Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS6246815B2 - - Google Patents
[go: Go Back, main page]

JPS6246815B2 - - Google Patents

Info

Publication number
JPS6246815B2
JPS6246815B2 JP57230876A JP23087682A JPS6246815B2 JP S6246815 B2 JPS6246815 B2 JP S6246815B2 JP 57230876 A JP57230876 A JP 57230876A JP 23087682 A JP23087682 A JP 23087682A JP S6246815 B2 JPS6246815 B2 JP S6246815B2
Authority
JP
Japan
Prior art keywords
gas
pressure
measured
volumetric
conduit
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
JP57230876A
Other languages
Japanese (ja)
Other versions
JPS59116015A (en
Inventor
Yoshiaki Emura
Yoshinori Takeda
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.)
Toyota Motor Corp
Original Assignee
Toyota Motor Corp
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 Toyota Motor Corp filed Critical Toyota Motor Corp
Priority to JP57230876A priority Critical patent/JPS59116015A/en
Publication of JPS59116015A publication Critical patent/JPS59116015A/en
Publication of JPS6246815B2 publication Critical patent/JPS6246815B2/ja
Granted legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01MTESTING STATIC OR DYNAMIC BALANCE OF MACHINES OR STRUCTURES; TESTING OF STRUCTURES OR APPARATUS, NOT OTHERWISE PROVIDED FOR
    • G01M3/00Investigating fluid-tightness of structures
    • G01M3/02Investigating fluid-tightness of structures by using fluid or vacuum
    • G01M3/26Investigating fluid-tightness of structures by using fluid or vacuum by measuring rate of loss or gain of fluid, e.g. by pressure-responsive devices, by flow detectors
    • G01M3/32Investigating fluid-tightness of structures by using fluid or vacuum by measuring rate of loss or gain of fluid, e.g. by pressure-responsive devices, by flow detectors for containers, e.g. radiators
    • G01M3/3236Investigating fluid-tightness of structures by using fluid or vacuum by measuring rate of loss or gain of fluid, e.g. by pressure-responsive devices, by flow detectors for containers, e.g. radiators by monitoring the interior space of the containers

Landscapes

  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Measuring Volume Flow (AREA)

Description

【発明の詳細な説明】 本発明は圧縮空気の如き気体を貯容し又は搬送
する圧力タンク、導管、接続部材の如き被測定対
象物からの気体の漏洩量を測定する方法及び装置
に係る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for measuring the amount of gas leaking from an object to be measured, such as a pressure tank, conduit, or connecting member that stores or conveys a gas such as compressed air.

圧力タンクの如くそれ自身の重量及びその内部
に貯容された気体の重量変化を測定することが困
難であり又は不可能である被測定対象物内より漏
洩する気体の漏洩量を測定する方法の一つとし
て、従来より放置法が知られている。この方法に
於ては、被測定対象物の使用時に於ける気体の圧
力に等しい圧縮空気の如き気体を被測定対象物内
に封入し、漏洩により被測定対象物内の気体の圧
力が低下する際の圧力低下率を求め下記の式に従
つて気体の圧力がP0である場合に於ける洩れ重量
として単位時間当りの気体の漏洩量が算出され
る。
A method for measuring the amount of gas leaking from an object to be measured, such as a pressure tank, in which it is difficult or impossible to measure changes in its own weight and the weight of the gas stored therein. One method that has been known is the leaving method. In this method, a gas such as compressed air that is equal to the pressure of the gas when the object is in use is sealed inside the object to be measured, and the pressure of the gas inside the object decreases due to leakage. The rate of pressure drop at that time is determined, and the amount of gas leaked per unit time is calculated as the leakage weight when the gas pressure is P 0 according to the following formula.

(dG/dt)P0=V/RT・dP/dt ……(A) ここに V=被測定対象物の容積 R=気体定数 T=気体の絶対温度 dP/dt=圧力P0に於ける圧力低下率 しかし一般には圧力タンクの如き被測定対象物
の容積Vが不明であることが多く、またその容積
を測定したり計算によつて求めることが困難であ
るため、上述の如き従来の放置法により被測定対
象物内より漏洩する気体の漏洩量を求めることは
できない。
(dG/dt) P0 = V/RT・dP 0 /dt ...(A) Here, V = Volume of the object to be measured R = Gas constant T = Absolute temperature of gas dP 0 /dt = Pressure at P 0 However, in general, the volume V of an object to be measured such as a pressure tank is often unknown, and it is difficult to measure or calculate the volume. It is not possible to determine the amount of gas leaking from within the object to be measured using the leaving method.

