JPH0227222A - Flow rate measuring apparatus - Google Patents

Flow rate measuring apparatus

Info

Publication number
JPH0227222A
JPH0227222A JP17787388A JP17787388A JPH0227222A JP H0227222 A JPH0227222 A JP H0227222A JP 17787388 A JP17787388 A JP 17787388A JP 17787388 A JP17787388 A JP 17787388A JP H0227222 A JPH0227222 A JP H0227222A
Authority
JP
Japan
Prior art keywords
flow rate
space
steam
inlet
passage
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
JP17787388A
Other languages
Japanese (ja)
Other versions
JPH0663806B2 (en
Inventor
Mamoru Nagase
守 永瀬
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 JP17787388A priority Critical patent/JPH0663806B2/en
Publication of JPH0227222A publication Critical patent/JPH0227222A/en
Publication of JPH0663806B2 publication Critical patent/JPH0663806B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To enable accurate measurement of a condenser flow rate and a steam flow rate by arranging hot-wire type flow rate measuring elements in a space for passage of gas and a space for passage for liquid respectively. CONSTITUTION:Hot-wire type flow rate measuring elements 9 and 10 are arranged respectively in a space 7 for passage of gas and a space 8 for passage of liquid having both ends thereof connected to a power source through an output terminal. A temperature sensor 12 is mounted to correct a temperature due to a stream pressure at the top of an inlet 2. With such an arrangement, a condenser at the inlet 2 enters a measuring chamber 5 and flows to a drain space 6 through the space 8 to measure a flow rate of a condenser passing through the space 8 with the element 10. In case a float 11 suffers a steam leak, steam of the measuring chamber 5 leaks out to an outlet 3 from a space 6 passing through the space 7. A flow rate of the steam passing through the space 7 is measured with the element 9, thereby enabling the determining of a correct condenser flow rate and steam flow rate.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は蒸気の輸送管、蒸気使用機器に発生した復水を
導出する復水管などの蒸気管を流れる復水の量を測定す
る流量測定装置に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a flow rate measuring device for measuring the amount of condensate flowing through steam pipes such as steam transport pipes and condensate pipes that lead out condensate generated in steam-using equipment. .

蒸気管を流れる蒸気の流量を測定すれば、蒸気使用機器
で消費する蒸気の量が判り、蒸気使用機器の加熱効率を
改善するデータが得られる。しかしながら、蒸気は圧力
変動を受けると比容積が大きく変化するので、その流量
測定は極めて困難であった。
Measuring the flow rate of steam flowing through steam pipes can determine the amount of steam consumed by steam-using equipment, providing data for improving the heating efficiency of steam-using equipment. However, since the specific volume of steam changes greatly when it is subjected to pressure fluctuations, it has been extremely difficult to measure its flow rate.

従来の技術 そこで、本出願人は圧力変化が生じないようにして復水
の流量を測定する装置の開発を行ってきた。その原理は
、ケーシングで流体の入口と出口を形成し、ケーシング
内に仕切壁を立てて、その人口側に測定室を、出口側に
排水空間を形成し、測定室と排水空間を連通する空間を
仕切壁の上方に形成し、仕切壁に円形の孔や縦長のスリ
ット等のセキ孔を開け、装置の下流側にスチームトラッ
プ等の復水を自動的に排出する弁手段を配置し、仕切壁
の上流空間の液位を検出してセキ孔を通過する復水の流
量を求めるものである。
BACKGROUND OF THE INVENTION Therefore, the applicant has developed an apparatus for measuring the flow rate of condensate without causing pressure changes. The principle is that a casing forms the inlet and outlet of the fluid, a partition wall is erected inside the casing, a measurement chamber is formed on the population side, and a drainage space is formed on the exit side, and a space is created that communicates the measurement chamber and the drainage space. is formed above the partition wall, holes such as circular holes or vertical slits are made in the partition wall, and a valve means for automatically discharging condensate such as a steam trap is placed downstream of the device. The liquid level in the upstream space of the wall is detected to determine the flow rate of condensate passing through the drain hole.

