JPS5831292A - Recovering method for heat of drain - Google Patents

Recovering method for heat of drain

Info

Publication number
JPS5831292A
JPS5831292A JP12868781A JP12868781A JPS5831292A JP S5831292 A JPS5831292 A JP S5831292A JP 12868781 A JP12868781 A JP 12868781A JP 12868781 A JP12868781 A JP 12868781A JP S5831292 A JPS5831292 A JP S5831292A
Authority
JP
Japan
Prior art keywords
drain
cooling water
cooler
heat
heat exchange
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
JP12868781A
Other languages
Japanese (ja)
Inventor
Akizo Chiba
千葉 彰三
Fumio Adachi
足立 文雄
Tetsuya Yokogawa
横川 徹也
Osami Mori
森 修身
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.)
KANAGAWAKEN
Kanagawa Prefecture
Original Assignee
KANAGAWAKEN
Kanagawa Prefecture
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 KANAGAWAKEN, Kanagawa Prefecture filed Critical KANAGAWAKEN
Priority to JP12868781A priority Critical patent/JPS5831292A/en
Publication of JPS5831292A publication Critical patent/JPS5831292A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

PURPOSE:To enable to securely recover the thermal energy of a drain, by a method wherein a high-temperature high-pressure drain is separated into a gas and a liquid, the vapors separated are directed into a cooler, and heat exchange is conducted. CONSTITUTION:An unstable drain at a high temperature and a high pressure is directed into a closed container 1 through an intake part 2 for the unstable drain, and is separated into a gas and a liquid. The liquefied drain is accumulated in the container 1, while the vapor separated are directed into the cooler 4 provided on the top face of the container 1. In the cooler 4, heat exchange is conducted between the vapor and cooling water which flows from an inflow port 8 for the cooling water to a discharging port 10 for the cooling water through an upper-stage heat-exchanging pipe 5a, an intermediate-stage heat-exchanging pipe 5b and a lower-stage heat-exchanging pipe 5c. Accordingly, the thermal energy of the drain can be securely recovered.

Description

【発明の詳細な説明】 本発明は、高温・高圧ドレンの熱エネルギーを回収する
方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for recovering thermal energy from high temperature, high pressure drains.

一般的に暖房や加温のための熱の伝送は蒸気によってい
るが、熱の伝送を終えた蒸気はドレン化し、このドレン
を除去しなければ熱の伝送効率は悪化してしまうことに
なる。
Generally, heat is transferred for space heating and heating by steam, but after the heat has been transferred, the steam turns into condensate, and if this condensate is not removed, the heat transfer efficiency will deteriorate.

また、ドレンは一般的には高温・高圧であって、大気圧
下に放出される時、フラッシュ蒸気の形で大量に蒸気化
する。近時、ドレンの熱エネルギーは利用されているが
、フラッシュ蒸気については無策状態であった。ドレン
は大気圧下で100C以下の状態にならなければ不安定
で種々再利用し雌く、ドレンを安定化させるためには熱
を奪う(熱の発生)必要があるが、現状では大気開放状
態のドレンタンクにドレンを貯蔵していて、トレン安定
化のための熱エネルギーの奪取は、発生したドレンの熱
エネルギーを周囲に発散することであった。故にその熱
エネルギーはほとんど利用できなかった。
Furthermore, condensate is generally at high temperature and high pressure, and when discharged to atmospheric pressure, a large amount of condensate vaporizes in the form of flash steam. Recently, the thermal energy of drains has been utilized, but nothing has been done about flash steam. Drain is unstable unless it reaches a temperature of 100C or less under atmospheric pressure and cannot be reused in various ways.In order to stabilize the drain, it is necessary to remove heat (generate heat), but currently it is open to the atmosphere. Condensate was stored in a drain tank, and the method of capturing thermal energy for stabilizing the drain was to dissipate the thermal energy of the generated condensate to the surrounding area. Therefore, the thermal energy could hardly be used.

本発明は上記の点に鑑み、不安定ドレンの熱エネルギー
を確実に回収し、ドレンを安定化させ、さらに安定した
高温冷却水を得るようにするドレ/の熱回収方法を提供
することにある。
In view of the above points, the present invention provides a method for recovering heat from an unstable drain that reliably recovers the thermal energy of the unstable drain, stabilizes the drain, and obtains stable high-temperature cooling water. .

以下、本発明の方法を図面を参照して詳細に説明する。Hereinafter, the method of the present invention will be explained in detail with reference to the drawings.

