JP6345382B2 - Heat exchanger - Google Patents

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JP6345382B2
JP6345382B2 JP2012221803A JP2012221803A JP6345382B2 JP 6345382 B2 JP6345382 B2 JP 6345382B2 JP 2012221803 A JP2012221803 A JP 2012221803A JP 2012221803 A JP2012221803 A JP 2012221803A JP 6345382 B2 JP6345382 B2 JP 6345382B2
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condensate
heat exchange
steam
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pressure
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悠一 杉江
悠一 杉江
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Tlv Co Ltd
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Description

本発明は、水を加熱用の蒸気で加熱して、所定温度の温水を発生し供給することのできる熱交換器に関する。 The present invention relates to a heat exchanger capable of generating and supplying hot water having a predetermined temperature by heating water with heating steam.

熱交換器としては、蒸気供給口を有する熱回収室に冷却菅を内設し、この熱回収室に大気開放部を連通して、大気開放部と熱回収室の下部に凝縮液を貯留させることにより、熱回収室へ不凝縮気体、例えば空気等が流入することを防止して効率良く蒸気と水を熱交換することができるものである。 As a heat exchanger, a cooling tub is installed in a heat recovery chamber having a steam supply port, and an air opening portion is communicated with the heat recovery chamber, and condensate is stored in the air opening portion and a lower portion of the heat recovery chamber. Thus, it is possible to efficiently exchange heat between steam and water by preventing non-condensable gas such as air from flowing into the heat recovery chamber.

この熱交換器においては、蒸気の保有する熱量を水へ完全に熱交換することができない問題があった。これは、蒸気と水のみを熱交換するだけであり、蒸気が凝縮して未だ高温状態の復水と水を熱交換しないためである。即ち、上記従来の熱交換器では、蒸気が気相から液相に相変化する場合の潜熱だけを利用しているが、高温復水の保有している顕熱を十分には利用していないためである。 In this heat exchanger, there is a problem that the amount of heat held by the steam cannot be completely exchanged with water. This is because only the steam and water are heat-exchanged, and the steam is condensed and does not exchange heat between the high-temperature condensate and water. That is, the conventional heat exchanger uses only the latent heat when the vapor changes phase from the gas phase to the liquid phase, but does not sufficiently use the sensible heat possessed by the high-temperature condensate. Because.

特開昭60−120186号公報Japanese Patent Laid-Open No. 60-120186

解決しようとする課題は、蒸気の潜熱と共に高温復水の顕熱も利用することによって、蒸気と水の熱交換率を向上させることのできる熱交換器を提供することである。 The problem to be solved is to provide a heat exchanger capable of improving the heat exchange rate of steam and water by utilizing the sensible heat of the high-temperature condensate together with the latent heat of the steam.

本発明は、熱交換容器に蒸気と水を供給して、水を蒸気によって所定温度まで加熱するものにおいて、第1の熱交換容器の内部に加熱用蒸気が通過する加熱蒸気管を取り付けて、当該第1の熱交換容器の下部に加熱蒸気管と接続した液体圧送部材を配置して、当該液体圧送部材の復水出口に第2の熱交換容器を接続し、当該第2の熱交換容器で高温復水と水を熱交換するものである。 In the present invention, steam and water are supplied to a heat exchange container, and the water is heated to a predetermined temperature by steam, and a heating steam pipe through which heating steam passes is attached to the inside of the first heat exchange container, A liquid pumping member connected to the heating steam pipe is disposed below the first heat exchange container, a second heat exchange container is connected to the condensate outlet of the liquid pumping member, and the second heat exchange container The heat exchange between hot condensate and water.

本発明の熱交換器は、第1の熱交換容器の加熱蒸気管で蒸気の相変化に伴う潜熱で水を加熱すると共に、第2の熱交換容器で高温復水の顕熱で水を加熱することによって、蒸気と水の熱交換率を向上させることができる。 The heat exchanger of the present invention heats water with the latent heat accompanying the phase change of the steam in the heating steam pipe of the first heat exchange container, and heats the water with the sensible heat of the high-temperature condensate in the second heat exchange container. By doing so, the heat exchange rate of steam and water can be improved.

本発明の熱交換器の実施例を示す構成図。The block diagram which shows the Example of the heat exchanger of this invention.