この場合、測定室と排水空間は仕切壁の上方で連通して
いるので、また、下流側にはスチームトラップ等の蒸気
は逃さずに復水を自動的に排出する弁が取り付(プでお
るから、測定室も排水空間も、入口側の蒸気と同じ圧力
である。従って、復水は再蒸発を伴わずに仕切壁を通過
する。
In this case, since the measurement chamber and the drainage space communicate above the partition wall, a valve such as a steam trap is installed on the downstream side to automatically discharge condensate without letting steam escape. Therefore, both the measuring chamber and the drainage space have the same pressure as the steam on the inlet side.Therefore, the condensate passes through the partition wall without being re-evaporated.

測定室の液位とセキ孔を通過する流量との間には所定の
関係があるから、この関係を予め求めてあき、液位を測
って、セキ孔を通過する復水の流木発明が解決しようと
する間開X この場合、測定室の液面は流入する流体で波立つので、
正確な復水流量を測定することができない。また、スチ
ームトラップ等の弁手段が蒸気漏洩を起こす場合には、
その蒸気漏洩量分は測定することができない。
Since there is a predetermined relationship between the liquid level in the measurement chamber and the flow rate passing through the drain hole, the invention of the driftwood method for condensate water by determining this relationship in advance, measuring the liquid level, and passing through the drain hole solved the problem. In this case, the liquid level in the measurement chamber will ripple due to the inflowing fluid, so
Unable to measure accurate condensate flow rate. In addition, if a valve means such as a steam trap causes steam leakage,
The amount of steam leakage cannot be measured.

従って、本発明の技術的課題は、正確な復水流量及び蒸
気流量を求めることができるようにすることでおる。
Therefore, the technical problem of the present invention is to enable accurate condensate flow rate and steam flow rate to be determined.

傅 閤題点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、ケーシングで流体の入口と出口を形成し、ケ
ーシング内に仕切壁を立てて、その入口側に測定室を、
出口側に排水空間を形成し、仕切壁の入口の開口位置よ
りも上部に気体通過用空間を、仕切壁の出口の開口位置
よりも下部に液体通過用空間を形成して測定室と排水空
間を連通し、気体通過用空間と液体通過用空間にそれぞ
れ熱線式流量測定素子を配置した、ものでおる。
Means for Solving the Problems The technical means of the present invention taken to solve the above technical problems is to form a fluid inlet and an outlet in a casing, and erect a partition wall in the casing. There is a measurement room on the entrance side,
A drainage space is formed on the exit side, a space for gas passage is formed above the opening position of the inlet of the partition wall, and a space for liquid passage is formed below the opening position of the exit of the partition wall, thereby forming a measurement chamber and a drainage space. A hot wire type flow rate measuring element is arranged in each of the gas passage space and the liquid passage space.

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

スチームトラップ等の復水を自動的に排出する弁手段は
出口の二次側、あるいは出口の一次側の排水空間に配置
される。この弁手段の上流側、即ち、仕切壁の前後は同
じ圧力である。入口の復水は測定室に入り、液体通過用
空間を通って排水空間に流出する。熱線式流量測定素子
は、通電して自己発熱状態に保つと、流体の通過により
温度降下を生じてその抵抗値が減少する。この温度変化
は熱線の放熱量を示し、これが流体の通過流量に比例す
ることを利用して上記抵抗値変化あるいは端子電圧変化
から流体の流量を検知するものである。液体通過用空間
に配置した熱線式流量測定素子で、そこを通過する復水
流量を測定する。
Valve means for automatically discharging condensate, such as a steam trap, is arranged in the drainage space on the secondary side of the outlet or on the primary side of the outlet. The pressure is the same upstream of this valve means, ie before and after the partition wall. The condensate at the inlet enters the measuring chamber and flows out through the liquid passage space into the drainage space. When a hot wire flow rate measuring element is energized and maintained in a self-heating state, the temperature drops due to the passage of fluid and its resistance value decreases. This temperature change indicates the amount of heat dissipated by the hot wire, and by utilizing the fact that this is proportional to the flow rate of the fluid passing through, the flow rate of the fluid is detected from the change in the resistance value or the change in the terminal voltage. A hot wire flow rate measurement element placed in the liquid passage space measures the flow rate of condensate passing through it.

