JPH0886398A - Condensate discharging device - Google Patents

Condensate discharging device

Info

Publication number
JPH0886398A
JPH0886398A JP6247002A JP24700294A JPH0886398A JP H0886398 A JPH0886398 A JP H0886398A JP 6247002 A JP6247002 A JP 6247002A JP 24700294 A JP24700294 A JP 24700294A JP H0886398 A JPH0886398 A JP H0886398A
Authority
JP
Japan
Prior art keywords
steam
gas
pipe
liquid separation
separation container
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
JP6247002A
Other languages
Japanese (ja)
Other versions
JP3509954B2 (en
Inventor
Shizumaro Ooishi
鎮麿 大石
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 JP24700294A priority Critical patent/JP3509954B2/en
Publication of JPH0886398A publication Critical patent/JPH0886398A/en
Application granted granted Critical
Publication of JP3509954B2 publication Critical patent/JP3509954B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

PURPOSE: To provide a condensate discharging device capable of sucking the condensate produced in a steam using device surely without accumulating it. CONSTITUTION: A steam feeding pipe 15 to feed steam is connected to a steam using device 1, and a gas-liquid separating container 3 is connected to the steam using device 1 through a pipe 2. Also a cylindrical pipe 4 and an atmospheric pressure interconnecting pipe 6 are attached to the inside of the gas-liquid separating container 3 so as to form a liquid sump part 7 and an atmospheric pressure interconnecting part 8, and a cooling pipe 10 is arranged inside the gas-liquid separating container 3.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は蒸気使用装置内に滞留す
る不凝縮性の気体としてのエア―や、蒸気が凝縮して生
じた復水を、蒸気使用装置から排出するものに関する。
通常、蒸気使用装置では蒸気による加熱効率を高くする
ために、装置内部に滞留するエア―や、蒸気が加熱を行
なうことによって生じた復水は、速やかに装置外へ排出
されている。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to air as a non-condensable gas that accumulates in a steam-using device, and to condensate produced by condensation of steam from a steam-using device.
Usually, in a steam using apparatus, in order to increase heating efficiency by steam, air staying inside the apparatus and condensed water generated by heating by the steam are promptly discharged to the outside of the apparatus.

【0002】[0002]

【従来の技術】従来から初期エア―や復水を排出するも
のとして、所謂スチ―ムトラップが用いられていた。ス
チ―ムトラップは各種型式のものが用いられているが、
蒸気と復水の比重差を利用して復水が流入してくればフ
ロ―トが浮上して弁口を開口することにより復水を系外
へ排出するものや、バイメタルやベロ―ズ等の温度応動
素子を組み込んで蒸気よりも所定温度低くなった復水や
エア―を排出するもの等が使用されている。
2. Description of the Related Art Conventionally, a so-called steam trap has been used as a device for discharging initial air and condensed water. Various types of steam traps are used,
When the condensate flows in using the difference in specific gravity between steam and the condensate, the float floats up and opens the valve opening to discharge the condensate out of the system, bimetal, velor, etc. There is used a device that incorporates the temperature responsive element of (1) and discharges condensate or air whose temperature is lower than steam by a predetermined temperature.

【0003】[0003]

【発明が解決しようとする課題】従来から用いられてい
るスチ―ムトラップは、蒸気使用装置で発生した復水を
吸引することができず、蒸気使用装置に復水を滞留して
しまう問題があった。蒸気使用圧力が低くて大気圧とほ
とんど差が無い場合や、蒸気使用装置とスチ―ムトラッ
プとの間に立下げ部を設けることができないような場合
には、蒸気使用装置で発生した復水がスチ―ムトラップ
に自然流下することができず滞留してしまうのである。
The conventional steam trap has a problem in that the condensed water generated in the steam using apparatus cannot be sucked in and the condensed water stays in the steam using apparatus. It was If the steam usage pressure is low and there is almost no difference from the atmospheric pressure, or if it is not possible to provide a fall part between the steam usage device and the steam trap, the condensate generated in the steam usage device It cannot flow down to the steam trap and stays there.

【0004】従って本発明の技術的課題は、蒸気使用装
置等で発生した復水を確実に吸引することができるよう
にして、復水を滞留することがない復水排出装置を得る
ことである。
Therefore, a technical object of the present invention is to obtain a condensate drainage device which can surely suck the condensate water generated in a steam using device or the like so as not to retain the condensed water. .

【0005】[0005]

【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、蒸気使用装置
から不凝縮性の気体や凝縮した復水を排出するものにお
いて、気液分離容器と、該容器の下部に設けた液溜め部
と、該液溜め部の下部と連通した大気圧連通部と、気液
分離容器の主に上方部に取り付けた冷却部とから成るも
のである。
Means for Solving the Problems The technical means of the present invention taken to solve the above-mentioned technical problem is to discharge a non-condensable gas or condensed condensate from a steam using device. What comprises a liquid separation container, a liquid reservoir provided in the lower part of the container, an atmospheric pressure communication part communicating with the lower part of the liquid reservoir, and a cooling part mainly attached to the upper part of the gas-liquid separation container Is.

【0006】[0006]

【作用】上記の技術的手段の作用は下記の通りである。
蒸気使用装置の使用開始時はエア―が滞留しており、気
液分離容器内の液溜め部に液体は存在しない。従って、
蒸気使用装置に初期蒸気が供給されてエア―が気液分離
容器内へ押し出されて来ると、エア―は気液分離容器を
素通りして系外へ排出される。
The operation of the above technical means is as follows.
At the beginning of use of the steam-using device, air is accumulated, and there is no liquid in the liquid reservoir inside the gas-liquid separation container. Therefore,
When the initial steam is supplied to the steam using device and air is pushed out into the gas-liquid separation container, the air passes through the gas-liquid separation container and is discharged to the outside of the system.

【0007】エア―が排出された後、蒸気使用装置で凝
縮した復水が気液分離容器内へ流入して来ると、復水が
下部に溜って液溜め部に滞留すると共に、復水の一部が
再蒸発する。再蒸発した蒸気を冷却部により冷却するこ
とにより、気液分離容器内は大気圧よりも低い減圧状態
となる。気液分離容器内が減圧状態と成ることにより、
蒸気使用装置で生じた復水は気液分離容器内へ吸引さ
れ、所定量溜ると水頭圧により液溜め部と大気圧連通部
とを経て系外へ排出される。
When the condensate condensed by the steam using device flows into the gas-liquid separation container after the air is discharged, the condensate collects in the lower part and stays in the liquid reservoir, and at the same time, the condensate is condensed. Partly re-evaporates. By cooling the re-evaporated vapor by the cooling unit, the inside of the gas-liquid separation container is in a reduced pressure state lower than atmospheric pressure. By reducing the pressure inside the gas-liquid separation container,
Condensate produced in the steam-using device is sucked into the gas-liquid separation container, and when it is accumulated in a predetermined amount, it is discharged to the outside of the system via the liquid reservoir and the atmospheric pressure communicating portion due to the water head pressure.

【0008】[0008]

【実施例】上記の技術的手段の具体例を示す実施例を説
明する。蒸気使用装置1に加熱用の蒸気を供給する蒸気
供給管15をバルブ16を介して接続する。蒸気使用装
置1に管路2を介して気液分離容器3を接続する。気液
分離容器3は円筒状容器で形成し、中心部に気液分離容
器3よりも小径の円筒パイプ4を下端に隙間5を設けて
取り付ける。円筒パイプ4の下部に円筒パイプ4より更
に小径の大気圧連通管6を配置する。大気圧連通管6は
パイプ20により大気へ開放されている。大気圧連通管
6の上端は円筒パイプ4の下端よりも所定量だけ上部に
位置するように取り付ける。大気圧連通管6の外周と円
筒パイプ4の内外周及び気液分離容器3の下部内周とで
液溜め部7を形成する。大気圧連通管6及び円筒パイプ
4の内周で大気圧連通部8を形成する。
EXAMPLES Examples showing specific examples of the above technical means will be described. A steam supply pipe 15 for supplying steam for heating to the steam using apparatus 1 is connected via a valve 16. A gas-liquid separation container 3 is connected to the steam using device 1 via a pipe line 2. The gas-liquid separation container 3 is formed as a cylindrical container, and a cylindrical pipe 4 having a diameter smaller than that of the gas-liquid separation container 3 is attached to the center portion with a gap 5 provided at the lower end. An atmospheric pressure communicating pipe 6 having a diameter smaller than that of the cylindrical pipe 4 is arranged below the cylindrical pipe 4. The atmospheric pressure communication pipe 6 is opened to the atmosphere by a pipe 20. The atmospheric pressure communication pipe 6 is attached so that the upper end thereof is located above the lower end of the cylindrical pipe 4 by a predetermined amount. The outer periphery of the atmospheric pressure communication pipe 6, the inner and outer periphery of the cylindrical pipe 4, and the lower inner periphery of the gas-liquid separation container 3 form a liquid reservoir 7. An atmospheric pressure communication portion 8 is formed on the inner circumferences of the atmospheric pressure communication pipe 6 and the cylindrical pipe 4.

【0009】気液分離容器3の上方部に冷却部としての
冷却管10を取り付ける。冷却管10は円筒パイプ4の
外周を螺旋状に取り巻いたもので、冷却流体供給部11
から冷却流体を供給して、気液分離容器3内の蒸気を冷
却することにより凝縮させて復水とし、冷却流体取り出
し部12から系外へ排除したり、あるいは、別途の温水
使用箇所へ送付するするものである。
A cooling pipe 10 as a cooling unit is attached to the upper part of the gas-liquid separation container 3. The cooling pipe 10 is formed by spirally surrounding the outer circumference of the cylindrical pipe 4, and the cooling fluid supply unit 11
The cooling fluid is supplied from the cooling fluid, and the steam in the gas-liquid separation container 3 is cooled to condense it into condensate, which is then removed from the cooling fluid extraction section 12 to the outside of the system, or sent to a separate hot water point. To do.

【0010】蒸気供給管15を分岐して管路17とバル
ブ18を介して気液分離容器3の上部と接続する。この
分岐管路17は、気液分離容器3内の再蒸発蒸気の量が
少ない場合や変動する場合等に所望量の蒸気を供給する
ことにより、気液分離容器3内の減圧状態を確保するた
めのものである。
The vapor supply pipe 15 is branched and connected to the upper part of the gas-liquid separation container 3 via a pipe line 17 and a valve 18. This branch line 17 secures a depressurized state in the gas-liquid separation container 3 by supplying a desired amount of steam when the amount of re-evaporated vapor in the gas-liquid separation container 3 is small or fluctuates. It is for.

【0011】次に作用を説明する。蒸気使用装置1の使
用初期においては、蒸気使用装置1内には不凝縮性のエ
ア―が滞留していると共に、気液分離容器3下部の液溜
め部7に液体は存在しない。この状態でバルブ16を開
弁して加熱用の蒸気を蒸気供給管15から蒸気使用装置
1へ供給すると、蒸気使用装置1内のエア―は蒸気に押
し出されて気液分離容器3に至り、液体の存在しない下
部液溜め部7と隙間5と大気圧連通管6及びパイプ20
を経て外部に排出される。
Next, the operation will be described. At the beginning of use of the steam using device 1, non-condensable air is accumulated in the steam using device 1 and no liquid exists in the liquid reservoir 7 below the gas-liquid separation container 3. In this state, when the valve 16 is opened to supply the steam for heating from the steam supply pipe 15 to the steam using apparatus 1, the air in the steam using apparatus 1 is pushed out by the steam and reaches the gas-liquid separation container 3. Liquid-free lower liquid reservoir 7, gap 5, atmospheric pressure communication pipe 6 and pipe 20
And then discharged to the outside.

【0012】エア―が排出されるに連れて気液分離容器
3内へは、蒸気使用装置1を初期加熱して生じた復水が
流入し、液溜め部7に溜ると共に、その一部が再蒸発し
て再度蒸気となり気液分離容器3の上方に溜る。冷却管
10に冷却流体を供給することにより、再蒸発した蒸気
は再度凝縮して復水となり、蒸気が凝縮した割合いだけ
気液分離容器3内は減圧状態となる。減圧状態となるこ
とにより、蒸気使用装置1で加熱により生じた復水は気
液分離容器3内へ吸引され液溜め部7に溜る。液溜め部
7に溜った復水の量が所定量を越えるとその水頭圧によ
り大気圧を越えて大気圧連通管6とパイプ20から外部
へ排出される。
Condensate generated by the initial heating of the steam-using device 1 flows into the gas-liquid separation container 3 as the air is discharged, and the condensed water accumulates in the liquid reservoir 7 and a part of it. It re-evaporates to become vapor again and accumulates above the gas-liquid separation container 3. By supplying the cooling fluid to the cooling pipe 10, the re-evaporated vapor is condensed again and becomes condensed water, and the inside of the gas-liquid separation container 3 is depressurized by the rate of the condensed vapor. Due to the reduced pressure state, the condensate generated by heating in the steam using device 1 is sucked into the gas-liquid separation container 3 and is accumulated in the liquid reservoir 7. When the amount of the condensed water accumulated in the liquid reservoir 7 exceeds a predetermined amount, the head pressure of the condensed water exceeds the atmospheric pressure, and the condensed water is discharged from the atmospheric pressure communicating pipe 6 and the pipe 20 to the outside.