本発明は、気体の漏洩量を測定されるべき被測
定対象物の容積が不明である場合に於ても、その
内部より漏洩する気体の漏洩量を高精度に測定す
ることのできる方法及び装置を提供することを目
的としている。
The present invention provides a method and an apparatus that can accurately measure the amount of gas leaking from the inside of an object to be measured, even when the volume of the object to be measured is unknown. is intended to provide.

かかる目的は、本発明によれば、容積がVxで
ある被測定対象物内より漏洩する気体の漏洩量を
測定する方法にして、それぞれ互いに異なる既知
の容積V1及びV2を有する第一及び第二の容器
と、容積がV3であり前記被測定対象物と前記第
一の容器とを連通接続して第一の容積系を構成す
る第一の導管と、容積がV4であり前記被測定対
象物と前記第二の容器とを連通接続して第二の容
積系を構成する第二の導管と、前記第一及び第二
の容積系へ加圧された気体を供給する加圧気体源
と、前記第一の容積系と前記加圧気体源との連通
を遮断する第一の弁装置と、前記第二の容積系と
前記加圧気体源との連通を遮断する第二の弁装置
と、前記第一及び第二の容積系内の気体の圧力を
連続的に測定する測定装置とを有する気体漏洩量
測定装置を用い、 前記第一の導管にて前記被測定対象物と前記第
一の容器とを連通接続して前記第一の容積系を形
成し、該第一の容積系内部に前記加圧気体源より
加圧された気体を導入し、前記第一の容積系内の
気体の圧力が所定の圧力P1に到達した時点で前記
第一の弁装置を閉弁させ、前記測定装置により前
記第一の容積系内の気体の圧力変化を測定し、前
記第一の容積系内の気体の圧力が所定の圧力P0
到達した時点に於ける圧力低下率dP/dtを求め、 前記第二の導管にて前記被測定対象物と前記第
二の容器とを連通接続して前記第二の容積系を形
成し、該第二の容積系内部に前記加圧気体源より
加圧された気体を導入し、前記第二の容積系内の
気体の圧力が所定の圧力P2に到達した時点で前記
第二の弁装置を閉弁させ、前記測定装置により前
記第二の容積系内の気体の圧力変化を測定し、前
記第二の容積系内の気体の圧力が所定の圧力P0
到達した時点に於ける圧力低下率dP′/dtを求め
、 これにより下記の式(1)、式(2)、及び式(3)を連立
させて前記被測定対象物内の気体の圧力がP0であ
る時点に於ける気体の単位時間当りの漏洩量を洩
れ重量(dG/dt)P0として下記の式(4)より求める
方 法、 (dG/dt)P0=(V+V+Vx)/RT・d
/dt……(1) (dG/dt)P0=(V+V+Vx)/RT・d
′/dt……(2) V4=V3+k(k:一定) ……(3) ここに R=気体定数 T=気体の絶対温度 及び被測定対象物内より漏洩する気体の漏洩量
を測定する装置にして、互いに異なる既知の容積
を有する第一及び第二の容器と、前記被測定対象
物と前記第一の容器とを連通接続して第一の容積
系を構成する第一の導管と、前記被測定対象物と
前記第二の容器とを連通接続して第二の容積系を
構成する第二の導管と、前記第一及び第二の容積
系へ加圧された気体を供給する加圧気体源と、前
記第一の容積系と前記加圧気体源との連通を遮断
する第一の弁装置と、前記第二の容積系と前記加
圧気体源との連通を遮断する第二の弁装置と、前
記被測定対象物内の気体の圧力を連続的に測定す
る測定装置とを有する装置によつて達成される。
According to the present invention, the present invention provides a method for measuring the amount of gas leaking from an object to be measured whose volume is Vx . a second container, a first conduit having a volume of V 3 and communicatively connecting the object to be measured and the first container to form a first volume system; a second conduit that communicates and connects the object to be measured and the second container to constitute a second volume system; and pressurization for supplying pressurized gas to the first and second volume systems. a gas source, a first valve device for blocking communication between the first volumetric system and the pressurized gas source, and a second valve device for blocking communication between the second volumetric system and the pressurized gas source. Using a gas leakage measuring device having a valve device and a measuring device that continuously measures the pressure of the gas in the first and second volumetric systems, the first volumetric system is formed by communicating with the first container, the pressurized gas from the pressurized gas source is introduced into the first volumetric system, and the first volumetric system is When the pressure of the gas in the first volume system reaches a predetermined pressure P1 , the first valve device is closed, the pressure change of the gas in the first volume system is measured by the measuring device, and the first valve device is closed. Determine the pressure drop rate dP 0 /dt at the time when the pressure of the gas in the volumetric system reaches a predetermined pressure P 0 , and connect the object to be measured and the second container through the second conduit. are connected in communication to form the second volumetric system, pressurized gas from the pressurized gas source is introduced into the second volumetric system, and the pressure of the gas in the second volumetric system is increased. When a predetermined pressure P2 is reached, the second valve device is closed, the pressure change of the gas in the second volume system is measured by the measurement device, and the gas in the second volume system is The pressure drop rate dP 0 '/dt at the point when the pressure reaches the predetermined pressure P 0 is determined, and from this, the following equations (1), (2), and (3) are combined to form the above equation. A method of calculating the amount of gas leaked per unit time when the pressure of the gas inside the object to be measured is P 0 using the following formula (4), where the leakage weight (dG/dt) P0 is calculated as (dG/dt). ) P0 = (V 1 +V 3 +Vx)/RT・d
P 0 /dt...(1) (dG/dt) P0 = (V 2 +V 4 +Vx)/RT・d
P 0 '/dt...(2) V 4 =V 3 +k (k: constant)...(3) Here, R=gas constant T=absolute temperature of gas and an apparatus for measuring the amount of gas leaking from inside an object to be measured, comprising first and second containers having mutually different known volumes, and the object to be measured. A first conduit that connects the object to be measured and the first container to form a first volume system; and a first conduit that connects the object to be measured and the second container to form a second volume system. A second conduit constituting the system, a pressurized gas source supplying pressurized gas to the first and second volumetric systems, and communication between the first volumetric system and the pressurized gas source. a first valve device for blocking communication between the second volumetric system and the pressurized gas source; and a second valve device for continuously measuring the pressure of the gas in the object to be measured. This is accomplished by a device having a measuring device.

