JPH0625741B2 - Thermal conductivity measurement method - Google Patents
Thermal conductivity measurement methodInfo
- Publication number
- JPH0625741B2 JPH0625741B2 JP780188A JP780188A JPH0625741B2 JP H0625741 B2 JPH0625741 B2 JP H0625741B2 JP 780188 A JP780188 A JP 780188A JP 780188 A JP780188 A JP 780188A JP H0625741 B2 JPH0625741 B2 JP H0625741B2
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- Prior art keywords
- temperature
- thermal conductivity
- heat transfer
- sample
- transfer plate
- 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.)
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Description
【発明の詳細な説明】 「産業上の利用分野」 この発明は、断熱材や保温材等の各種材料の特に高温下
における熱伝導率を測定する場合に採用して好適な熱伝
導率測定方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION "Industrial field of application" The present invention is suitable for measuring the thermal conductivity of various materials such as heat insulating materials and heat insulating materials especially at high temperatures. It is about.
「従来の技術」 一般に、断熱材や保温材として用いられる各種の材料の
熱伝導率の値は、常に一定ではなく温度条件によって変
化するものであって、第5図に示すように温度が高いほ
ど熱伝導率も大きくなる、すなわち熱を伝え易くなる傾
向にある。したがって、特にたとえば1,000℃を越
えるような温度条件で使用される断熱材や保温材のよう
に高温下における熱伝導率が問題とされる材料にあって
は、その熱伝導率の測定は試料を実際に使用温度まで加
熱して行うことが必要となる。“Prior Art” Generally, the values of thermal conductivity of various materials used as heat insulating materials and heat insulating materials are not always constant but change depending on temperature conditions, and as shown in FIG. 5, the temperature is high. The higher the thermal conductivity, the easier it is to transfer heat. Therefore, especially for a material whose thermal conductivity at high temperature is a problem, such as a heat insulating material or a heat insulating material used under a temperature condition exceeding 1,000 ° C., the thermal conductivity cannot be measured. It is necessary to actually heat the sample to the working temperature.
そのような熱伝導率の測定を行う装置としては第6図に
示すものが知られている。この従来の熱伝導率測定装置
は、断熱性を有する保護円筒a内の上部、下部にそれぞ
れ主ヒータb、補助ヒータcを配して、保護円筒a内部に
下向きの定常的な熱流を生ぜしめるとともに、補助ヒー
タcの上部にその定常熱流の熱流量を計測するための熱
流計測板dを備えたものである。An apparatus shown in FIG. 6 is known as an apparatus for measuring such thermal conductivity. In this conventional thermal conductivity measuring device, a main heater b and an auxiliary heater c are arranged in an upper portion and a lower portion of a protective cylinder a having a heat insulating property to generate a steady downward heat flow inside the protective cylinder a. In addition, a heat flow measuring plate d for measuring the heat flow rate of the steady heat flow is provided above the auxiliary heater c.
この熱伝導率測定装置によって測定を行うには、保護円
筒a内の中心位置に熱伝導率を測定するべき試料Sを配
するとともに、その上下に熱伝導率が既知の標準伝熱板
s1,s2を配し、主ヒータb、補助ヒータcを制御すること
によって保護円筒a内部に図中破線Aで示すような熱平
衡状態を作って、試料Sおよび標準伝熱板s1,s2に折
線Bのような温度勾配を形成させ、試料Sの平均内部温
度がが熱伝導率を計測するべき温度T℃になるように保
持する。In order to perform the measurement with this thermal conductivity measuring device, a sample S whose thermal conductivity is to be measured is arranged at the center position in the protective cylinder a, and standard heat transfer plates whose thermal conductivity is known are arranged above and below the sample S.
By disposing s 1 and s 2 and controlling the main heater b and the auxiliary heater c, a thermal equilibrium state shown by a broken line A in the figure is created inside the protective cylinder a, and the sample S and the standard heat transfer plate s 1 , A temperature gradient such as a polygonal line B is formed on s 2 and the average internal temperature of the sample S is maintained at a temperature T ° C. at which the thermal conductivity should be measured.