本発明は、加熱蒸気管を取り付けた第1の熱交換容器と、顕熱加熱する第2の熱交換容器を用いるものであるが、この第2の熱交換容器も内部に高温復水菅を取り付けて、高温復水と水を間接熱交換することが好適である。 The present invention uses a first heat exchange vessel with a heated steam pipe and a second heat exchange vessel that performs sensible heat heating. The second heat exchange vessel also has a high-temperature condensate inside. It is preferred to attach and indirect heat exchange between hot condensate and water.

図1において、第1の熱交換容器1と、第1の熱交換容器1へ加熱用の蒸気を供給する蒸気供給管2と、第1の熱交換容器1の内部に取り付けた加熱蒸気管3と、第1の熱交換容器1の下部に配置した液体圧送部材4と、液体圧送部材4の復水出口5と接続した第2の熱交換容器6とで熱交換器を構成する。 In FIG. 1, a first heat exchange container 1, a steam supply pipe 2 for supplying steam for heating to the first heat exchange container 1, and a heating steam pipe 3 attached to the inside of the first heat exchange container 1. And the heat exchanger is comprised by the 2nd heat exchange container 6 connected to the condensate exit 5 of the liquid pumping member 4 and the liquid pumping member 4 arrange | positioned in the lower part of the 1st heat exchange container 1. FIG.

第1の熱交換容器1は円筒状のタンクであり、上部に蒸気供給管2を接続すると共に、下部には第2の熱交換容器6からの温水供給管7を接続する。第1の熱交換容器1の上部右側面には、第1の熱交換容器1の内部で所定温度まで加熱された温水排出管8を接続する。温水排出管8の右側端部は、図示しない温水使用装置と接続する。   The first heat exchange container 1 is a cylindrical tank, and a steam supply pipe 2 is connected to the upper part, and a hot water supply pipe 7 from the second heat exchange container 6 is connected to the lower part. A hot water discharge pipe 8 heated to a predetermined temperature inside the first heat exchange container 1 is connected to the upper right side surface of the first heat exchange container 1. The right end of the hot water discharge pipe 8 is connected to a hot water use device (not shown).

第1の熱交換容器1の下部に液体圧送部材4を配置する。液体圧送部材4は、 第1の熱交換容器1の加熱蒸気管3で蒸気の凝縮した復水が流入する復水流入口12の入口側に逆止弁14を取り付ける。この逆止弁14は、液体圧送部材4側への復水の通過を許容し、逆方向の復水の通過は許容しないものである。   A liquid pumping member 4 is disposed below the first heat exchange container 1. The liquid pumping member 4 has a check valve 14 attached to the inlet side of the condensate inlet 12 into which condensate condensed with steam through the heating steam pipe 3 of the first heat exchange vessel 1 flows. This check valve 14 allows the condensate to pass to the liquid pumping member 4 and does not allow the condensate to pass in the reverse direction.

液体圧送部材4の復水出口5にも逆止弁16を介して復水圧送管路17を接続する。この逆止弁16は液体圧送部材4から復水圧送管路17側へのみ復水を通過させるものである。復水圧送管路17の左側端部を第2の熱交換容器6の上部に接続する。  A condensate pressure feed line 17 is also connected to the condensate outlet 5 of the liquid pressure feed member 4 via a check valve 16. This check valve 16 allows the condensate to pass only from the liquid pumping member 4 to the condensate pumping line 17 side. The left end of the condensate pressure feed line 17 is connected to the upper part of the second heat exchange vessel 6.

液体圧送部材4の上部に、圧送流体としての高圧蒸気供給管18と接続した高圧蒸気導入口19を設ける。高圧蒸気供給管18の上端部は蒸気供給管2と接続する。高圧蒸気導入口19の右側方に高圧蒸気の排出口20を設ける。排出口20には高圧蒸気の排出管21を接続する。  A high-pressure steam inlet 19 connected to a high-pressure steam supply pipe 18 as a pressure-feeding fluid is provided on the upper part of the liquid pressure-feeding member 4. The upper end of the high-pressure steam supply pipe 18 is connected to the steam supply pipe 2. A high-pressure steam outlet 20 is provided on the right side of the high-pressure steam inlet 19. A high-pressure steam discharge pipe 21 is connected to the discharge port 20.

