JPS6230366B2 - - Google Patents

Info

Publication number
JPS6230366B2
JPS6230366B2 JP55091863A JP9186380A JPS6230366B2 JP S6230366 B2 JPS6230366 B2 JP S6230366B2 JP 55091863 A JP55091863 A JP 55091863A JP 9186380 A JP9186380 A JP 9186380A JP S6230366 B2 JPS6230366 B2 JP S6230366B2
Authority
JP
Japan
Prior art keywords
condensate
tank
counter
accumulated
time
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
Application number
JP55091863A
Other languages
Japanese (ja)
Other versions
JPS5717819A (en
Inventor
Hiroo Harada
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 JP9186380A priority Critical patent/JPS5717819A/en
Publication of JPS5717819A publication Critical patent/JPS5717819A/en
Publication of JPS6230366B2 publication Critical patent/JPS6230366B2/ja
Granted legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01FMEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
    • G01F3/00Measuring the volume flow of fluids or fluent solid material wherein the fluid passes through the meter in successive and more or less isolated quantities, the meter being driven by the flow
    • G01F3/36Measuring the volume flow of fluids or fluent solid material wherein the fluid passes through the meter in successive and more or less isolated quantities, the meter being driven by the flow with stationary measuring chambers having constant volume during measurement
    • G01F3/38Measuring the volume flow of fluids or fluent solid material wherein the fluid passes through the meter in successive and more or less isolated quantities, the meter being driven by the flow with stationary measuring chambers having constant volume during measurement having only one measuring chamber

Description

【発明の詳細な説明】 本発明は蒸気系内に発生した復水の流量を測定
する復水用流量計に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a condensate flow meter that measures the flow rate of condensate generated in a steam system.

蒸気系内で発生した復水の流量を正確に測定す
ることは、蒸気系の熱管理を行う上で極めて重要
なことである。ところが、従来の流量計は構造が
複雑かつ大形で、而も少流量の測定には不向き
で、蒸気主管や小形の熱交換器等の復水発生量の
少ない箇所の流量測定には使用できなかつた。ま
た、復水は高温高圧で取り扱いが難しく、流量計
内等で再蒸発を起こす為、複水の流量の測定を行
える流量計は極めて少なかつた。
Accurately measuring the flow rate of condensate generated within a steam system is extremely important for thermal management of the steam system. However, conventional flowmeters have a complicated structure and are large, making them unsuitable for measuring small flow rates and cannot be used to measure flow rates in areas where a small amount of condensate is generated, such as steam main pipes or small heat exchangers. Nakatsuta. In addition, condensate is difficult to handle due to its high temperature and pressure, and it causes re-evaporation within the flowmeter, so there are very few flowmeters that can measure the flow rate of double water.

本発明は上記事情に鑑みて、構造が簡単で小形
化することができ、而も復水の流量を正確に測定
できる復水用流量計の提供を目的とする。
In view of the above circumstances, it is an object of the present invention to provide a condensate flow meter that has a simple structure, can be made compact, and can accurately measure the flow rate of condensate.

上記の目的を達成するために講じた本発明の技
術的手段は、内部に定量の復水を溜めることがで
きかつこれを検出できる様に形成されたタンク、
蒸気系に接続し蒸気系内に発生した復水をタンク
内に導く様にタンクの上部に開口して設けられた
流入口、タンク内に溜つた復水を自動的に排出す
る様に流出口側に配されたスチームトラツプ、タ
ンク内の復水の貯溜及び流出を制御する様にスチ
ームトラツプの下流側に配された弁手段、及びタ
ンク内に定量の復水が溜る時間を測定する時間測
定手段から成り、復水の溜つた量とその所要時間
とを乗除計算して復水の流量を測定する様にした
ものである。
The technical means of the present invention taken to achieve the above object are: a tank formed to be able to store a fixed amount of condensate inside and to be able to detect this;
An inlet is provided at the top of the tank to connect to the steam system and guide the condensate generated in the steam system into the tank, and an outlet is provided to automatically discharge the condensate that has accumulated in the tank. A steam trap placed on the side, a valve means placed downstream of the steam trap to control the accumulation and outflow of condensate in the tank, and measuring the time for a certain amount of condensate to accumulate in the tank. It consists of a time measuring means, and measures the flow rate of condensate by multiplying and dividing the accumulated amount of condensate by the required time.

上記の技術的手段の作用は下記の通りである。 The operation of the above technical means is as follows.