【0013】[0013]

【発明の効果】上記のように本発明によれば、気液分離
容器内を液溜め部により大気圧雰囲気と遮断し、冷却部
により所定の減圧状態を維持することができることによ
り、低圧の蒸気使用装置やスチ―ムトラップへの立下げ
部を設けることができないような場合であっても、蒸気
使用装置で発生した復水や初期エア―を気液分離容器内
へ吸引して系外へ排出することができる。
As described above, according to the present invention, the inside of the gas-liquid separation container can be shut off from the atmospheric pressure atmosphere by the liquid reservoir, and a predetermined depressurized state can be maintained by the cooling unit. Even if it is not possible to provide a device or a trap for the steam trap, the condensate and initial air generated in the steam-using device are sucked into the gas-liquid separation container and discharged to the outside of the system. can do.

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

【図1】本発明の復水排出装置の使用例を示す構成図で
ある。
FIG. 1 is a configuration diagram showing an example of use of a condensate discharge device of the present invention.

【符号の説明】[Explanation of symbols]

1 蒸気使用装置 3 気液分離容器 4 円筒パイプ 6 大気圧連通管 7 液溜め部 8 大気圧連通部 10 冷却管 15 蒸気供給管 1 Steam use device 3 Gas-liquid separation container 4 Cylindrical pipe 6 Atmospheric pressure communication pipe 7 Liquid storage part 8 Atmospheric pressure communication part 10 Cooling pipe 15 Steam supply pipe

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 蒸気使用装置から不凝縮性の気体や凝縮
した復水を排出するものにおいて、気液分離容器と、該
容器の下部に設けた液溜め部と、該液溜め部の下部と連
通した大気圧連通部と、気液分離容器の主に上方部に取
り付けた冷却部とから成ることを特徴とする復水排出装
置。
1. A device for discharging a non-condensable gas or condensed condensate from a steam-using device, a gas-liquid separation container, a liquid reservoir provided at a lower portion of the container, and a lower portion of the liquid reservoir. A condensate discharge device comprising: an atmospheric pressure communication part that communicates with a cooling part, which is mainly attached to an upper part of a gas-liquid separation container.
JP24700294A 1994-09-14 1994-09-14 Condensate discharge device Expired - Fee Related JP3509954B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24700294A JP3509954B2 (en) 1994-09-14 1994-09-14 Condensate discharge device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24700294A JP3509954B2 (en) 1994-09-14 1994-09-14 Condensate discharge device

Publications (2)

Publication Number Publication Date
JPH0886398A true JPH0886398A (en) 1996-04-02
JP3509954B2 JP3509954B2 (en) 2004-03-22

Family

ID=17156925

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24700294A Expired - Fee Related JP3509954B2 (en) 1994-09-14 1994-09-14 Condensate discharge device

Country Status (1)

Country Link
JP (1) JP3509954B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002306955A (en) * 2001-04-13 2002-10-22 Tlv Co Ltd Steam heating apparatus
JP2002306956A (en) * 2001-04-13 2002-10-22 Tlv Co Ltd Steam heating apparatus
JP2007076219A (en) * 2005-09-15 2007-03-29 Tlv Co Ltd Vapor heater

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6017203Y2 (en) * 1980-09-16 1985-05-27 株式会社草野科学器械製作所 Gas trap for distillation
JPS63182397U (en) * 1987-05-15 1988-11-24
JPH04108156U (en) * 1991-03-06 1992-09-18 三菱重工業株式会社 condenser
JPH05141614A (en) * 1991-11-15 1993-06-08 Tlv Co Ltd Vapor liquid separator with temperature adjustment function
JPH05196373A (en) * 1992-01-06 1993-08-06 Hitachi Ltd Condenser
JPH0632898U (en) * 1992-10-07 1994-04-28 国際電気株式会社 Steam trap pressure regulator

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6017203Y2 (en) * 1980-09-16 1985-05-27 株式会社草野科学器械製作所 Gas trap for distillation
JPS63182397U (en) * 1987-05-15 1988-11-24
JPH04108156U (en) * 1991-03-06 1992-09-18 三菱重工業株式会社 condenser
JPH05141614A (en) * 1991-11-15 1993-06-08 Tlv Co Ltd Vapor liquid separator with temperature adjustment function
JPH05196373A (en) * 1992-01-06 1993-08-06 Hitachi Ltd Condenser
JPH0632898U (en) * 1992-10-07 1994-04-28 国際電気株式会社 Steam trap pressure regulator

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002306955A (en) * 2001-04-13 2002-10-22 Tlv Co Ltd Steam heating apparatus
JP2002306956A (en) * 2001-04-13 2002-10-22 Tlv Co Ltd Steam heating apparatus
JP2007076219A (en) * 2005-09-15 2007-03-29 Tlv Co Ltd Vapor heater

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