液体圧送部材4は、内部に配置した図示しないフロートが下方部に位置する場合に、高圧蒸気の導入口19が閉口され、一方、排出口20が開口されて、第1の熱交換容器1の加熱蒸気管3内で蒸気の凝縮した復水が、逆止弁14と復水流入口12を通って液体圧送部材4内へ流下する。  When the float (not shown) arranged inside is located in the lower part, the liquid pressure feeding member 4 is closed with the high-pressure steam inlet 19 while the outlet 20 is opened, so that the first heat exchange container 1 Condensate condensed with steam in the heating steam pipe 3 flows into the liquid pressure feeding member 4 through the check valve 14 and the condensate inlet 12.

液体圧送部材4内に復水が溜まって図示しないフロートが所定の上方部に位置すると、排出口20が閉口され、一方、高圧蒸気の導入口19が開口されて、高圧蒸気供給管18から高圧蒸気が液体圧送部材4内に流入し、内部に溜まった復水を、復水出口5と逆止弁16及び復水圧送管路17を経て第2の熱交換容器6へと圧送するものである。   When condensate accumulates in the liquid pumping member 4 and a float (not shown) is positioned at a predetermined upper portion, the discharge port 20 is closed, while the high-pressure steam inlet 19 is opened, and the high-pressure steam supply pipe 18 Steam flows into the liquid pumping member 4, and the condensate accumulated inside is pumped to the second heat exchange vessel 6 through the condensate outlet 5, the check valve 16 and the condensate pumping line 17. is there.

復水が圧送されて液体圧送部材4内の水位が低下すると、再度、高圧蒸気の導入口19が閉口され、排出口20が開口されることにより、復水流入口12から復水が液体圧送部材4内へ流下してくる。このような作動サイクルを繰り返すことにより、液体圧送部材4は、第1の熱交換容器1内で蒸気の凝縮した復水を第2の熱交換容器6へ圧送するものである。   When the condensate is pumped and the water level in the liquid pumping member 4 decreases, the high pressure steam inlet 19 is closed again and the outlet 20 is opened, so that the condensate is fed from the condensate inlet 12 to the liquid pumping member. It flows down into 4. By repeating such an operation cycle, the liquid pumping member 4 pumps the condensate condensed with steam in the first heat exchange vessel 1 to the second heat exchange vessel 6.

第2の熱交換容器6には、下部に水供給管9を接続すると共に、上部に温水供給管7の下端部を接続する。第2の熱交換容器6の復水圧送管路17の下端部には、蒸気は排出することがなく、復水だけを外部へ排出する機能を有する蒸気トラップ10を取り付ける。   A water supply pipe 9 is connected to the lower part of the second heat exchange vessel 6 and a lower end part of the hot water supply pipe 7 is connected to the upper part. A steam trap 10 having a function of discharging only the condensate to the outside is attached to the lower end portion of the condensate pressure-feeding conduit 17 of the second heat exchange vessel 6.

蒸気供給管2から第1の熱交換容器1の加熱蒸気管3へ供給される蒸気は、内部の温水を所定温度まで加熱することによって、凝縮して復水となり下部に設置された液体圧送部材4へと流下する。一方、第1の熱交換容器1で所定温度まで加熱された温水は、温水排出管8から図示しない温水使用装置へと供給される。 The steam supplied from the steam supply pipe 2 to the heating steam pipe 3 of the first heat exchange vessel 1 is condensed to condensate by heating the internal warm water to a predetermined temperature, and is a liquid pressure-feeding member installed in the lower part. Flow down to 4. On the other hand, the hot water heated to a predetermined temperature in the first heat exchange vessel 1 is supplied from the hot water discharge pipe 8 to a hot water using device (not shown).

液体圧送部材4へ流下した復水は、高温状態であるために多くの熱量を保有しており、この高温復水が液体圧送部材4から第2の熱交換容器6へ供給され、水供給管9から供給される水を顕熱加熱する。顕熱加熱された水は、温水供給管7から第1の熱交換容器1へ供給されて蒸気で潜熱加熱される。 Since the condensate flowing down to the liquid pumping member 4 is in a high temperature state, it has a large amount of heat, and this high temperature condensate is supplied from the liquid pumping member 4 to the second heat exchange vessel 6 and is supplied to the water supply pipe. The water supplied from 9 is heated by sensible heat. The sensible heat-heated water is supplied from the hot water supply pipe 7 to the first heat exchange container 1 and is latently heated with steam.