そして、定常状態において試料Sの上面、下面の正確な
温度を温度計e,eによって計測して、それらの温度差
と、熱流計測板dによって計測される定常熱流の熱流す
なわち試料Sを透過した熱貫流量とから、試料Sのその
温度T℃(試料Sの平均内部温度)における熱伝導率を
算出するようにしている。Then, in the steady state, the accurate temperatures of the upper surface and the lower surface of the sample S are measured by the thermometers e, e, and the temperature difference between them and the heat flow of the steady heat flow measured by the heat flow measurement plate d, that is, the sample S are transmitted. The thermal conductivity of the sample S at the temperature T ° C. (average internal temperature of the sample S) is calculated from the heat transmission flow rate.
すなわち、計測された熱貫流量がQ(Kcal/h)、試料
Sの上面温度、下面温度がそれぞれθ1,θ2(℃)であっ
たとし、試料Sの厚み寸法がδ(m)、試料Sの有効面積
がA(m2)であったとすると、試料Sの温度T℃における
熱伝導率λ(Kcal/m・h・deg)は、 Q=(λ/δ)・A(θ1−θ2) の関係が成り立つから、この式から、 λ=Q・δ/A(θ1−θ2) ……(1) として求められる。That is, it is assumed that the measured heat transmission flow rate is Q (Kcal / h), the upper surface temperature and the lower surface temperature of the sample S are θ 1 and θ 2 (° C.), respectively, and the thickness dimension of the sample S is δ (m), Assuming that the effective area of the sample S is A (m 2 ), the thermal conductivity λ (Kcal / m · h · deg) of the sample S at the temperature T ° C. is Q = (λ / δ) · A (θ 1 Since the relation of −θ 2 ) is established, it can be obtained from this formula as λ = Q · δ / A (θ 1 −θ 2 ) ... (1).
なお、上記従来の熱伝導率測定装置における標準伝熱板
s1,s2は、試料Sの温度を高温に保持するためのもので
あるとともに、それらの表面温度を温度計f…によって
計測することによって、それらの表面温度および上記の
熱貫流量Qとから求められる熱伝導率の値を既知の熱伝
導率の値と比較することによって、計測値を検証し、必
要に応じて補正するためのものである。The standard heat transfer plate in the conventional thermal conductivity measuring device
s 1 and s 2 are for keeping the temperature of the sample S at a high temperature, and by measuring their surface temperature with a thermometer f ... This is for verifying the measured value by comparing the value of the thermal conductivity obtained from the above with the known value of the thermal conductivity, and for correcting it if necessary.
また、符号g…は壁面温度補償用のヒータであって、こ
れらのヒータg…は、保護内筒a内部の温度勾配がAの
状態となるように保護円筒aの表面温度を制御し、これ
により保護円筒aとその内部空間との間の熱授受を無く
して熱流が保護円筒aの周面から放散してしまうことを
防止するためのものである。Further, reference characters g ... Are wall surface temperature compensating heaters, and these heaters g ... Control the surface temperature of the protective cylinder a so that the temperature gradient inside the protective inner cylinder a is in the state of A. This prevents heat transfer between the protective cylinder a and the internal space thereof and prevents the heat flow from radiating from the peripheral surface of the protective cylinder a.
「発明が解決しようとする課題」 ところで、上記のような熱伝導率測定装置を用いて測定
を行う場合、試料Sの上面、下面がそれぞれ標準伝熱板
s1,s2に接していることから、それらの温度が高くなる
と表面温度を正確に計測することは容易ではなく、それ
によって測定範囲が制約を受けていた。[Problems to be Solved by the Invention] By the way, when the measurement is performed using the thermal conductivity measuring device as described above, the upper surface and the lower surface of the sample S are standard heat transfer plates
Since it is in contact with s 1 and s 2 , it is not easy to measure the surface temperature accurately when the temperature becomes high, and the measurement range is restricted by it.
