JPS5821552B2 - Heat recovery equipment using a cyclone evaporator - Google Patents
Heat recovery equipment using a cyclone evaporatorInfo
- Publication number
- JPS5821552B2 JPS5821552B2 JP54105254A JP10525479A JPS5821552B2 JP S5821552 B2 JPS5821552 B2 JP S5821552B2 JP 54105254 A JP54105254 A JP 54105254A JP 10525479 A JP10525479 A JP 10525479A JP S5821552 B2 JPS5821552 B2 JP S5821552B2
- Authority
- JP
- Japan
- Prior art keywords
- evaporator
- hot water
- indirect contact
- cyclone
- contact condenser
- 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.)
- Expired
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B1/00—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
- F28B1/02—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using water or other liquid as the cooling medium
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Description
【発明の詳細な説明】
本発明は熱回収装置に関し、サイクロン式蒸発器と間接
接触凝縮器とを組合わせ、例えば地熱水や工場温排水の
ようなスケール成分などの不純物を含む流体から、その
保有熱を回収し利用することを目的とするものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heat recovery device that combines a cyclone evaporator and an indirect contact condenser to recover heat from a fluid containing impurities such as scale components, such as geothermal water or heated industrial wastewater. The purpose is to recover and utilize the retained heat.
以下本発明の一実施例を図面に基づいて説明する。An embodiment of the present invention will be described below based on the drawings.
不純物を多く含む熱水aは熱水管1を通ってサイクロン
式蒸発器2に入る。Hot water a containing many impurities passes through a hot water pipe 1 and enters a cyclone evaporator 2.
該蒸発器2の蒸気取出管3は間接接触凝縮器5に接続さ
れ前記サイクロン式蒸発器2の内部圧力は、前記間接接
触凝縮器5およびその上部に連結された真空装置9によ
って熱水aの温度に対応する飽和圧力よりも低(保たれ
ており、従って熱水aはサイクロン式蒸発器2の内部で
自己蒸発する。The steam extraction pipe 3 of the evaporator 2 is connected to an indirect contact condenser 5, and the internal pressure of the cyclone type evaporator 2 is controlled by the indirect contact condenser 5 and the vacuum device 9 connected to the upper part of the hot water a. The temperature is kept lower than the corresponding saturation pressure, so the hot water a self-evaporates inside the cyclone evaporator 2.
第2図aまたはbはサイクロン式蒸発器2のそれぞれ一
例を示す横断面図であり、熱水管1を通ってサイクロン
式蒸発器2の胴部に対して接続方向から流入して来た熱
水aは胴部内面に沿って円周方向の運動を与えられる。FIG. 2 a or b is a cross-sectional view showing an example of the cyclone evaporator 2, in which hot water flows into the body of the cyclone evaporator 2 from the connection direction through the hot water pipe 1. a is given circumferential motion along the inner surface of the barrel.
従って蒸気と液の密度差により液は胴部内面に沿って円
周運動しながら蒸発器2の底部に溜まり、第1図のよう
に排温水すとして排水管4から排出される。Therefore, due to the density difference between the vapor and the liquid, the liquid moves circumferentially along the inner surface of the body and accumulates at the bottom of the evaporator 2, and is discharged from the drain pipe 4 as a hot water drain as shown in FIG.
一方サイクロン式蒸発器2で自己蒸発した蒸気Cは蒸気
取出管3に流入し間接接触凝縮器5に導かれる。On the other hand, the steam C self-evaporated in the cyclone evaporator 2 flows into the steam extraction pipe 3 and is led to the indirect contact condenser 5.
この間は間接接触凝縮器5の内圧が前記真空装置90作
用によりサイクロン式蒸発器2より低いので、蒸発Cは
自動的に間接接触凝縮器5の方に流れる。During this period, the internal pressure of the indirect contact condenser 5 is lower than that of the cyclone evaporator 2 due to the action of the vacuum device 90, so the evaporated C automatically flows to the indirect contact condenser 5.
間接接触凝縮器5の内部には伝熱管6が配置され、その
一端に接続された冷水管7からは加熱されるべき清浄な
冷水dが供給され、伝熱管6を通る間にサイクロン式蒸
発器2から導入された蒸気Cにより加熱され、伝熱管6
の他端に接続された温水管8を通って温水eとして利用
系へ導かれる。A heat exchanger tube 6 is disposed inside the indirect contact condenser 5, and clean cold water d to be heated is supplied from a cold water tube 7 connected to one end of the tube, and while passing through the heat exchanger tube 6, a cyclone type evaporator The heat transfer tube 6 is heated by the steam C introduced from the heat exchanger tube 6.
It passes through a hot water pipe 8 connected to the other end and is guided to the utilization system as hot water e.