第1図および第2図において、1は気液分離の密閉容器
であり、この密閉容器1の一方上端には不安定ドレン取
入部2が設けられ、他方下端には安定化ドレン取出部3
が設けられている。
1 and 2, reference numeral 1 denotes a closed container for gas-liquid separation, and an unstable drain intake section 2 is provided at one upper end of this closed container 1, and a stabilized drain outlet section 3 at the other lower end.
is provided.

4は密閉容器1の上面に設けられた大気と接する冷却器
であり、この冷却器4は三段の熱交換パイプ5a 、 
5b 、 5cの各連設部位間をリング状のバッキング
6により密閉状態に接続し、周凹を断熱材7で被覆した
ものである。
4 is a cooler provided on the upper surface of the closed container 1 and in contact with the atmosphere, and this cooler 4 has three stages of heat exchange pipes 5a,
The continuous parts 5b and 5c are connected in a sealed manner by a ring-shaped backing 6, and the circumferential recess is covered with a heat insulating material 7.

そして、前記上段熱交換パイプ5aの一方下端には冷却
水流入口8が設けられており、他方上端から第1連結管
9aによって中段熱交換バイブ5bの一方下端と連結さ
れ、中段熱交換バイブ5bの他方上端からはまた第2連
結管9bによって下段熱交換バイブ5cの一方下端と連
結され、さらに下段熱交換バイブ5cの他方上端には冷
却水排出口10が設けられている。
A cooling water inlet 8 is provided at one lower end of the upper heat exchange pipe 5a, and is connected from the other upper end to one lower end of the middle heat exchange vibe 5b by a first connecting pipe 9a. The other upper end is connected to one lower end of the lower heat exchange vibe 5c by a second connecting pipe 9b, and a cooling water outlet 10 is provided at the other upper end of the lower heat exchange vibe 5c.

前記密閉容器1内には前記下段熱交換バイブ5Cの冷却
水排出口10に連設された密閉容器内熱交換パイプ11
が配設され、ドレンと部分に熱交換を行ってドレンと平
衡温度として高温水取出部12より取り出せるようにな
っている。
Inside the sealed container 1, there is a heat exchange pipe 11 connected to the cooling water outlet 10 of the lower heat exchange vibrator 5C.
is arranged so that the water can be taken out from the high-temperature water extraction part 12 by exchanging heat with the drain and bringing the temperature to equilibrium with that of the drain.

また、この高温水取出口12および下段熱交換バイブ5
cの冷却水排出口10には温水の循環バイブ13を連接
して冷却器4の上部へ導き、蒸気と充分に接触させなが
ら密閉容器1内へ導入するものと゛なっている。そして
また、冷却器4内に液化した蒸気または前記した冷却器
上部からの冷却水とフラッシュ蒸気との接触を良くする
ために金網等の充填物14を収容すると、熱回収により
効果的である。
In addition, this high temperature water outlet 12 and the lower heat exchange vibe 5
A circulating vibrator 13 of warm water is connected to the cooling water outlet 10 of c, and is guided to the upper part of the cooler 4, and is introduced into the closed container 1 while making sufficient contact with the steam. Furthermore, heat recovery is more effective if a filler 14 such as a wire mesh is housed in the cooler 4 in order to improve the contact between the liquefied steam or the cooling water from the upper part of the cooler and the flash steam.

しかして、E述の如く構成されているドレンの熱回収装
置を使用すれば、高温・高圧の不安定ドレンを不安定ド
レン堆人部2より密閉容器1内に導き、気液分離して液
化ドレンを密閉容器1内に貯留させると共に、分離した
蒸気を密閉容器1の上面に設けられた冷却器4に導いて
冷却器4に冷却水流入口8より上段熱交換バイブ5a、
中段熱交換バイブ5bおよび下段熱交換バイブ5cを経
て冷却水排出口10へと流れる冷却水と接触させて熱交
換を行なう。
Therefore, if the condensate heat recovery device configured as described in E is used, the unstable condensate at high temperature and high pressure is introduced into the closed container 1 from the unstable condensate collection section 2, and the condensate is separated into gas and liquid and liquefied. The drain is stored in the closed container 1, and the separated steam is guided to the cooler 4 provided on the upper surface of the closed container 1, and the upper heat exchange vibe 5a is connected to the cooler 4 through the cooling water inlet 8.
Heat exchange is performed by contacting the cooling water flowing to the cooling water outlet 10 via the middle heat exchange vibe 5b and the lower heat exchange vibe 5c.