このため、標準伝熱板s1,s2を省略することも考えられ
ようが、上面側の標準伝熱板s1は省略することも可能で
はあるが、下面側の標準伝熱板s2は、測定温度がが特に
高温の場合には熱流計測板dを低温に保持する必要があ
ることから省略することができないものであった。Therefore, it may be possible to omit the standard heat transfer plates s 1 and s 2 , but it is possible to omit the standard heat transfer plate s 1 on the upper surface side, but it is possible to omit the standard heat transfer plate s 2 on the lower surface side. However, when the measurement temperature is particularly high, the heat flow measurement plate d needs to be kept at a low temperature, and therefore cannot be omitted.
この発明は上記の事情に鑑みてなされたもので、試料の
特に高温化における熱伝導率を、容易にかつ正確に測定
することのできる測定方法を提供することを目的として
いる。The present invention has been made in view of the above circumstances, and an object thereof is to provide a measuring method capable of easily and accurately measuring the thermal conductivity of a sample, especially at high temperatures.
「課題を解決するための手段」 この発明は、所定の測定温度Tにおける試料の熱伝導率
λsを測定するに際し、まず、標準伝熱板の下面温度t0
を一定に保持しつつ、かつ上面温度t1を段階的に変化
させつつ、この標準伝熱板の各温度における熱伝導率λ
1を求め、次いで、標準伝熱板の上面に試料を重ね合わ
せ、標準伝熱板の下面温度をそのまま上記の温度t0に
保持するとともに、試料の上面温度を測定温度Tに保持
して、この状態における標準伝熱板と試料との総合熱伝
導率λtを求め、その総合伝導率λtの値と、前記標準伝
熱板の各温度における熱伝導率λ1の値に基づいて試料
の測定温度Tにおける熱伝導率λsを算出することを特
徴としている。"Means for Solving the Problem" In the present invention, when measuring the thermal conductivity λs of a sample at a predetermined measurement temperature T, first, the lower surface temperature t 0 of the standard heat transfer plate is measured.
While the temperature is kept constant and the upper surface temperature t 1 is changed stepwise, the thermal conductivity λ of the standard heat transfer plate at each temperature is increased.
1 is obtained, and then the sample is superposed on the upper surface of the standard heat transfer plate, and the lower surface temperature of the standard heat transfer plate is maintained as it is at the above temperature t 0, and the upper surface temperature of the sample is maintained at the measurement temperature T, Obtain the total thermal conductivity λt of the standard heat transfer plate and the sample in this state, and measure the sample based on the value of the total conductivity λt and the thermal conductivity λ 1 at each temperature of the standard heat transfer plate. It is characterized in that the thermal conductivity λs at the temperature T is calculated.
「実施例」 以下、この発明方法の実施例を図面を参照して説明す
る。[Embodiment] An embodiment of the method of the present invention will be described below with reference to the drawings.
まず、第1図を参照して、この発明方法を実施するに際
して用いて好適な熱伝導率測定装置について説明する。
第1図はその装置の概略構成を示す立断面図であって、
図中符号1は炉容器である。この炉容器1は、それぞれ
水冷ジャケットを有する本体2および本体2にヒンジ3
によって連結された蓋体4から構成されている。First, with reference to FIG. 1, a thermal conductivity measuring apparatus suitable for carrying out the method of the present invention will be described.
FIG. 1 is a vertical cross-sectional view showing a schematic configuration of the device,
Reference numeral 1 in the drawing is a furnace vessel. The furnace vessel 1 includes a main body 2 and a main body 2 each having a water cooling jacket and a hinge 3 attached to the main body 2.
It is composed of the lid body 4 connected by.