本発明による気体漏洩量測定方法によれば、気
体の漏洩量を測定されるべき被測定対象物を含み
互いに容積の異なる二つの容積系が構成され、そ
れぞれについて放置法が適用され、それぞれにつ
いて上述の式(A)の関係が求められ、それらを連立
方程式としてその解である単位時間当りの気体の
漏洩量が求められるので、被測定対象物の容積が
不明である場合にも、その被測定対象物内より漏
洩する気体の漏洩量を簡単に且正確に測定するこ
とができる。また本発明による方法によれば、前
述の連立方程式の他の一つの解として被測定対象
物の容積をも簡単に且正確に求めることができ
る。
According to the method for measuring the amount of gas leakage according to the present invention, two volume systems including the object to be measured whose amount of gas leakage is to be measured and having different volumes are configured, and the leaving method is applied to each of them, and the above-mentioned method is applied to each volume system. The relationship in Equation (A) is determined, and the solution is the gas leakage amount per unit time, which is a simultaneous equation. Therefore, even if the volume of the object to be measured is unknown, The amount of gas leaking from inside the object can be easily and accurately measured. Furthermore, according to the method according to the present invention, the volume of the object to be measured can also be easily and accurately determined as another solution to the above-mentioned simultaneous equations.

また本発明による気体漏洩量測定装置によれ
ば、上述の如き気体漏洩量測定方法を能率良く実
施することができる。
Further, according to the gas leakage measuring device according to the present invention, the method for measuring the amount of gas leakage as described above can be carried out efficiently.