さらに、冷却水排出口10より排出された冷却水を必要
に応じて密閉容器1内の密閉容器内熱交換パイプ11に
導き、液化ドレンと熱交換させて液化ドレンと平衡温度
として、冷却水を高温水取出部12より取シ出すと共に
、液化ドレンは安定化ドレンとして安定化ドレン取出部
3よシ取り出す。
Furthermore, the cooling water discharged from the cooling water outlet 10 is guided to the closed container heat exchange pipe 11 in the closed container 1 as needed, and the cooling water is exchanged with the liquefied drain to reach an equilibrium temperature with the liquefied drain. The liquefied drain is taken out from the high temperature water take-out part 12 and the liquefied drain is taken out from the stabilized drain take-out part 3 as stabilized drain.

このように本実施例による方法を用いれば、冷却器4に
おける冷却水の経路を複数段に構成し、冷却水温度を上
部側を低温度雰囲気にしであるので、効率のよい熱回収
ができ、よって高温水が得られることになる。さらに、
冷却水を冷却器4の冷却水排出口10を経て密閉容器1
内の密閉容器内熱交換パイプ11に導けば、よシ高温度
の温水を得ることができる。
In this way, if the method according to this embodiment is used, the cooling water path in the cooler 4 is configured in multiple stages, and the cooling water temperature is set to a low temperature atmosphere on the upper side, so that efficient heat recovery is possible. Therefore, high temperature water can be obtained. moreover,
The cooling water is passed through the cooling water outlet 10 of the cooler 4 to the closed container 1.
If the water is led to the heat exchange pipe 11 inside the closed container, hot water at a much higher temperature can be obtained.

次に、本発明に係るドレンの熱回収方法の他の実施例を
第3図について説明すると、前述の実施例は冷却水の各
々の経路において、下から上へと冷却水を流す構成につ
いて説明したが、本実施例では各段の熱交換パイプ5a
、5b、5cの連絡管15a、15bをトラップ様に構
成することにより、管内を冷却水が充満して流れること
となり、前述と同様の効果が得られることになる。なお
、本実施例で前述の実施例と同一部分には同一符号を伺
してその説明を省略する。
Next, another embodiment of the drain heat recovery method according to the present invention will be explained with reference to FIG. 3. The above embodiment describes a configuration in which cooling water flows from bottom to top in each path of cooling water. However, in this embodiment, each stage of heat exchange pipe 5a
, 5b, 5c are configured in a trap-like manner, so that the inside of the pipes is filled with cooling water and the same effect as described above can be obtained. In this embodiment, the same parts as those in the previous embodiment are designated by the same reference numerals, and their explanation will be omitted.

なお、冷却水排出口8や高温水取出部12から取り出す
温水は直接利用することも可能ではあるが、温度コント
ロールをしやすくするために温水貯槽を設け、温度、流
量等を調整することにより、より効果的なものとするこ
とができる。
Although it is possible to use the hot water taken out from the cooling water outlet 8 or the high temperature water outlet 12 directly, in order to make it easier to control the temperature, a hot water storage tank is provided and the temperature, flow rate, etc. are adjusted. It can be made more effective.

以下、実験例を示す。この実験における実験条件は第1
図に示す装置分用い熱交換パイプは1段、冷却水温度は
190のものを用いた。
Experimental examples are shown below. The experimental conditions in this experiment are the first
The heat exchange pipe used in the apparatus shown in the figure was one stage and had a cooling water temperature of 190°C.

実験例1  (3atmのドレ/を1 atmにする)
安定化ドレンの取出部3より96℃のドレン10に9を
得るため、冷却水排出口10より85℃の温水5V4を
得た。
Experimental example 1 (change 3 atm to 1 atm)
In order to obtain a drain 10 at 96°C from the stabilizing drain outlet 3, hot water 5V4 at 85°C was obtained from the cooling water outlet 10.

□実験例2  (5atmのドレンを1 atmにする
)安定化ドレンの取出部3より97℃のドレン10句を
得るため、冷却水排出口10より88℃の温水ZKoを
得た。
□ Experimental Example 2 (Reducing 5 atm drain to 1 atm) In order to obtain 10 drains at 97°C from the stabilized drain outlet 3, hot water ZKo at 88°C was obtained from the cooling water outlet 10.

実験例3  (!+atmのドレンを1 atmにする
)安定化ドレ/の取出部3より95℃のドレン10陽を
得るため高温水取出部12より93℃の温水4.5に4
を得た。
Experimental Example 3 (!+ATM drain to 1 ATM) To obtain 95°C drain 10 from the stabilizing drain/removal part 3, 93°C hot water 4.5 to 4 from the high temperature water take-out part 12.
I got it.

実験例4  (5atmのドレンを1 atmにする)
安定化ドレンの取出部3より96Cのドレン10Kgを
得るため高温水取出部12より94℃の温水6.5に4
を得た。
Experimental example 4 (5 atm drain to 1 atm)
In order to obtain 10 kg of 96C drain from the stabilized drain outlet 3, 94℃ hot water 6.5 to 4
I got it.