その炉容器1内には、それぞれ円板状の下部断熱材5、
上部断熱材6、および円筒状の側部断熱材7によって、
内部に試料Sが配される計測室8が形成されている。こ
の計測室8内の上部空間には計測室8内を所定の温度に
保持するための主ヒータ9が取り付けられているととも
に、下部断熱材中5にはこの下部断熱材5の内面温度を
熱流計測室板15(後述)の温度と同様に保持するため
の補償ヒータ10が埋め込まれており、それらの主ヒー
タ9、補償ヒータ10には炉容器1の蓋体4および本体
2を貫通している電極11,12が接続されている。な
お、符号13は計測室8内の温度を計測するための放射
温度計である。Inside the furnace vessel 1, a disk-shaped lower heat insulating material 5,
By the upper heat insulating material 6 and the cylindrical side heat insulating material 7,
A measurement chamber 8 in which the sample S is arranged is formed. A main heater 9 for keeping the inside of the measuring chamber 8 at a predetermined temperature is attached to the upper space of the measuring chamber 8, and the inner surface temperature of the lower insulating member 5 is heated by the heat flow in the lower insulating member 5. Compensation heaters 10 for keeping the same as the temperature of the measurement chamber plate 15 (described later) are embedded. The main heater 9 and the compensation heaters 10 penetrate the lid 4 of the furnace container 1 and the main body 2. The electrodes 11 and 12 are connected. Reference numeral 13 is a radiation thermometer for measuring the temperature in the measurement chamber 8.
また、計測室8の側壁を形成している上記の側部断熱材
7の内面は、充分な耐熱性を有しかつ熱伝導性に優れた
材料、たとえば、グラファイト、耐熱鋼、モリブデン
等、によって筒状に形成された壁面温度補償板14によ
って覆われている。この補償板14は、その優れた熱伝
導性によって計測室8の上部から下部に向かって熱を運
び、もって、側部断面材7の内面温度を試料Sあるいは
標準伝熱板24(後述)の各々の温度と同等に保持する
ためのものである。したがって、この装置においては、
従来の装置における壁面温度補償用のヒータg…を設け
る必要がなくなり、装置の簡略化、小形化が実現されて
いる。The inner surface of the side heat insulating material 7 forming the side wall of the measuring chamber 8 is made of a material having sufficient heat resistance and excellent thermal conductivity, for example, graphite, heat-resistant steel, molybdenum, or the like. It is covered with a wall surface temperature compensating plate 14 formed in a tubular shape. This compensating plate 14 carries heat from the upper part to the lower part of the measuring chamber 8 due to its excellent thermal conductivity, so that the inner surface temperature of the side cross-section member 7 is adjusted to the sample S or the standard heat transfer plate 24 (described later). It is for keeping the same temperature. Therefore, in this device,
It is not necessary to provide heaters g for wall surface temperature compensation in the conventional device, and the device is simplified and downsized.
また、下部断熱材5の上面中央部には円板形状の熱流計
測板15が配され、その周囲には環状の補償冷却板16
が配されている。熱流計測板15は、内部に熱貫流量を
計測するための測温用ガスの流通路が渦巻き状に形成さ
れており、その流通路に測温用ガスを図中の矢印で示す
ように流通させるためのガス導入管17およびガス導出
管18がそれぞれ接続されている。また、補償冷却板1
6は、内部に冷却ガスを流通させるための流通路が渦巻
き状に形成されていて、冷却用ガスを図中の矢印のよう
に流通させるための冷却ガス導入管19、冷却ガス導出
管20がそれぞれ接続されている。上記の測温用ガス、
冷却用ガスは、下部断熱材5中に埋め込まれているガス
予熱器21,22によって所定の温度とされた後に、そ
れぞれ熱流計測板15、補償冷却板16に導入されるよ
うになっている。また、図示は省略したが測温用ガスの
入口温度と出口温度、冷却用ガスの入口温度と出口温度
を計測するための温度計がそれぞれ設けられている。Further, a disc-shaped heat flow measuring plate 15 is arranged in the central portion of the upper surface of the lower heat insulating material 5, and an annular compensating cooling plate 16 is provided around the heat flow measuring plate 15.