弁手段が蒸気漏洩を起こしている場合は、測定室の蒸気
が仕切壁上部の気体通過用空間を通って排水空間に流れ
る。気体通過用空間に配した!I!線式流最測定素子で
、そこを通過する蒸気流量を測定することができる。
If the valve means is leaking steam, the steam in the measurement chamber flows into the drainage space through the gas passage space at the top of the partition wall. Arranged in the space for gas passage! I! A linear flow measurement element can measure the flow rate of steam passing through it.

熱線式流量測定素子で流量を測定するので、波立ちの影
響を受けずに測定することができる。
Since the flow rate is measured using a hot wire type flow rate measurement element, the flow rate can be measured without being affected by ripples.

発明の効果 本発明は下記の特有の効果を生じる。Effect of the invention The present invention produces the following unique effects.

上記のように本発明によれば、正確な復水流量及び蒸気
流量を求めることができる。
As described above, according to the present invention, accurate condensate flow rate and steam flow rate can be determined.

また、従来は蒸気流量と復水流量を個別にそれぞれ蒸気
流量計と復水流量計で測定していたが、本発明によれば
、1つの計器で蒸気流量と復水流量をしかも同時に測定
することができる。
Furthermore, in the past, steam flow rate and condensate flow rate were measured separately using a steam flow meter and a condensate flow meter, but according to the present invention, steam flow rate and condensate flow rate can be measured simultaneously with one instrument. be able to.

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(第
1図参照)。
Embodiment An embodiment illustrating a specific example of the above technical means will be described (see FIG. 1).

ケーシング1の上部に入口2を、下部に出口3を形成す
る。ケーシング1に仕切壁4を形成して、入口2側に測
定室5を、出口3側に排水空間6を形成する。仕切壁4
の入口2の開口位置よりも上部に気体通過用空間7を、
出口3の開口位置よりも下部に液体通過用空間8を開け
て、測定室5と排水空間6を連通する。
An inlet 2 is formed in the upper part of the casing 1, and an outlet 3 is formed in the lower part. A partition wall 4 is formed in the casing 1 to form a measurement chamber 5 on the inlet 2 side and a drainage space 6 on the outlet 3 side. Partition wall 4
A gas passage space 7 is provided above the opening position of the inlet 2,
A liquid passage space 8 is opened below the opening position of the outlet 3 to communicate the measurement chamber 5 and the drainage space 6.

気体通過用空間7に熱線式流量測定素子9を、液体通過
用空間8に熱線式流量測定素子10を配置する。測定素
子9.10はそれぞれ、その両端部が出力端子を介して
電源に接続されている。
A hot wire flow rate measurement element 9 is placed in the gas passage space 7, and a hot wire flow rate measurement element 10 is placed in the liquid passage space 8. Each measuring element 9.10 is connected at both ends to a power supply via an output terminal.

排水空間6に出口3を開閉する排水弁としてのフロート
11が自由状態で収容されている。フロート11は液位
と共に浮上降下して出口3を開閉し、復水のみを排出す
るものである。
A float 11 serving as a drain valve for opening and closing the outlet 3 is housed in the drain space 6 in a free state. The float 11 ascends and descends with the liquid level to open and close the outlet 3 and discharge only condensate.

入口2の上部に温度センサ12を取り付ける。A temperature sensor 12 is attached to the upper part of the inlet 2.

温度センサ12は蒸気圧力による温度補正を行なうため
のものである。
The temperature sensor 12 is for temperature correction based on steam pressure.

入口2の復水は測定室5に入り、液体通過用空間8を通
って排水空間6に流れる。この空間8を通過する復水流
量を熱線式流量測定素子10で測定する。フロート11
が蒸気漏洩を起こしている場合は、測定子5の蒸気が気
体通過用空間7を通って排水空間6から出口3に流出す
る。この空間7を通過する蒸気流量を熱線式流量測定素
子9で測定する。
The condensate at the inlet 2 enters the measuring chamber 5 and flows through the liquid passage space 8 to the drainage space 6. The flow rate of condensate passing through this space 8 is measured by a hot wire flow rate measuring element 10. float 11
If steam leakage occurs, the steam in the probe 5 passes through the gas passage space 7 and flows out from the drainage space 6 to the outlet 3. The flow rate of steam passing through this space 7 is measured by a hot wire type flow rate measuring element 9.