以上述べたように本発明に係るドレンの熱回収方法は、
高温・高圧ドレンを密閉容器内に導いて気液分離し、液
化ドレンを密閉容器に貯留すると共に、分離した蒸気を
密閉容器より冷却器に導き、この冷却器内を流通する冷
却水により分離した蒸気の熱交換を行なわしめ、しかる
のち冷却水を温水として取り出すことにより、確実にド
レンの熱エネルギーの回収を行なえ、さらに冷却器より
取り出した温水を密閉容器内において再度熱交換せしめ
てより高温の温水を取り出すことにより、さらに安定し
た高温水を得、熱エネルギーを□はとんど回収できるこ
とができる。
As described above, the drain heat recovery method according to the present invention is
High-temperature, high-pressure condensate is guided into a sealed container to separate gas and liquid, and the liquefied drain is stored in the sealed container, and the separated steam is led from the sealed container to a cooler, where it is separated by cooling water flowing through the cooler. By performing heat exchange with the steam and then taking out the cooling water as hot water, the thermal energy of the drain can be reliably recovered. Furthermore, the hot water taken out from the cooler can be heat-exchanged again in the sealed container to generate hot water at a higher temperature. By extracting hot water, more stable high-temperature water can be obtained, and most of the thermal energy can be recovered.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は本発明に係るドレンの熱回収方法を示すもので、
第1図は一実施例を示す概略構成図、第2図は冷却器部
分を抽出して示す縦断面図、第6図は他の実施例を示す
概略構成図である。 1 密閉容器、4 冷却器、5a 、 5b 、 Sc
  熱交換パイプ、8・・冷却水流入口、10・・冷却
水排出口特許出願人神奈川県
The drawing shows the drain heat recovery method according to the present invention.
FIG. 1 is a schematic configuration diagram showing one embodiment, FIG. 2 is a vertical sectional view showing an extracted cooler portion, and FIG. 6 is a schematic configuration diagram showing another embodiment. 1 Airtight container, 4 Cooler, 5a, 5b, Sc
Heat exchange pipe, 8...Cooling water inlet, 10...Cooling water outlet Patent applicant Kanagawa Prefecture

Claims (2)

【特許請求の範囲】[Claims] (1)  高温・高圧ドレンを密閉容器内に導いて気液
分離し、液化ドレンを密閉容器に貯留すると共に、分離
した蒸気を密閉容器より冷却器に導き、この冷却器内を
流通している冷却水により熱交換を行なわしめることを
特徴とするドレンの熱回収方法。
(1) High-temperature, high-pressure condensate is guided into a sealed container to separate gas and liquid, and the liquefied drain is stored in the sealed container, and the separated vapor is led from the sealed container to a cooler where it circulates. A drain heat recovery method characterized by performing heat exchange with cooling water.
(2)  高温・高圧ドレ/を密閉容器に導いて気液分
離し、液化ドレンを密閉容器に貯留すると共に、分離し
た蒸気を密閉容器よシ冷却器に導き、この冷却器内を流
通している冷却水により熱交換を行なわしめ、該冷却水
を前記密閉容器内に導いて高温・高圧ドレンと熱交換を
行なわしめることを特徴とするドレンの熱回収方法。
(2) High-temperature, high-pressure drain is introduced into a closed container to separate gas and liquid, and the liquefied drain is stored in the closed container, and the separated vapor is led from the closed container to a cooler, where it is circulated through the cooler. 1. A method for recovering heat from a drain, characterized in that heat exchange is performed with the cooling water contained in the drain, and the cooling water is guided into the closed container to exchange heat with the high temperature/high pressure drain.
JP12868781A 1981-08-19 1981-08-19 Recovering method for heat of drain Pending JPS5831292A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12868781A JPS5831292A (en) 1981-08-19 1981-08-19 Recovering method for heat of drain

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12868781A JPS5831292A (en) 1981-08-19 1981-08-19 Recovering method for heat of drain

Publications (1)

Publication Number Publication Date
JPS5831292A true JPS5831292A (en) 1983-02-23

Family

ID=14990935

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12868781A Pending JPS5831292A (en) 1981-08-19 1981-08-19 Recovering method for heat of drain

Country Status (1)

Country Link
JP (1) JPS5831292A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5100739A (en) * 1990-04-26 1992-03-31 Nkk Corporation Separating sheet provided with a plurality of plating layers, excellent in strippability and having a high hardness

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5100739A (en) * 1990-04-26 1992-03-31 Nkk Corporation Separating sheet provided with a plurality of plating layers, excellent in strippability and having a high hardness

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