Are arranged. The heat flow measuring plate 15 has a flow passage for the temperature measuring gas for measuring the heat transmission flow formed in a spiral shape, and the temperature measuring gas is circulated in the flow passage as indicated by an arrow in the figure. A gas inlet pipe 17 and a gas outlet pipe 18 are connected to each other. Also, the compensating cooling plate 1
6, a flow passage for circulating the cooling gas is formed in a spiral shape, and a cooling gas introduction pipe 19 and a cooling gas derivation pipe 20 for circulating the cooling gas as shown by arrows in the drawing are provided. Each is connected. The above temperature measuring gas,
The cooling gas is introduced into the heat flow measuring plate 15 and the compensating cooling plate 16 after being brought to a predetermined temperature by the gas preheaters 21 and 22 embedded in the lower heat insulating material 5. Although not shown, thermometers for measuring the inlet temperature and the outlet temperature of the temperature measuring gas and the inlet temperature and the outlet temperature of the cooling gas are respectively provided.
上記の熱流計測板15は、測温用ガスの入り口と出口で
の温度を計測することによって、その温度差とガス流量
とから測温用ガスの受熱量、すなわち試料Sを透過した
熱貫流量を計測するためのものである。また、その周囲
に配された補償冷却板16は、熱流計測板15と同温度
に保持されることによりそれら相互間の熱授受を防ぐた
めのものである。The heat flow measuring plate 15 measures the temperatures at the inlet and the outlet of the temperature measuring gas, and from the temperature difference and the gas flow rate, the heat receiving amount of the temperature measuring gas, that is, the heat transmission flow rate passing through the sample S. Is for measuring. Further, the compensating cooling plate 16 arranged around it is for holding heat exchange between them by being kept at the same temperature as the heat flow measuring plate 15.
上記の熱流計測板15および補償冷却板16の上面には
下部測温板23が配され、その上面に断熱性を有する標
準伝熱板24が配され、その上面熱伝導率を計測するべ
き試料Sが配され、さらにその上面に上部測温板25が
配されるようになっている。下部測温板23、上部測温
板25にはそれぞれ熱電対温度計(図示略)が挿入され
ており、それらの熱電対温度計または放射温度計13に
よって標準伝熱板24の下面温度、および試料Sの上面
温度が計測できるようにされている。A lower temperature measuring plate 23 is arranged on the upper surfaces of the heat flow measuring plate 15 and the compensating cooling plate 16, and a standard heat transfer plate 24 having heat insulating property is arranged on the upper surface thereof, and a sample whose upper surface thermal conductivity is to be measured. S is arranged, and the upper temperature measuring plate 25 is further arranged on the upper surface thereof. A thermocouple thermometer (not shown) is inserted in each of the lower temperature measuring plate 23 and the upper temperature measuring plate 25, and the lower surface temperature of the standard heat transfer plate 24 and the thermocouple thermometer or the radiation thermometer 13 are inserted. The upper surface temperature of the sample S can be measured.
以上で熱伝導率測定装置の構成を説明したが、次にその
装置を用いる測定方法について説明する。以下で説明す
る測定方法は、試料SのT℃における熱伝導率λsを測
定するに際して、試料Sの下面温度を直接的に計測する
ことなく、標準伝熱板24の熱伝導率λ1を測定して、
その値に基づき間接的に算出するものである。The configuration of the thermal conductivity measuring device has been described above. Next, a measuring method using the device will be described. The measuring method described below measures the thermal conductivity λ 1 of the standard heat transfer plate 24 without directly measuring the lower surface temperature of the sample S when measuring the thermal conductivity λs of the sample S at T ° C. do it,
It is calculated indirectly based on the value.
すなわち、まず、下部測温板23の上面に標準伝熱板2
4を配してその上面に試料Sを配することなく上部計測
板25を直接的に配し、上部断熱材6によって計測室8
を密閉するとともに炉容器1の蓋体4を閉じ、この標準
伝熱材24の熱伝導率を測定する。それには、従来の装
置と同様に主ヒータ9、補償ヒータ10を制御して計測
室8内に定常熱流を生ぜしめ、測温用ガス、冷却用ガス
をそれぞれ予熱器21,22によって所定温度に加熱し
て熱流計測板15、補償冷却板16に流通させることに
よってそれらの温度を同等に保持するようにし、定常状
態となったら熱流計測板15内を流通する測温用ガスの
入口、出口の温度を計測し、測温用ガスの温度差とその
流量とから受熱量すなわち標準伝熱板24を透過した熱
貫流量を求め、その熱貫流量の値と、標準伝熱板24の
上下両面の温度、およびその厚み寸法とから、次の(2)
式によってこの状態における標準伝熱板24の熱伝導率
を求める。That is, first, the standard heat transfer plate 2
4 and the upper measuring plate 25 is directly arranged without arranging the sample S on the upper surface thereof, and the measuring chamber 8 is arranged by the upper heat insulating material 6.
And the lid 4 of the furnace container 1 are closed, and the thermal conductivity of this standard heat transfer material 24 is measured. To this end, similar to the conventional device, the main heater 9 and the compensating heater 10 are controlled to generate a steady heat flow in the measuring chamber 8, and the temperature measuring gas and the cooling gas are brought to predetermined temperatures by the preheaters 21 and 22, respectively. The temperatures of the heat flow measuring plate 15 and the compensating cooling plate 16 are maintained at the same level by heating and flowing to the heat flow measuring plate 15 and the compensating cooling plate 16. The temperature is measured, the amount of heat received, that is, the heat transmission flow rate that has passed through the standard heat transfer plate 24 is obtained from the temperature difference of the temperature measurement gas and its flow rate, and the value of the heat transmission flow rate and the upper and lower surfaces of the standard heat transfer plate 24 are both obtained. From the temperature and the thickness dimension, the following (2)
The thermal conductivity of the standard heat transfer plate 24 in this state is calculated by the equation.
この場合、第2図に模式的に表すように、標準伝熱板2
4の熱貫流量をQ1、下面温度がt0、上面温度がt1、標
準伝熱板24の厚み寸法がδ1であり、この状態におけ
る標準伝熱板の熱伝導率をλ1とすると、 Q1=(λ1/δ1)A(t1−t0) ……(2) であるから、これによりλ1を求める。なお、この場
合、標準伝熱板24の有効面積Aは熱流計測板15の面
積である。In this case, as shown schematically in FIG. 2, the standard heat transfer plate 2
4 is Q 1 , the lower surface temperature is t 0 , the upper surface temperature is t 1 , the thickness dimension of the standard heat transfer plate 24 is δ 1 , and the thermal conductivity of the standard heat transfer plate in this state is λ 1 . Then, since Q 1 = (λ 1 / δ 1 ) A (t 1 −t 0 ) ... (2), λ 1 is obtained from this. In this case, the effective area A of the standard heat transfer plate 24 is the area of the heat flow measurement plate 15.