尚本発明の方法及び装置に於ては、k=0、即
ち第一の導管の容積V3と第二の導管の容積V4
が等しくされることが好ましく、この場合には連
立方程式を解く際に第一の導管の容積と第二の導
管の容積とが相違することを補正する必要がなく
なる。また本発明による方法及び装置に於ては、
一つの導管を第一の導管及び第二の導管として共
用し、その導管に第一及び第二の容器を順次接続
することにより漏洩量の測定が行われることが好
ましく、この場合には共用される導管の容積が不
明であつても被測定対象物内より漏洩する気体の
漏洩量を測定することができる。
In the method and apparatus of the present invention, it is preferable that k=0, that is, the volume V 3 of the first conduit and the volume V 4 of the second conduit are equal, and in this case, the simultaneous equations are When unraveling, there is no need to correct the difference in volume between the first conduit and the second conduit. Further, in the method and apparatus according to the present invention,
It is preferable to measure the amount of leakage by sharing one conduit as the first conduit and the second conduit and connecting the first and second containers to that conduit in sequence; Even if the volume of the conduit is unknown, the amount of gas leaking from within the object to be measured can be measured.

以下に添付の図を参照しつつ、本発明を実施例
について詳細に説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The invention will be explained in detail below by way of example embodiments with reference to the accompanying figures.

第1図は本発明による気体漏洩量測定装置の一
つの実施例を示す概略構成図である。図に於て、
本発明による気体漏洩量測定装置はそれぞれ互い
に異なる既知の容積V1及びV2を有する第一及び
第二の容器1及び2と、気体の漏洩量を測定され
るべき被測定対象物3と、被測定対象物3と第一
の容器1とを連通接続する第一の導管系4と、被
測定対象物3と第二の容器2とを連通接続する第
二の導管系5とを含んでいる。第一の導管系4は
一端にて被測定対象物3に連通接続される導管6
と、一端にて第一の容器1に連通接続され他端に
て導管6の他端に連通接続され途中に開閉弁7を
有する導管8とよりなつている。また第二の導管
系5は導管6と、一端にて第二の容器2に連通接
続され他端にて導管6の他端に連通接続され途中
に開閉弁9を有する導管10とよりなつている。
FIG. 1 is a schematic diagram showing one embodiment of a gas leakage measuring device according to the present invention. In the figure,
The gas leakage measuring device according to the present invention includes first and second containers 1 and 2 having known volumes V 1 and V 2 that are different from each other, and an object 3 whose gas leakage is to be measured. It includes a first conduit system 4 that communicates and connects the object to be measured 3 and the first container 1, and a second conduit system 5 that communicates and connects the object to be measured 3 and the second container 2. There is. The first conduit system 4 has a conduit 6 connected to the object to be measured 3 at one end.
and a conduit 8 which is connected to the first container 1 at one end, connected to the other end of the conduit 6 at the other end, and has an on-off valve 7 in the middle. The second conduit system 5 is composed of a conduit 6 and a conduit 10 that is connected to the second container 2 at one end, connected to the other end of the conduit 6 at the other end, and has an on-off valve 9 in the middle. There is.

導管6には導管11により圧縮空気供給源12
が連通接続されており、導管11の途中には開閉
弁13が設けられている。また導管6には導管1
4により圧力測定装置15が接続されており、圧
力測定装置15は導管6内の気体の圧力を連続的
に測定し得るようになつており、またその測定デ
ータは記録装置16により連続的に記録されるよ
うになつている。
The conduit 6 is connected to a compressed air supply source 12 by a conduit 11.
are connected to each other, and an on-off valve 13 is provided in the middle of the conduit 11. In addition, conduit 1 is connected to conduit 6.
A pressure measuring device 15 is connected by 4, and the pressure measuring device 15 can continuously measure the pressure of the gas in the conduit 6, and the measured data can be continuously recorded by a recording device 16. It is becoming more and more common.