上記の実施例に於いては、排水弁手段を出口の一次側の
ケーシング内に配置したので、排水弁手段と流量測定装
置を別々に配管する必要がない。
In the above embodiment, since the drain valve means is disposed within the casing on the primary side of the outlet, there is no need to provide separate piping for the drain valve means and the flow rate measuring device.

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

第1図は本発明の実施例の流量測定装置の断面図である
。 1:ケーシング    2:入口 3:出口       4:仕切壁 5:測定子      6:排水空間 7:気体通過用空間  8:液体通過用空間9.10:
熱線式流量測定素子 10熱vJl 測免tケ 5スロ
FIG. 1 is a sectional view of a flow rate measuring device according to an embodiment of the present invention. 1: Casing 2: Inlet 3: Outlet 4: Partition wall 5: Measuring element 6: Drainage space 7: Space for gas passage 8: Space for liquid passage 9.10:
Hot wire flow rate measuring element 10 heat vJl measurement and measurement tke 5 slots

Claims (1)

【特許請求の範囲】[Claims] 1、ケーシングで流体の入口と出口を形成し、ケーシン
グ内に仕切壁を立てて、その入口側に測定室を、出口側
に排水空間を形成し、仕切壁の入口の開口位置よりも上
部に気体通過用空間を、仕切壁の出口の開口位置よりも
下部に液体通過用空間を形成して測定室と排水空間を連
通し、気体通過用空間と液体通過用空間にそれぞれ熱線
式流量測定素子を配置した流量測定装置。
1. Form the inlet and outlet of the fluid with the casing, set up a partition wall inside the casing, form a measurement chamber on the inlet side, and a drainage space on the outlet side, above the opening position of the inlet of the partition wall. A gas passage space is formed with a liquid passage space below the opening position of the outlet of the partition wall to connect the measurement chamber and the drainage space, and a hot wire flow rate measuring element is installed in each of the gas passage space and the liquid passage space. A flow rate measuring device with a
JP17787388A 1988-07-15 1988-07-15 Flow measuring device Expired - Fee Related JPH0663806B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17787388A JPH0663806B2 (en) 1988-07-15 1988-07-15 Flow measuring device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17787388A JPH0663806B2 (en) 1988-07-15 1988-07-15 Flow measuring device

Publications (2)

Publication Number Publication Date
JPH0227222A true JPH0227222A (en) 1990-01-30
JPH0663806B2 JPH0663806B2 (en) 1994-08-22

Family

ID=16038553

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17787388A Expired - Fee Related JPH0663806B2 (en) 1988-07-15 1988-07-15 Flow measuring device

Country Status (1)

Country Link
JP (1) JPH0663806B2 (en)

Also Published As

Publication number Publication date
JPH0663806B2 (en) 1994-08-22

Similar Documents

Publication Publication Date Title
JPS6347596A (en) Measuring device for quantity of leakage of steam of steam trap
JPH0227222A (en) Flow rate measuring apparatus
FI90593B (en) Device for measuring steam leakage in a steam trap
KR101767415B1 (en) Two-phase Fluid Sensor
JPH0511892B2 (en)
JPH0479565B2 (en)
JPH0338480B2 (en)
RU2164667C2 (en) Plant for stand study of flow characteristics of hydraulic resistances
JPH01105098A (en) Flow-rate measuring device
JPS645199B2 (en)
JPH0310480Y2 (en)
JPH0227223A (en) Flow rate measuring apparatus
US1677189A (en) Meter for fluids
JPH0337679B2 (en)
JPH05164672A (en) Wetness measuring apparatus
JPH02269913A (en) Differential pressure type steam flowmeter
JPH11344595A (en) Feed water heater drain system
JPS63252227A (en) Discrete measurement of quantity of discharge heat
JPS5830221Y2 (en) water quality tester
JP2003075317A (en) Steam dryness measurement device
CN110686732A (en) Flow constant temperature and pressure measuring device for parts
JPS5813295A (en) Measuring device for quantity of steam leaking from steam trap
JPS59134401A (en) Detector for leakage of feedwater heater
JPS6246814B2 (en)
JPH0654160B2 (en) Steam trap with vapor leakage measurement mechanism

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees