JPH0465972B2 - - Google Patents

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Publication number
JPH0465972B2
JPH0465972B2 JP60207470A JP20747085A JPH0465972B2 JP H0465972 B2 JPH0465972 B2 JP H0465972B2 JP 60207470 A JP60207470 A JP 60207470A JP 20747085 A JP20747085 A JP 20747085A JP H0465972 B2 JPH0465972 B2 JP H0465972B2
Authority
JP
Japan
Prior art keywords
thermal
temperature
medium
time
heat
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 - Lifetime
Application number
JP60207470A
Other languages
Japanese (ja)
Other versions
JPS6266147A (en
Inventor
Hideo Watanabe
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.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP20747085A priority Critical patent/JPS6266147A/en
Publication of JPS6266147A publication Critical patent/JPS6266147A/en
Publication of JPH0465972B2 publication Critical patent/JPH0465972B2/ja
Granted legal-status Critical Current

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  • Investigating Or Analyzing Materials Using Thermal Means (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、媒質中に熱量の非定常拡散を、熱源
素子、温度設定素子を共用する細線(円筒状熱伝
導体)を利用して行い、媒質の熱定数である熱伝
導率、熱拡散率を測定する方法に関するものであ
る。 本発明の特徴とするところは、熱的に平衡状態
で媒質中に円筒状伝導体を配置し、ある時刻から
円筒状伝導体を瞬時的に一定温度量ΔTだけステ
ツプ状に変化させて熱平衡を破り、円筒状熱伝導
体の温度を以後、一定値に維持するように熱量を
補償し、このときの補償熱量Q(t)を時間tの
関数として測定し、温度上昇量ΔTとQ(t)を
既知の時間tに関する関数に回帰し、回帰係数よ
り媒質の熱定数である熱伝導率、熱拡散率を求め
ることにある。 媒質中に温度の不均一分布があると、温度勾
配、熱伝導率、熱拡散率の大きさに従つて、系全
体が平衡状態に近づくように熱が移動する。熱平
衡状態にある媒質中に半径aの円筒状導体(細
線)が置かれているとき、ある時刻t=0から、
ある種の動作により、細線の温度をΔTだけステ
ツプ状に上昇させた場合、細線の表面から単位長
さあたり次式で示される熱流Q(t)が媒質中に
流出する。 Q(t)=4πλΔT 〓 〓n=1 {Ao/(logχt)n+1/2 4/σ2χt Bo/(log
χt)n 1/32(4/σ2χt)2Co/(logχt)n+……
}(1) ただし、σ=e〓(γ=0.5772……、オイラー
数)、χ=4κ/a2σ2、λ、κはそれぞれ熱定数の
うちの熱伝導率、熱拡散率である。係数Ao、Bo
Coは方程式を厳密に解くことで求めることがで
きるが、測定に必要な範囲で表1に示す。
The present invention performs unsteady diffusion of heat into a medium by using a thin wire (cylindrical thermal conductor) that serves as a heat source element and a temperature setting element. It relates to a method of measuring. The feature of the present invention is that a cylindrical conductor is placed in a medium in a thermally equilibrium state, and the cylindrical conductor is instantaneously changed in steps by a constant temperature amount ΔT from a certain time to maintain thermal equilibrium. After that, the amount of heat is compensated so that the temperature of the cylindrical heat conductor is maintained at a constant value, the amount of compensated heat Q(t) at this time is measured as a function of time t, and the amount of temperature increase ΔT and Q(t ) is regressed on a function related to a known time t, and the thermal conductivity and thermal diffusivity, which are the thermal constants of the medium, are determined from the regression coefficients. When there is a non-uniform distribution of temperature in a medium, heat moves so that the entire system approaches an equilibrium state according to the magnitude of the temperature gradient, thermal conductivity, and thermal diffusivity. When a cylindrical conductor (thin wire) with radius a is placed in a medium in thermal equilibrium, from a certain time t = 0,
When the temperature of the thin wire is increased stepwise by ΔT by some kind of operation, a heat flow Q(t) expressed by the following equation flows out from the surface of the thin wire per unit length into the medium. Q(t)=4πλΔT 〓 〓 n=1 {A o /(logχt) n +1/2 4/σ 2 χt B o /(log
χt) n 1/32 (4/σ 2 χt) 2 C o /(logχt) n +...
}(1) However, σ=e〓(γ=0.5772..., Euler's number), χ=4κ/a 2 σ 2 , λ, and κ are the thermal conductivity and thermal diffusivity, respectively, of the thermal constants. Coefficients A o , B o ,
C o can be determined by strictly solving the equation, but Table 1 shows the range necessary for measurement.