尚上述の如く構成された気体漏洩量測定装置に
於て、第一の導管系4と、導管14と、分岐点1
7より開閉弁13までの導管11と、分岐点18
より開閉弁9までの導管10とよりなる第一の容
器系19の容積はV3であり、また第二の導管系
5と、導管14と、分岐点17より開閉弁13ま
での導管11と、分岐点18より開閉弁7までの
導管8とよりなる第二の容積系20の容積はV4
であり、V4=V3+k(k:一定)であることが
解つている。
In the gas leakage measuring device configured as described above, the first conduit system 4, the conduit 14, and the branch point 1
Conduit 11 from 7 to on-off valve 13 and branch point 18
The volume of the first container system 19 consisting of the conduit 10 from the branch point 17 to the on-off valve 9 is V 3 , and the volume of the first container system 19 consisting of the conduit 10 from the branch point 17 to the on-off valve 13 is V 3 . , the volume of the second volume system 20 consisting of the conduit 8 from the branch point 18 to the on-off valve 7 is V 4
It is understood that V 4 =V 3 +k (k: constant).

本発明による気体漏洩量測定方法は上述の如く
構成された気体漏洩量測定装置を用いて以下の如
く実施される。まず開閉弁7及び13を開弁し開
閉弁9を閉弁して第一の容器1及び被測定対象物
3などの内部に圧縮空気供給源12より圧縮空気
を導入し、導管6内の圧縮空気の圧力が所定の圧
力P1に到達した時点で開閉弁13を閉弁し、圧力
測定装置15により第一の容積系19内の圧縮空
気の圧力変化を測定し、第一の容積系19内の圧
縮空気の圧力が所定の圧力P0(P0<P1)に到達し
た時点に於ける圧力低下率dP/dtを第2図に示さ
れ ている如く記録装置16に記録された圧力変化の
グラフより圧力P0に於ける曲線の傾きとして求め
る。以上の手続により下記の式(1)の関係を求め
る。
The method for measuring the amount of gas leakage according to the present invention is carried out as follows using the gas leakage amount measuring device configured as described above. First, the on-off valves 7 and 13 are opened, the on-off valve 9 is closed, and compressed air is introduced from the compressed air supply source 12 into the first container 1 and the object to be measured 3, etc., and the compressed air in the conduit 6 is When the air pressure reaches a predetermined pressure P1 , the on-off valve 13 is closed, and the pressure measurement device 15 measures the pressure change of the compressed air in the first volume system 19. The pressure drop rate dP 0 /dt at the time when the pressure of the compressed air in the chamber reached a predetermined pressure P 0 (P 0 <P 1 ) was recorded on the recording device 16 as shown in FIG. Obtain it as the slope of the curve at pressure P 0 from the pressure change graph. Through the above procedure, the relationship expressed by equation (1) below is determined.

(dG/dt)P0=(V+V+Vx)/RT・d
/dt……(1) 同様に、開閉弁9及び13を開弁し開閉弁7を
閉弁して第二の容器2及び被測定対象物3などの
内部に圧縮空気供給源12より圧縮空気を導入
し、導管6内の圧縮空気の圧力が所定の圧力P2
到達した時点で開閉弁13を閉弁し、圧力測定装
置15により第二の容積系20内の圧縮空気の圧
力変化を測定し、第二の容積系20内の圧縮空気
の圧力が所定の圧力P0に到達した時点に於ける圧
力低下率dP′/dtを第2図に示されている如く記
録装 置16により記録された圧力変化のグラフより圧
力P0に於ける曲線の傾きとして求める。以上の手
続により下記の式(2)の関係を求める。
(dG/dt) P0 = (V 1 +V 3 +Vx)/RT・d
P 0 /dt...(1) Similarly, the on-off valves 9 and 13 are opened and the on-off valve 7 is closed to supply air from the compressed air supply source 12 to the inside of the second container 2, the object to be measured 3, etc. Compressed air is introduced, and when the pressure of the compressed air in the conduit 6 reaches a predetermined pressure P2 , the on-off valve 13 is closed, and the pressure of the compressed air in the second volume system 20 is measured by the pressure measuring device 15. The change is measured, and the pressure drop rate dP 0 '/dt at the time when the pressure of the compressed air in the second volumetric system 20 reaches a predetermined pressure P 0 is recorded using a recording device as shown in FIG. It is determined as the slope of the curve at pressure P 0 from the graph of pressure changes recorded by No. 16. Through the above procedure, the relationship expressed by equation (2) below is determined.