一方間接接触凝縮器5内部で冷水を加熱した蒸気Cは凝
縮して底部に溜まり、その凝縮水fは復水ポンプ10に
より排出されるが、この凝縮水fは不純物を含む熱水か
ら抽出された純水であり、種種の用水として利用できる
。On the other hand, steam C that heats cold water inside the indirect contact condenser 5 condenses and accumulates at the bottom, and the condensed water f is discharged by the condensate pump 10, but this condensed water f is extracted from the hot water containing impurities. It is pure water and can be used as irrigation water for various species.
ここで熱水から離脱してでき、間接接触凝縮器5内に蓄
積される種々の不凝縮ガスは、真空装置9により外部に
排出され、伝熱管6の伝熱性能の劣化は防止される。Various non-condensable gases that are separated from the hot water and accumulated in the indirect contact condenser 5 are discharged to the outside by the vacuum device 9, thereby preventing deterioration of the heat transfer performance of the heat transfer tubes 6.
なお復水ポンプ10は間接接触凝縮器5の下部の液水頭
を、液を流送するに必要な位置水頭以上に保つことによ
り省略できる。Note that the condensate pump 10 can be omitted by keeping the liquid head at the lower part of the indirect contact condenser 5 at a level higher than the position water head required to flow the liquid.
以上本発明によれば地熱水や工場温排水のようなスケー
ル成分などの不純物を含む熱水からその保有熱を取り出
して有効に使用できるものであり。As described above, according to the present invention, retained heat can be extracted from hot water containing impurities such as scale components, such as geothermal water or heated industrial wastewater, and used effectively.
またサイクロン式蒸発器の内部圧力を簡抜接触凝縮器お
よびそれに接続される真空装置によって供給熱水の温度
に対する飽和圧力よりも低く保持できるので、流入され
た熱水を容易に自己蒸発させることが可能である。In addition, the internal pressure of the cyclone type evaporator can be maintained lower than the saturation pressure for the temperature of the supplied hot water by the simple extraction contact condenser and the vacuum device connected to it, so the hot water that flows in can be easily self-evaporated. It is possible.
また間接接触凝縮器を用いるので、加熱して得られる温
水は清浄を保持できる。Furthermore, since an indirect contact condenser is used, the hot water obtained by heating can maintain its purity.
第1図は本発明の一実施例を示す構成図、第2図a、b
はそれぞれサイクロン式蒸発器の横断面図である。
2・・・・・・サイクロン式蒸発器、5・・・・・・間
接接触凝縮器、6・・・・・・伝熱器、9・・・・・・
真空装置。Fig. 1 is a configuration diagram showing an embodiment of the present invention, Fig. 2 a, b
are cross-sectional views of a cyclone evaporator, respectively. 2...Cyclone evaporator, 5...Indirect contact condenser, 6...Heat transferr, 9...
Vacuum equipment.
Claims (1)
うサイクロン式蒸発器と、該サイクロン式蒸発器に接続
され、該蒸発器で得られた蒸気と加熱されるべき冷水と
を伝熱器を介して間接接触させて温水を得る間接接触凝
縮器と、該間接接触凝縮器に接続された真空装置とを具
備したことを特徴とするサイクロン式蒸発器を使用した
熱回収装置。1. A cyclone type evaporator that self-evaporates inflowing hot water and performs gas-liquid separation, and a heat transfer device connected to the cyclone type evaporator, which transfers the steam obtained in the evaporator and the cold water to be heated. 1. A heat recovery device using a cyclone type evaporator, comprising: an indirect contact condenser that obtains hot water by indirect contact via a cyclone evaporator; and a vacuum device connected to the indirect contact condenser.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP54105254A JPS5821552B2 (en) | 1979-08-17 | 1979-08-17 | Heat recovery equipment using a cyclone evaporator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP54105254A JPS5821552B2 (en) | 1979-08-17 | 1979-08-17 | Heat recovery equipment using a cyclone evaporator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5628691A JPS5628691A (en) | 1981-03-20 |
JPS5821552B2 true JPS5821552B2 (en) | 1983-04-30 |
Family
ID=14402509
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP54105254A Expired JPS5821552B2 (en) | 1979-08-17 | 1979-08-17 | Heat recovery equipment using a cyclone evaporator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5821552B2 (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS445982Y1 (en) * | 1966-08-25 | 1969-03-04 | ||
JPS4910875A (en) * | 1972-05-30 | 1974-01-30 | ||
JPS547677A (en) * | 1977-06-20 | 1979-01-20 | Toshiba Corp | Air-liquid separator |
-
1979
- 1979-08-17 JP JP54105254A patent/JPS5821552B2/en not_active Expired
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS445982Y1 (en) * | 1966-08-25 | 1969-03-04 | ||
JPS4910875A (en) * | 1972-05-30 | 1974-01-30 | ||
JPS547677A (en) * | 1977-06-20 | 1979-01-20 | Toshiba Corp | Air-liquid separator |
Also Published As
Publication number | Publication date |
---|---|
JPS5628691A (en) | 1981-03-20 |
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