【表】【table】

【表】 上記原理に基づいて、熱定数を求める方法の具
体例を図1に従つて述べる。 図1は抵抗R1,R2,R3,RS、RLからなるホー
イストンブリツジの出力電圧をサーボ増幅器に導
入し、その出力電圧をブリツジの電源として帰還
している状態を示している。RS,RLは前述した
細線によつて作られた電気抵抗で、添字S、Lは
細線の短、長を示しており、細線内を軸方向に伝
わる熱流の影響を打消す目的で2個の細線抵抗を
利用する。R1,R2,R3は初期状態でブリツジを
平衡させるために使用する。 一般に電気伝導体の抵抗率は温度に依存するの
で、RS,RLの抵抗値は温度の関数となる。初期
状態でRS,RLで発生するジユール熱が無視しえ
るようにしてブリツジの平衡を達成し、ある瞬間
から、R1,R2,R3のいずれかの抵抗を微少量変
化させると、ブリツジの出力が再び零となるよう
にサーボ系が動作する。 ブリツジが再び釣合の状態になつたときは、抵
抗RS,RLは温度差ΔTだけ上昇して初期状態と異
なつた値になつている。このとき、RS,RLで発
生するジユール熱は、RS,RLに流れる電流値、
その抵抗値から容易に算出できる。このジユール
熱は、媒質中に流出するので、細線の有効な長さ
を測定することにより、単位長さあたりの熱流流
出量を求めることができる。このようにして、時
間の関数として求めたQ(t)とΔTの関係によ
り、熱定数が測定可能となる。 補足的に言えば、ブリツジはホーイストンブリ
ツジだけでなく、他の名称で呼ばれるブリツジも
同様使用可能である。
[Table] Based on the above principle, a specific example of a method for determining a thermal constant will be described with reference to FIG. Figure 1 shows a state in which the output voltage of a Wheatstone bridge consisting of resistors R 1 , R 2 , R 3 , R S , and R L is introduced into a servo amplifier, and the output voltage is fed back as a power source for the bridge. There is. R S and R L are the electrical resistances created by the thin wires mentioned above, and the subscripts S and L indicate the shortness and length of the thin wires. Use several thin wire resistors. R 1 , R 2 , and R 3 are used to balance the bridge in the initial state. Generally, the resistivity of an electrical conductor depends on temperature, so the resistance values of R S and R L are a function of temperature. If we achieve bridge equilibrium by making the Joule heat generated in R S and R L negligible in the initial state, and then change the resistance of R 1 , R 2 , or R 3 by a small amount from a certain moment, , the servo system operates so that the bridge output becomes zero again. When the bridge is in equilibrium again, the resistances R S and R L have increased by the temperature difference ΔT and have different values from their initial states. At this time, the Joule heat generated in R S and R L is the current value flowing in R S and R L ,
It can be easily calculated from the resistance value. Since this Joule heat flows out into the medium, the amount of heat flow per unit length can be determined by measuring the effective length of the thin wire. In this way, the thermal constant can be measured from the relationship between Q(t) and ΔT determined as a function of time. As a supplementary note, the bridge is not limited to the Wheatstone bridge, but bridges called by other names can be used as well.

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

第1図は本発明による測定原理の一例を示すも
ので、R1,R2,R3,RS,RLはブリツジを形成す
る抵抗である。
FIG. 1 shows an example of the measurement principle according to the present invention, where R 1 , R 2 , R 3 , R S and RL are resistances forming a bridge.

Claims (1)

【特許請求の範囲】[Claims] 1 熱的に平衡状態で媒質中に円筒状熱伝導体を
配置し、ある時刻から円筒状熱伝導体を瞬時的に
一定温度量ΔTだけステツプ状に変化させて熱平
衡を破り、円筒状熱伝導体から媒質中に熱流を流
出させ、円筒状熱伝導体の温度を以後、一定値に
維持するように熱量を補償し、このときの補償熱
量Q(t)を時間tの関数として測定し、温度上
昇量ΔTとQ(t)を既知の時間tに関する関数
に回帰し、回帰係数より媒質の熱定数である熱伝
導率、熱拡散率を測定することを特徴とする温度
ステツプ細線加熱による熱定数の測定方法。
1 A cylindrical heat conductor is placed in a medium in a state of thermal equilibrium, and from a certain time the temperature of the cylindrical heat conductor is instantaneously changed in steps by a constant amount ΔT to break the thermal equilibrium and increase the cylindrical heat conduction. Flowing heat flow from the body into the medium, compensating the amount of heat so as to maintain the temperature of the cylindrical heat conductor at a constant value from then on, and measuring the compensated amount of heat Q(t) at this time as a function of time t, Temperature step heating by thin wire heating characterized by regressing the temperature increase ΔT and Q(t) on a function related to a known time t, and measuring the thermal constants of the medium, such as thermal conductivity and thermal diffusivity, from the regression coefficient. How to measure constants.
JP20747085A 1985-09-19 1985-09-19 Measuring method for heat constant by temperature step thin wire heating Granted JPS6266147A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20747085A JPS6266147A (en) 1985-09-19 1985-09-19 Measuring method for heat constant by temperature step thin wire heating

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20747085A JPS6266147A (en) 1985-09-19 1985-09-19 Measuring method for heat constant by temperature step thin wire heating

Publications (2)

Publication Number Publication Date
JPS6266147A JPS6266147A (en) 1987-03-25
JPH0465972B2 true JPH0465972B2 (en) 1992-10-21

Family

ID=16540293

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20747085A Granted JPS6266147A (en) 1985-09-19 1985-09-19 Measuring method for heat constant by temperature step thin wire heating

Country Status (1)

Country Link
JP (1) JPS6266147A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6221408B2 (en) * 2013-06-27 2017-11-01 富士電機株式会社 Thermal resistance measuring method and thermal resistance measuring device

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6058159B2 (en) * 1976-08-25 1985-12-18 株式会社豊田自動織機製作所 Container spreader safety equipment
JPS5945098B2 (en) * 1978-08-09 1984-11-02 三菱電機株式会社 Thermal resistance measuring device
JPS5984145A (en) * 1982-10-01 1984-05-15 サラソタ・オ−トメイシヨン・リミテツド Method and device for measuring reynolds number of fluid

Also Published As

Publication number Publication date
JPS6266147A (en) 1987-03-25

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