(dG/dt)P0=(V+V+Vx)/RT・d
/dt……(2) 前述の如く第一の容積系19の容積V3と第二
の容積系20の容積V4との間には V4=V3+k(k:一定) ……(3) の関係があり、また容積は異なつても気体の圧力
が等しい場合には洩れ重量(dG/dt)P0は等しいの で、これらの式(1)、式(2)、及び式(3)を連立させ
て、被測定対象物3内の圧縮空気の圧力がP0であ
る時点に於ける圧縮空気の単位時間当りの漏洩量
を洩れ重量(dG/dt)P0として下記の式(4)より求
め る。
(dG/dt) P0 = (V 2 +V 4 +Vx)/RT・d
P 0 /dt...(2) As mentioned above, the relationship between the volume V 3 of the first volume system 19 and the volume V 4 of the second volume system 20 is V 4 =V 3 +k (k: constant)... ...(3) exists, and even if the volumes are different, if the pressures of the gases are the same, the leakage weights (dG/dt) P0 are the same, so these equations (1), (2), and equations ( By combining 3), the leakage amount of compressed air per unit time at the time when the pressure of compressed air inside the object to be measured 3 is P0 is the leakage weight (dG/dt) P0 , and the following formula ( 4) Ask for more.

尚本発明による方法及び装置によれば、上述の
三つの式を連立させることにより、被測定対象物
3内の容積Vxを下記の式(5)により求めることも
できる。
According to the method and apparatus according to the present invention, the volume Vx inside the object to be measured 3 can also be determined by the following equation (5) by combining the above three equations.

以上に於ては本発明を特定の実施例について詳
細に説明したが、本発明はかかる実施例に限定さ
れるものではなく、本発明の範囲内にて種々の実
施例が可能であることは当業者にとつて明らかで
あろう。例えば開閉弁7及び9は分岐点18に設
けられた切換弁に置換えられてもよい。また圧縮
空気の圧力P1及びP2とP0とは同一の値であつても
よい。
Although the present invention has been described in detail with respect to specific embodiments above, the present invention is not limited to such embodiments, and it is understood that various embodiments are possible within the scope of the present invention. It will be clear to those skilled in the art. For example, the on-off valves 7 and 9 may be replaced with switching valves provided at the branch point 18. Further, the pressures P 1 and P 2 of the compressed air and P 0 may be the same value.

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

第1図は本発明による気体漏洩量測定装置の一
つの実施例を示す概略構成図、第2図は第1図に
示された気体漏洩量測定装置の記録装置により記
録された圧力Pと時間tとの関係を示すグラフで
ある。 1…第一の容器、2…第二の容器、3…被測定
対象物、4…第一の導管系、5…第二の導管系、
7…開閉弁、8…導管、9…開閉弁、10,11
…導管、12…圧縮空気供給源、13…開閉弁、
14…導管、15…圧力測定装置、16…記録装
置、17,18…分岐点、19…第一の容積系、
20…第二の容積系。
Fig. 1 is a schematic configuration diagram showing one embodiment of the gas leakage measuring device according to the present invention, and Fig. 2 is a pressure P and time recorded by the recording device of the gas leakage measuring device shown in Fig. 1. It is a graph showing the relationship with t. 1... First container, 2... Second container, 3... Measured object, 4... First conduit system, 5... Second conduit system,
7... Opening/closing valve, 8... Conduit, 9... Opening/closing valve, 10, 11
... conduit, 12 ... compressed air supply source, 13 ... on-off valve,
14... Conduit, 15... Pressure measuring device, 16... Recording device, 17, 18... Branch point, 19... First volumetric system,
20...Second volumetric system.

Claims (1)