復水量の測定をする前にスチームトラツプの下
流側に配した弁手段を閉じる。蒸気系内で発生し
た復水は流入口からタンク内に流入して溜る。時
間測定手段でタンク内に定量の復水が溜る時間を
測定し、タンク内に溜つた復水量とその所要時間
とを乗除計算して単位時間当りの流量を演算す
る。タンクの流出口側には気体は逃さず復水のみ
を自動的に排出するスチームトラツプを取り付け
ているので、スチームトラツプの上流側、すなわ
ち、タンク内は蒸気系と同じ圧力である。従つ
て、復水はタンク内で再蒸発を起こさず、正確な
復水量の測定ができる。
Before measuring the amount of condensate, close the valve means located downstream of the steam trap. Condensate generated in the steam system flows into the tank from the inlet and accumulates there. The time measuring means measures the time it takes for a certain amount of condensate to accumulate in the tank, and the amount of condensate accumulated in the tank is multiplied and divided by the required time to calculate the flow rate per unit time. A steam trap is installed on the outlet side of the tank to automatically discharge only condensate without letting gas escape, so the upstream side of the steam trap, that is, the inside of the tank, is at the same pressure as the steam system. Therefore, condensate does not re-evaporate within the tank, allowing accurate measurement of the amount of condensate.

次に、本発明を第1,2図に示す実施例に基づ
いて説明する。第1図に於いて、1は復水を溜め
るタンクで、内部に復水溜り室4を形成する。室
4の天井部には流入口2が開口し、底部には流出
口3が開口する。流入口2は連結管5及び該管5
に配したバルブ19を通して復水発生側6に接続
し、復水を室4内に流下させる。流出口3は連結
管7及びバルブ16を介して復水流出側(図示せ
ず)に接続する。室4の所定上位Hと所定下位L
には電極棒8,9を取り付ける。この際、電極棒
8,9間の容積は予め求めて置く。電極棒8,9
からの信号は時間測定手段10に送る。タンク1
の外表面は保温材17で被い、保温材17の表面
は外装材18で被覆する。
Next, the present invention will be explained based on the embodiments shown in FIGS. 1 and 2. In FIG. 1, numeral 1 denotes a tank for storing condensate, and a condensate storage chamber 4 is formed inside. An inlet 2 opens at the ceiling of the chamber 4, and an outlet 3 opens at the bottom. The inlet 2 is connected to the connecting pipe 5 and the pipe 5
It is connected to the condensate generation side 6 through a valve 19 arranged in the chamber 4, and the condensate flows down into the chamber 4. The outlet 3 is connected to a condensate outlet (not shown) via a connecting pipe 7 and a valve 16. Predetermined upper H and predetermined lower L of room 4
Attach the electrode rods 8 and 9 to the. At this time, the volume between the electrode rods 8 and 9 is determined in advance. Electrode rods 8, 9
The signal from is sent to time measuring means 10. tank 1
The outer surface of is covered with a heat insulating material 17, and the surface of the heat insulating material 17 is covered with an exterior material 18.

時間測定手段10は第2図のものから形成す
る。即ち、一定時間毎にパルス信号を出す基準発
信器12、電極棒9が復水に接した時点から電極
棒8が復水に接する時点までの信号を下記計数器
に送るゲート部11、パルス信号を受信して計数
する計数器13、計数器13からの受信値(時間
値)で予め求めて置いた電極棒8,9間の容積を
乗除計算して単位時間当りの流量を計算する乗除
算器14、及び乗除算器14からの受信値を表示
又は記録する結果表示器15から形成する。図
中、矢印は電極棒8,9からの信号を示す。
The time measuring means 10 is formed from that shown in FIG. That is, a reference transmitter 12 that outputs a pulse signal at fixed time intervals, a gate unit 11 that sends a signal from the time when the electrode rod 9 comes into contact with condensate to the time when the electrode rod 8 comes into contact with the condensate to the following counter, and a pulse signal. A counter 13 that receives and counts the value (time value) received from the counter 13, and a multiplication/division operation that calculates the flow rate per unit time by multiplying and dividing the volume between the electrode rods 8 and 9, which has been determined in advance by the received value (time value) from the counter 13. 14, and a result display 15 for displaying or recording the received value from the multiplier/divider 14. In the figure, arrows indicate signals from electrode rods 8 and 9.