本発明は、水を加熱用の蒸気で加熱して、所定温度の温水を発生し供給することのできる熱交換器として利用することができる。   INDUSTRIAL APPLICABILITY The present invention can be used as a heat exchanger that can heat water with heating steam to generate and supply hot water at a predetermined temperature.

1 第1の熱交換容器
2 蒸気供給管
3 加熱蒸気管
4 液体圧送部材
5 復水出口
6 第2の熱交換容器
7 温水供給管
8 温水排出管
9 水供給管
12 復水流入口
17 復水圧送管路
18 高圧蒸気供給管
19 高圧蒸気導入口
20 高圧蒸気の排出口
DESCRIPTION OF SYMBOLS 1 1st heat exchange container 2 Steam supply pipe 3 Heating steam pipe 4 Liquid pumping member 5 Condensate outlet 6 Second heat exchange container 7 Hot water supply pipe 8 Hot water discharge pipe 9 Water supply pipe 12 Condensate inlet 17 Condensate pressure feed Line 18 High-pressure steam supply pipe 19 High-pressure steam inlet 20 High-pressure steam outlet

Claims (1)

水を蒸気によって所定温度まで加熱する熱交換器であって、
加熱用蒸気が通過する加熱蒸気管を内部に有し、外部から供給された温水を前記加熱用蒸気で潜熱加熱する第1の熱交換容器と、
前記第1の熱交換容器の下流の加熱蒸気管と接続され、前記加熱蒸気管から排出された復水を、高圧蒸気を用いて外部に圧送する液体圧送部材と、
前記液体圧送部材の復水出口に接続された復水圧送管路を有し、外部から供給された水を前記復水圧送管路の復水で顕熱加熱して得られた温水を、前記第1の熱交換容器の内部に供給する第2の熱交換容器とを備え、
前記液体圧送部材は、前記加熱蒸気管から排出された復水を、高圧蒸気を用いて前記第2の熱交換容器の前記復水圧送管路に圧送する熱交換器。
A heat exchanger for heating water to a predetermined temperature with steam,
A first heat exchange vessel that has a heating steam pipe through which heating steam passes, and heats the hot water supplied from the outside with the heating steam;
A liquid pumping member connected to a heating steam pipe downstream of the first heat exchange vessel and pumping the condensate discharged from the heating steam pipe to the outside using high-pressure steam;
The have a recovery pressure Okukanro connected to condensate outlet of the liquid pumping member, hot water obtained by sensible heat of water supplied from the outside in the condensate of the condensate water pressure Okukanro, wherein A second heat exchange container that is supplied to the inside of the first heat exchange container,
The liquid pumping member is a heat exchanger that pumps the condensate discharged from the heating steam pipe to the condensate pumping line of the second heat exchange container using high-pressure steam.
JP2012221803A 2012-10-04 2012-10-04 Heat exchanger Active JP6345382B2 (en)

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JP2012221803A JP6345382B2 (en) 2012-10-04 2012-10-04 Heat exchanger

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Application Number Priority Date Filing Date Title
JP2012221803A JP6345382B2 (en) 2012-10-04 2012-10-04 Heat exchanger

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JP2014074531A JP2014074531A (en) 2014-04-24
JP2014074531A5 JP2014074531A5 (en) 2015-09-17
JP6345382B2 true JP6345382B2 (en) 2018-06-20

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Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60120186A (en) * 1983-12-02 1985-06-27 Kanagawaken Heat exchanger
JPH04116346A (en) * 1990-09-05 1992-04-16 Hisaka Works Ltd Condenser
JP2002054883A (en) * 2000-08-10 2002-02-20 Tlv Co Ltd Heat exchanger
JP2004308933A (en) * 2003-04-02 2004-11-04 Toyo Radiator Co Ltd Half-filled liquid type regenerator
JP5350057B2 (en) * 2009-04-15 2013-11-27 株式会社テイエルブイ Heat exchanger

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