【特許請求の範囲】 1 容積がVxである被測定対象物内より漏洩す
る気体の漏洩量を測定する方法にして、それぞれ
互いに異なる既知の容積V1及びV2を有する第一
及び第二の容器と、容積がV3であり前記被測定
対象物と前記第一の容器とを連通接続して第一の
容積系を構成する第一の導管と、容積がV4であ
り前記被測定対象物と前記第二の容器とを連通接
続して第二の容積系を構成する第二の導管と、前
記第一及び第二の容積系へ加圧された気体を供給
する加圧気体源と、前記第一の容積系と前記加圧
気体源との連通を遮断する第一の弁装置と、前記
第二の容積系と前記加圧気体源との連通を遮断す
る第二の弁装置と、前記第一及び第二の容積系内
の気体の圧力を連続的に測定する測定装置とを有
する気体漏洩量測定装置を用い、 前記第一の導管にて前記被測定対象物と前記第
一の容器とを連通接続して前記第一の容積系を形
成し、該第一の容積系内部に前記加圧気体源より
加圧された気体を導入し、前記第一の容積系内の
気体の圧力が所定の圧力P1に到達した時点で前記
第一の弁装置を閉弁させ、前記測定装置により前
記第一の容積系内の気体の圧力変化を測定し、前
記第一の容積系内の気体の圧力が所定の圧力P0
到達した時点に於ける圧力低下率dP/dtを求め、 前記第二の導管にて前記被測定対象物と前記第
二の容器とを連通接続して前記第二の容積系を形
成し、該第二の容積系内部に前記加圧気体源より
加圧された気体を導入し、前記第二の容積系内の
気体の圧力が所定の圧力P2に到達した時点で前記
第二の弁装置を閉弁させ、前記測定装置により前
記第二の容積系内の気体の圧力変化を測定し、前
記第二の容積系内の気体の圧力が所定の圧力P0
到達した時点に於ける圧力低下率dP′/dtを求め
、 これにより下記の式(1)、式(2)、及び式(3)を連立
させて前記被測定対象物内の気体の圧力がP0であ
る時点に於ける気体の単位時間当りの漏洩量を洩
れ重量(dG/dt)P0として下記の式(4)より求める
方 法。 (dG/dt)P0=(V+V+Vx)/RT・d
/dt……(1) (dG/dt)P0=(V+V+Vx)/RT・d
′/dt……(2) V4=V3+k(k:一定) ……(3) ここに R=気体定数 T=気体の絶対温度 2 被測定対象物内より漏洩する気体の漏洩量を
測定する装置にして、互いに異なる既知の容積を
有する第一及び第二の容器と、前記被測定対象物
と前記第一の容器とを連通接続して第一の容積系
を構成する第一の導管と、前記被測定対象物と前
記第二の容器とを連通接続して第二の容積系を構
成する第二の導管と、前記第一及び第二の容積系
へ加圧された気体を供給する加圧気体源と、前記
第一の容積系と前記加圧気体源との連通を遮断す
る第一の弁装置と、前記第二の容積系と前記加圧
気体源との連通を遮断する第二の弁装置と、前記
被測定対象物内の気体の圧力を連続的に測定する
測定装置とを有する装置。
[Claims] 1. A method for measuring the amount of gas leaking from an object to be measured whose volume is Vx, which includes first and second volumes having different known volumes V1 and V2, respectively. a container, a first conduit having a volume of V 3 and communicatively connecting the object to be measured and the first container to constitute a first volume system, and a volume of V 4 to the object to be measured. a second conduit that communicates and connects the object and the second container to form a second volumetric system; and a pressurized gas source that supplies pressurized gas to the first and second volumetric systems. , a first valve device that cuts off communication between the first volumetric system and the pressurized gas source, and a second valve device that cuts off communication between the second volumetric system and the pressurized gas source. , using a gas leakage measuring device having a measuring device that continuously measures the pressure of gas in the first and second volumetric systems; the first volumetric system is formed by communicating with the container, and pressurized gas from the pressurized gas source is introduced into the first volumetric system, and the gas in the first volumetric system is When the pressure of the gas reaches a predetermined pressure P1 , the first valve device is closed, the measuring device measures the pressure change of the gas in the first volume system, and the pressure of the gas in the first volume system is measured. The pressure drop rate dP 0 /dt at the time when the pressure of the gas inside reaches a predetermined pressure P 0 is determined, and the object to be measured and the second container are connected in communication through the second conduit. to form the second volumetric system, pressurized gas from the pressurized gas source is introduced into the second volumetric system, and the pressure of the gas in the second volumetric system is at a predetermined pressure. When P 2 is reached, the second valve device is closed, and the measuring device measures the change in the pressure of the gas in the second volumetric system, and the pressure of the gas in the second volumetric system is measured. The rate of pressure decrease dP 0 '/dt at the point when the predetermined pressure P 0 is reached is determined, and from this, the following equations (1), (2), and (3) are simultaneously applied to the object to be measured. A method of calculating the amount of gas leaking per unit time when the pressure of the gas inside the object is P 0 using the following formula (4) as the leakage weight (dG/dt) P0 . (dG/dt) P0 = (V 1 +V 3 +Vx)/RT・d
P 0 /dt...(1) (dG/dt) P0 = (V 2 +V 4 +Vx)/RT・d
P 0 '/dt...(2) V 4 =V 3 +k (k: constant)...(3) Here, R = Gas constant T = Absolute temperature of gas 2 A device for measuring the amount of gas leaking from inside an object to be measured, comprising first and second containers having different known volumes, and the object to be measured. A first conduit that connects the object to be measured and the first container to form a first volume system; and a first conduit that connects the object to be measured and the second container to form a second volume system. A second conduit constituting the system, a pressurized gas source supplying pressurized gas to the first and second volumetric systems, and communication between the first volumetric system and the pressurized gas source. a first valve device for blocking communication between the second volumetric system and the pressurized gas source; and a second valve device for continuously measuring the pressure of the gas in the object to be measured. A device having a measuring device.
JP57230876A 1982-12-23 1982-12-23 Method and apparatus for measuring leakage quantity of gas Granted JPS59116015A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57230876A JPS59116015A (en) 1982-12-23 1982-12-23 Method and apparatus for measuring leakage quantity of gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57230876A JPS59116015A (en) 1982-12-23 1982-12-23 Method and apparatus for measuring leakage quantity of gas