本実施例の作用を説明する。復水を測定する前
にバルブ16を閉じる。復水は流入口2から室4
内に流入して溜り始める。室4内の復水位がLに
達した時、電極棒9は復水に接して時間測定手段
10に信号を送る。ゲート部11はこれより基準
発振器12からの信号を計数器13に送る。室4
内の復水位がHに達した時、電極棒8は復水に接
して時間測定手段10に信号を送る。ゲート部1
1はこれにより基準発振器12からの信号を計数
器13に送ることを停止する。乗除算器14はL
―H間に達するまでの所定時間と、L―H間の容
積を乗除算して単位時間当りの流量を計算し、結
果表示器15はこの流量を表示又は記録する。
The operation of this embodiment will be explained. Close valve 16 before measuring condensate. Condensate flows from inlet 2 to chamber 4
It flows inside and begins to accumulate. When the condensate level in the chamber 4 reaches L, the electrode rod 9 contacts the condensate and sends a signal to the time measuring means 10. The gate section 11 then sends the signal from the reference oscillator 12 to the counter 13. room 4
When the condensate level within reaches H, the electrode rod 8 contacts the condensate and sends a signal to the time measuring means 10. Gate part 1
1 thereby stops sending the signal from the reference oscillator 12 to the counter 13. The multiplier/divider 14 is L
The flow rate per unit time is calculated by multiplying and dividing the predetermined time until reaching the interval between L and H by the volume between L and H, and the result display 15 displays or records this flow rate.

本実施例は、タンク1、電極棒8,9、バルブ
16及び時間測定手段10から成り、構造が簡単
で小形化できる。而も、復水位がHまで上昇した
際の総容積が分つている場合には、バルブ16の
閉弁直後から時間測定手段10を作動させ、電極
棒9を省くこともできる。復水の流量を測定する
際、バルブ16は閉弁し、室4は蒸気系と同圧に
なつている為、復水は室4内で再蒸気を起こさ
ず、従つて復水の再蒸発による誤差なく正確に測
定できる。また、タンク1は保温され、大気中へ
の放熱が少ないので、タンク1内の蒸気が凝縮し
て復水量を増やし、測定誤差を生じることもな
い。更に、測定流量は時間測定手段10の結果表
示器15に表示又は記録され、測定者が計算する
必要が全くなく、取り扱いが容易である。
This embodiment consists of a tank 1, electrode rods 8, 9, a valve 16, and a time measuring means 10, and has a simple structure and can be made compact. However, if the total volume when the condensate level rises to H is known, the time measuring means 10 can be operated immediately after the valve 16 is closed, and the electrode rod 9 can be omitted. When measuring the flow rate of condensate, the valve 16 is closed and the chamber 4 is at the same pressure as the steam system, so the condensate does not re-steam in the chamber 4, and therefore the condensate does not re-evaporate. Accurate measurements can be made without any errors caused by Furthermore, since the tank 1 is kept warm and little heat is radiated into the atmosphere, the steam in the tank 1 does not condense to increase the amount of condensed water and cause measurement errors. Furthermore, the measured flow rate is displayed or recorded on the result display 15 of the time measuring means 10, and there is no need for the measurer to calculate it, making it easy to handle.

本実施例に於いては、スチームトラツプ31が
流出口3側に配されている為、測定を行う前にバ
ルブ16を開き、タンク1内を空にする様な場合
に於いて、復水発生側6と復水流出側の間の大き
な圧力差により、復水発生側6の復水が全て流出
し、通常の復水発生状態と異なる状態で復水の流
量を測定することを防止できる。即ち、スチーム
トラツプ31はタンク1内を復水発生側6とほぼ
同程度の圧力状態に保ち、復水発生側6を通常の
状態に維持して流量測定を可能にする。同時に、
復水発生側6から不必要に蒸気が流出することも
防止できる。
In this embodiment, since the steam trap 31 is placed on the outlet 3 side, when the valve 16 is opened and the tank 1 is emptied before measurement, the condensate can be removed. Due to the large pressure difference between the generation side 6 and the condensate outflow side, all of the condensate on the condensate generation side 6 flows out, making it possible to prevent the flow rate of condensate from being measured in a state different from the normal condensate generation state. . That is, the steam trap 31 maintains the pressure inside the tank 1 at approximately the same pressure as the condensate generation side 6, and maintains the condensate generation side 6 in a normal state to enable flow rate measurement. at the same time,
It is also possible to prevent unnecessary steam from flowing out from the condensate generation side 6.

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

第1図は本発明の一実施例の復水用流量計の断
面図、第2図は時間測定手段の概略ブロツク図で
ある。 1…タンク、2…流入口、3…流出口、4…復
水溜り室、8,9…電極棒、10…時間測定手
段、11…ゲート部、12…基準発振器、13…
計数器、14…乗除算器、15…結果表示器、3
1…スチームトラツプ。
FIG. 1 is a sectional view of a condensate flow meter according to an embodiment of the present invention, and FIG. 2 is a schematic block diagram of a time measuring means. DESCRIPTION OF SYMBOLS 1...tank, 2...inlet, 3...outlet, 4...condensate reservoir chamber, 8, 9...electrode rod, 10...time measuring means, 11...gate section, 12...reference oscillator, 13...
Counter, 14... Multiplier/divider, 15... Result display, 3
1...Steam trap.

Claims (1)

【特許請求の範囲】 1 内部に定量の復水を溜めることができかつこ
れを検出できる様に形成されたタンク、蒸気系に
接続し蒸気系内で発生した復水をタンク内に導く
様にタンクの上部に開口して設けられた流入口、
タンク内に溜つた復水を外部に流出させる様にタ
ンクの下部に開口して設けられた流出口、タンク
内に溜つた復水を自動的に排出する様に流出口側
に配されたスチームトラツプ、タンク内の復水の
貯溜及び流出を制御する様にスチームトラツプの
下流側に配された弁手段、及びタンク内に定量の
復水が溜る時間を測定する時間測定手段から成
り、復水の溜つた量とその所要時間とを乗除計算
して復水の流量を測定する復水用流量計。 2 特許請求の範囲第1項記載のものに於いて、
時間測定手段は、基準発振器、基準発振器からの
発振信号を受信し計数する計数器、及び基準発振
器と計数器の間に介在されタンク内に定量の復水
が溜る間のみ発振振号を計数器に受信させるゲー
ト部を有することを特徴とする復水用流量計。 3 特許請求の範囲第2項記載のものに於いて、
時間測定手段は、基準発振器、計数器及びゲート
部の他、計数器からの計数値と復水の溜つた量と
を乗除計算し流量に換算する乗除算器、及びその
流量を表示又は記録する結果表示器を有すること
を特徴とする復水用流量計。
[Claims] 1. A tank formed to be able to store and detect a fixed amount of condensate inside, and connected to a steam system so as to guide condensate generated in the steam system into the tank. An inlet opening at the top of the tank,
An outlet is provided at the bottom of the tank to drain the condensate accumulated in the tank to the outside, and a steam outlet is placed on the outlet side to automatically discharge the condensate accumulated in the tank. A trap, a valve means disposed downstream of the steam trap to control the accumulation and outflow of condensate in the tank, and a time measuring means for measuring the time for a certain amount of condensate to accumulate in the tank, A condensate flow meter that measures the flow rate of condensate by multiplying and dividing the accumulated amount of condensate by the time required. 2 In what is stated in claim 1,
The time measurement means includes a reference oscillator, a counter that receives and counts oscillation signals from the reference oscillator, and a counter that is interposed between the reference oscillator and the counter and that counts the oscillation signal only while a certain amount of condensate is accumulated in the tank. 1. A condensate flowmeter characterized by having a gate section for receiving signals from the condensate. 3 In what is stated in claim 2,
In addition to the reference oscillator, the counter, and the gate, the time measurement means includes a multiplier/divider that multiplies and divides the counted value from the counter and the accumulated amount of condensate and converts it into a flow rate, and displays or records the flow rate. A condensate flow meter characterized by having a result display.
JP9186380A 1980-07-04 1980-07-04 Flow meter for condensed water Granted JPS5717819A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9186380A JPS5717819A (en) 1980-07-04 1980-07-04 Flow meter for condensed water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9186380A JPS5717819A (en) 1980-07-04 1980-07-04 Flow meter for condensed water

Publications (2)

Publication Number Publication Date
JPS5717819A JPS5717819A (en) 1982-01-29
JPS6230366B2 true JPS6230366B2 (en) 1987-07-02

Family

ID=14038384

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9186380A Granted JPS5717819A (en) 1980-07-04 1980-07-04 Flow meter for condensed water

Country Status (1)

Country Link
JP (1) JPS5717819A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5696526B2 (en) * 2011-02-24 2015-04-08 三浦工業株式会社 Steam consumption measuring device
JP6006981B2 (en) * 2012-05-25 2016-10-12 株式会社テイエルブイ Drain flow meter
JP6380170B2 (en) * 2015-03-05 2018-08-29 住友金属鉱山株式会社 Thermal energy loss evaluation method for steam piping

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5548408Y2 (en) * 1975-12-04 1980-11-12

Also Published As

Publication number Publication date
JPS5717819A (en) 1982-01-29

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