger 1
It is set so as to substantially match the rated steam pressure P of 0.
【0019】従って、定格水蒸気圧力Pが例えば0.5
kg/cm2 g(すなわち0.5atg)の場合には、
ヘッド差Hを約5mに設定し、1atgの場合には約1
0mに設定する。なお、この第1実施形態の容量調整装
置は、加圧水蒸気圧力が低い場合に特に適しており、加
圧水蒸気圧力が高い場合には、後述する第2実施形態を
用いるのが好ましい。Therefore, the rated steam pressure P is, for example, 0.5
kg / cm 2 g (ie 0.5 atg)
The head difference H is set to about 5 m, and in the case of 1 atg, about 1
Set to 0m. The capacity adjusting device of the first embodiment is particularly suitable when the pressure of the pressurized steam is low, and when the pressure of the pressurized steam is high, it is preferable to use the second embodiment described later.
【0020】上述した本発明の構成によれば、熱交換器
10のドレンの排水側を高く配置し、かつそこに十分な
保有量を有する水タンク15を設置し、定格水蒸気圧力
Pにおいて熱交換器10内の水位が伝熱面より低くなる
ように設定されているので、定格負荷時には定格水蒸気
圧力Pにより熱交換器10内の水位が十分低く、伝熱面
積Aをそのまま有効に活用することができる。According to the configuration of the present invention described above, the drain side of the drain of the heat exchanger 10 is arranged high, and the water tank 15 having a sufficient amount is installed therein. Since the water level in the heat exchanger 10 is set to be lower than the heat transfer surface, the water level in the heat exchanger 10 is sufficiently low at the rated load due to the rated steam pressure P, and the heat transfer area A is effectively used as it is. Can be.
【0021】また、負荷減少時には流量調節弁11によ
り加熱用水蒸気流量が絞られ凝縮圧力が低下するので、
水タンク15内の水圧により水を逆に熱交換器に送り込
んで伝熱面積Aを小さくすることができる。この際、水
タンク15の水位は十分高いため、この差圧Hによって
自動的に水が熱交換器10側に送り込まれ、負荷に見合
った伝熱面積Aとなる水位でバランスする。水配管(ド
レン配管16)は抵抗の少ない十分な太さにしておくの
が好ましく、これにより、水は速やかに移動するため負
荷低減時の応答性を大幅に高め、応答遅れは無視できる
ほど小さくできる。When the load is reduced, the flow rate of the steam for heating is reduced by the flow rate control valve 11 and the condensing pressure is reduced.
Conversely, water can be sent to the heat exchanger by the water pressure in the water tank 15 to reduce the heat transfer area A. At this time, since the water level in the water tank 15 is sufficiently high, the water is automatically sent to the heat exchanger 10 side by the differential pressure H, and the water level is balanced with the heat transfer area A corresponding to the load. It is preferable that the water pipe (the drain pipe 16) be sufficiently thick with a small resistance, so that the water moves quickly, so that the response at the time of load reduction is greatly enhanced, and the response delay is negligibly small. it can.
【0022】更に、水蒸気の凝縮により水量が増加した
場合には、水タンク15の所定のレベルから排水ライン
17を介して溢流水を排水することができ、内部の保有
水水位を一定の範囲に自動的に調節することができる。
また特に、この容量調整装置14では、負荷減少に伴う
凝縮圧力の低下がもとで水が送り込まれるため、特別な
制御装置は不要であり、高い信頼性を得ることができ
る。Further, when the amount of water increases due to the condensation of water vapor, overflow water can be drained from a predetermined level in the water tank 15 through the drain line 17 so that the internal water level within the water tank 15 falls within a certain range. Can be adjusted automatically.
Further, in particular, in the capacity adjusting device 14, since water is sent in due to a decrease in condensing pressure due to a decrease in load, no special control device is required, and high reliability can be obtained.
【0023】図2は、本発明の第2実施形態を示す熱交
換器の容量調整装置の構成図である。この図において、
水タンク15は気密タンクであり、流量調節弁18aを
有するガスライン18から供給されるガスで一定圧力に
保持されるようになっている。このガスは、空気または
窒素ガスであるのがよい。また、排水ライン17は、ド
レン配管16から直接排水するようになっている。FIG. 2 is a configuration diagram of a heat exchanger capacity adjusting device according to a second embodiment of the present invention. In this figure,
The water tank 15 is an airtight tank, and is maintained at a constant pressure by gas supplied from a gas line 18 having a flow control valve 18a. This gas may be air or nitrogen gas. The drain line 17 drains directly from the drain pipe 16.