Publications (2)

Publication Number Publication Date
JPS59116015A JPS59116015A (en) 1984-07-04
JPS6246815B2 true JPS6246815B2 (en) 1987-10-05

Family

ID=16914688

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57230876A Granted JPS59116015A (en) 1982-12-23 1982-12-23 Method and apparatus for measuring leakage quantity of gas

Country Status (1)

Country Link
JP (1) JPS59116015A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105467153A (en) * 2015-12-31 2016-04-06 中国电建集团贵阳勘测设计研究院有限公司 Method for measuring seepage velocity of dam body and measuring cup used in method
CN108931277B (en) * 2018-07-06 2020-06-19 西安工程大学 Method for detecting total leakage of compressed air system of textile mill
CN109813388B (en) * 2019-01-01 2020-12-04 中国人民解放军63653部队 Device and method for measuring comprehensive performance of tinplate packaging container

Also Published As

Publication number Publication date
JPS59116015A (en) 1984-07-04

Similar Documents

Publication Publication Date Title
US8360112B2 (en) Method and device for filling pressure gas containers
CA1340901C (en) Process and apparatus for testing a hollow body
HK1002539B (en) In-line volume testing a plastic bottle
US6119507A (en) Method and apparatus for recovering helium after testing for leaks in a sample holder
US4763518A (en) Method for measuring net internal volume of a receptacle containing an unknown volume of residual liquid
US4012945A (en) Means for testing containers for leakage
US7254954B2 (en) Refrigerant charging system and method using cartridges and scale
JPS6246815B2 (en)
JPS63261114A (en) Method and device for measuring the volume of liquid in a tank
US20090299659A1 (en) Method for determining the total leak rate of systems impinged upon by pressure,and control apparatus for carrying out said method
EP0661529A3 (en) Procedure and device for leak testing of a volume and for determining the leaking amount.
JP3715543B2 (en) Airtight performance test method
EP0689038A2 (en) Non-invasive method of determining residual liquid reagents
RU2026533C1 (en) Method of determining volume of leaking tank
US2353275A (en) Container pressure withstanding testing device
JP3454406B2 (en) Leakage and flow rate inspection device
RU2206879C1 (en) Way to test articles for tightness
SU1136021A1 (en) Ship capacity volume determination method
JPS60210724A (en) Measurement of liquid level height
RU2333468C1 (en) Method for measuring effective volume and testing leakproofness of pneumatic brake chambers and device to this effect
SU1024733A1 (en) Device for measuring volume of air
JP3310224B2 (en) Method and apparatus for measuring gas leakage in a container
JP3054508B2 (en) Method and apparatus for measuring gas leakage in a container
SU1021965A1 (en) Method of checking articles for fluid-tightness
JP3353442B2 (en) Leak inspection method and device