【0024】本発明の容量調整装置14は、更に、水タ
ンク15内の水位を検出する水位センサ19と、排水ラ
イン17を開閉する排水弁17aとを備え、水位センサ
19により排水弁17aを操作して水タンク15内の水
位を所定の範囲に調節するようになっている。更に、こ
の実施形態では、水タンク15内の圧力を検出する圧力
センサ20を備え、この圧力センサ20により内部圧を
検出し、この内部圧を、熱交換器10の定格水蒸気圧力
Pにおいて熱交換器10内の水位が水蒸気室10aの下
部より低くなるように設定するようになっている。その
他の構成は、図1と同様である。The capacity adjusting device 14 of the present invention further includes a water level sensor 19 for detecting the water level in the water tank 15 and a drain valve 17a for opening and closing the drain line 17. The drain valve 17a is operated by the water level sensor 19. Then, the water level in the water tank 15 is adjusted to a predetermined range. Further, in this embodiment, a pressure sensor 20 for detecting the pressure in the water tank 15 is provided, and the internal pressure is detected by the pressure sensor 20. The internal pressure is used for heat exchange at the rated steam pressure P of the heat exchanger 10. The water level in the vessel 10 is set to be lower than the lower part of the steam chamber 10a. Other configurations are the same as those in FIG.
【0025】図2の発明は、加圧水蒸気の圧力(及び温
度)が高い場合に、特に適している。上述した本発明の
構成によれば、水タンク15がガスで加圧された気密タ
ンクであり、その内部圧が、熱交換器10の定格水蒸気
圧力Pにおいて熱交換器内の水位が伝熱面より低くなる
ように設定されているので、加圧水蒸気の圧力が例えば
10atg以上の場合でも、水タンク15を低い位置に
設置したままで、第1の発明と同様に機能することがで
きる。すなわち負荷が減少すれば、凝縮圧力が下がり、
水タンク15から水が送り込まれて伝熱面積Aが制御さ
れると共に、水タンク液位も低下することによってドレ
ン排水弁17aも閉じる。負荷が増大すれば水位が上昇
して排水弁17aが開き、ドレンを排水する。従って、
水タンク15の内部圧を定格水蒸気圧力Pに応じて一定
に保持するだけで、特別な制御装置は不要であり、高い
信頼性を得ることができる。またドレンの排水を、簡単
な水タンクの液位制御で行うことができ、保有水を適正
範囲に調節することができる。The invention of FIG. 2 is particularly suitable when the pressure (and temperature) of the pressurized steam is high. According to the configuration of the present invention described above, the water tank 15 is an airtight tank pressurized with gas, and the internal pressure of the water tank 15 is equal to the water level in the heat exchanger at the rated steam pressure P of the heat exchanger 10. Since the pressure is set to be lower, even when the pressure of the pressurized steam is, for example, 10 atg or more, it is possible to function in the same manner as in the first aspect of the invention, with the water tank 15 installed at a low position. That is, if the load decreases, the condensation pressure decreases,
Water is supplied from the water tank 15 to control the heat transfer area A, and the drain tank 17 a is also closed by decreasing the water tank liquid level. If the load increases, the water level rises and the drain valve 17a opens to drain the drain. Therefore,
Only by keeping the internal pressure of the water tank 15 constant according to the rated steam pressure P, no special control device is required, and high reliability can be obtained. In addition, drainage can be performed by simple liquid level control of the water tank, and the retained water can be adjusted to an appropriate range.
【0026】なお、本発明は上述した実施形態に限定さ
れず、本発明の要旨を逸脱しない範囲で種々に変更でき
ることは勿論である。It should be noted that the present invention is not limited to the above-described embodiment, but can be variously modified without departing from the gist of the present invention.
【0027】[0027]
【発明の効果】上述したように、本発明の熱交換器の容
量調整装置は、被加熱流体の過熱や、凝縮圧力の負圧化
も発生せず、低負荷(理論的には0%)まで安定した運
転状態が得られ、熱交換器の負荷低減時の応答性を大幅
に高めることができる、等の優れた効果を有する。As described above, the capacity adjusting device for a heat exchanger according to the present invention does not cause overheating of the fluid to be heated or negative pressure of the condensing pressure, and has a low load (theoretical 0%). It has an excellent effect that a stable operating state can be obtained, and the responsiveness of the heat exchanger when the load is reduced can be greatly increased.
【図1】本発明の第1実施形態を示す容量調整装置の構
成図である。FIG. 1 is a configuration diagram of a capacity adjusting device according to a first embodiment of the present invention.
【図2】本発明の第2実施形態を示す容量調整装置の構
成図である。FIG. 2 is a configuration diagram of a capacity adjusting device according to a second embodiment of the present invention.
【図3】従来の熱交換器の構成図である。FIG. 3 is a configuration diagram of a conventional heat exchanger.
1 耐圧容器(シェル) 2 伝熱管(チューブ) 3 バッフル 4 ヘッダ 5 被加熱流体 6 水蒸気 6a 蒸気ライン 7 流量調節弁 8 温度センサ 9 水位 10 熱交換器 10a 水蒸気室 11 流量調節弁 12 温度センサ 13 流量調節弁 14 容量調整装置 15 水タンク 16 ドレン配管 17 排水ライン 17a 排水弁 18 ガスライン 18a 流量調節弁 19 水位センサ 20 圧力センサ DESCRIPTION OF SYMBOLS 1 Pressure-resistant container (shell) 2 Heat transfer tube (tube) 3 Baffle 4 Header 5 Heated fluid 6 Steam 6a Steam line 7 Flow control valve 8 Temperature sensor 9 Water level 10 Heat exchanger 10a Steam chamber 11 Flow control valve 12 Temperature sensor 13 Flow rate Control valve 14 Capacity adjusting device 15 Water tank 16 Drain pipe 17 Drain line 17a Drain valve 18 Gas line 18a Flow control valve 19 Water level sensor 20 Pressure sensor
Claims (3)
交換器の水蒸気室容量よりも大きい保有水量を有する水
タンクと、水蒸気室下部と水タンク下部を連通するドレ
ン配管と、水タンクの所定のレベルからの溢流水を排水
する排水ラインとを備え、 前記水タンクの設置高さは、定格水蒸気圧力において熱
交換器内の水位が伝熱面より低くなるように設定されて
いる、ことを特徴とする熱交換器の容量調整装置。1. A water tank having a larger water holding capacity than a steam chamber capacity of a heat exchanger having a heat transfer surface using steam as a heating source, a drain pipe communicating between a lower portion of the steam chamber and a lower portion of the water tank, and A drain line for draining overflow water from a predetermined level in the tank, and the installation height of the water tank is set such that the water level in the heat exchanger is lower than the heat transfer surface at the rated steam pressure. And a heat exchanger capacity adjusting device.
交換器の水蒸気室容量よりも大きい保有水量を有する水
タンクと、水蒸気室下部と水タンク下部を連通するドレ
ン配管と、ドレン配管から排水する排水ラインとを備
え、 前記水タンクはガスで加圧された気密タンクであり、該
内部圧は、熱交換器の定格水蒸気圧力において熱交換器
内の水位が伝熱面より低くなるように設定されている、
ことを特徴とする熱交換器の容量調整装置。2. A water tank having a larger water holding capacity than a steam chamber capacity of a heat exchanger having a heat transfer surface using steam as a heating source, a drain pipe communicating between a lower portion of the steam chamber and a lower portion of the water tank, and a drain. A drain line for draining from a pipe, wherein the water tank is an airtight tank pressurized with gas, and the internal pressure is such that the water level in the heat exchanger is lower than the heat transfer surface at the rated steam pressure of the heat exchanger. Is set to be
A capacity adjusting device for a heat exchanger.
と、排水ラインを開閉する排水弁とを備え、水位センサ
により排水弁を操作して水タンク内の水位を所定の範囲
に調節するようになっている、ことを特徴とする請求項
2に記載の熱交換器の容量調整装置。3. A water level sensor for detecting a water level in a water tank, and a drain valve for opening and closing a drain line, wherein the water level sensor operates the drain valve to adjust the water level in the water tank to a predetermined range. The capacity adjusting device for a heat exchanger according to claim 2, wherein:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13311997A JP3812054B2 (en) | 1997-05-23 | 1997-05-23 | Capacity adjustment device for heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13311997A JP3812054B2 (en) | 1997-05-23 | 1997-05-23 | Capacity adjustment device for heat exchanger |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH10325697A true JPH10325697A (en) | 1998-12-08 |
JP3812054B2 JP3812054B2 (en) | 2006-08-23 |
Family
ID=15097243
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Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13311997A Expired - Fee Related JP3812054B2 (en) | 1997-05-23 | 1997-05-23 | Capacity adjustment device for heat exchanger |
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JP (1) | JP3812054B2 (en) |
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JP2005061478A (en) * | 2003-08-08 | 2005-03-10 | Ishikawajima Plant Construction Co Ltd | Cryogenic liquid heating method and its device |
JP2007263475A (en) * | 2006-03-29 | 2007-10-11 | Ihi Corp | Gas cooler |
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1997
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Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
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JP2005061478A (en) * | 2003-08-08 | 2005-03-10 | Ishikawajima Plant Construction Co Ltd | Cryogenic liquid heating method and its device |
JP4540315B2 (en) * | 2003-08-08 | 2010-09-08 | Ihiプラント建設株式会社 | Cryogenic liquid heating method and apparatus |
JP2007263475A (en) * | 2006-03-29 | 2007-10-11 | Ihi Corp | Gas cooler |
JP2019178737A (en) * | 2018-03-30 | 2019-10-17 | 大阪瓦斯株式会社 | Liquefied natural gas vaporizer, and operation method of liquefied natural gas vaporizer |
CN109405090A (en) * | 2018-09-06 | 2019-03-01 | 珠海格力电器股份有限公司 | Device and method for removing haze by using air conditioner condensed water and air conditioner |
CN109405090B (en) * | 2018-09-06 | 2023-11-17 | 珠海格力电器股份有限公司 | Device and method for removing haze by utilizing air conditioner condensed water and air conditioner |
CN114352364A (en) * | 2021-07-22 | 2022-04-15 | 杭州绿能环保发电有限公司 | Main steam temperature control device |
CN114352364B (en) * | 2021-07-22 | 2023-11-21 | 杭州绿能环保发电有限公司 | Main steam temperature control device |
CN114294971A (en) * | 2022-01-12 | 2022-04-08 | 连云港华港电力设备有限公司 | Condenser convenient to cold junction increase-volume |
CN114294971B (en) * | 2022-01-12 | 2023-01-20 | 连云港华港电力设备有限公司 | Condenser convenient to cold junction increase-volume |
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