続いて、標準伝熱板24の下面温度t0を一定に保持して
おくとともに、上面温度t1を測定温度T℃より高温にな
るまで所定の温度ずつ段階的に上昇させていき、それぞ
れの段階において以上と同様にして測定をおこなって各
温度における熱伝導率を求め、第3図に示すような熱伝
導率λ1の上面温度t1との関係を表すグラフを作成す
る。そして、λ1はt1の関数であるから、 λ1=Φ(t1) ……(3) と表す。関数Φは、多数のデータをコンピュータを用い
て処理することにより近似的に求めることができる。な
お、この関数Φは、標準伝熱板24の材質等によってそ
れぞれ異なることは勿論である。Subsequently, the lower surface temperature t 0 of the standard heat transfer plate 24 is kept constant, and the upper surface temperature t 1 is gradually increased by a predetermined temperature until it becomes higher than the measurement temperature T ° C. In the step, measurement is performed in the same manner as above to obtain the thermal conductivity at each temperature, and a graph showing the relationship between the thermal conductivity λ 1 and the upper surface temperature t 1 as shown in FIG. 3 is prepared. Since λ 1 is a function of t 1 , it is expressed as λ 1 = Φ (t 1 ) ... (3). The function Φ can be approximately calculated by processing a large amount of data using a computer. Of course, this function Φ varies depending on the material of the standard heat transfer plate 24 and the like.
以上のようにして標準伝熱板24の各温度における熱伝
導率λ1を求めたら、次に、標準伝熱板24の上面に試
料Sを重ね合わせ、その上面に上部測温板25を配す
る。そして、第4図に模式的に表すように、標準伝熱板
24の下面温度を上記と同じ温度t0に保持するととも
に、試料Sの上面温度を測定温度Tに保持し、定常状態
となったらその状態における熱貫流量Qtを計測する。
この場合、試料の厚み寸法をδsとし、試料Sと標準伝
熱板24の総合熱伝導率をλtとすると、次の関係が成
り立つ。After the thermal conductivity λ 1 at each temperature of the standard heat transfer plate 24 is obtained as described above, next, the sample S is superposed on the upper surface of the standard heat transfer plate 24, and the upper temperature measuring plate 25 is arranged on the upper surface thereof. To do. Then, as schematically shown in FIG. 4, the lower surface temperature of the standard heat transfer plate 24 is maintained at the same temperature t 0 as described above, and the upper surface temperature of the sample S is maintained at the measurement temperature T, so that the steady state is achieved. The heat transmission flow rate Qt in that state is measured.
In this case, if the thickness dimension of the sample is δs and the total thermal conductivity of the sample S and the standard heat transfer plate 24 is λt, the following relationship holds.
Qt={λt/(δ1+δs)}A(T−t0)……(4) これにより、試料Sと標準伝熱板24との総合熱伝導率
λtの値が求められる。 Qt = {λt / (δ 1 + δs)} A (T-t 0) ...... (4) Thus, the value of the overall thermal conductivity .lamda.t between the sample S and the standard heat transfer plate 24 is determined.
この第4図に示される状態を、試料Sと標準伝熱板24
とに分割して考え、試料Sの熱伝導率をλs、試料Sの
下面温度(=標準伝熱板24の上面温度)をt1′、この
状態における標準伝熱板24の熱伝導率λ1′、と仮定
すると、定常状態においては試料Sを通過する熱貫流量
と、標準伝熱板24を通過する熱貫流量は、いずれも全
体を通過する熱貫流量Qtに等しいことから、上記
(4)式は次のように展開できる。The state shown in FIG.
The thermal conductivity of the sample S is λs, the lower surface temperature of the sample S (= upper surface temperature of the standard heat transfer plate 24) is t 1 ′, the thermal conductivity λ of the standard heat transfer plate 24 in this state. Assuming 1 ′, the heat transmission flow rate passing through the sample S and the heat transmission flow rate passing through the standard heat transfer plate 24 are both equal to the heat transmission flow rate Qt passing through the whole in the steady state. Expression (4) can be expanded as follows.
Qt={λt/(δ1+δs)}A(T−t0)……(4) =(λ1′/δ1)A(t1′−t0)……(4)′ =(λs/δs)A(T−t1′) ……(4)″ したがって、(4)′式=(4)″式とおくと (λ1′/δ1)A(t1′−t0) =(λs/δs)A(T−t1′)……(4) 一方、この状態における試料Sと標準伝熱板24との総
合熱抵抗率Rtは、標準伝熱板24の熱抵抗率R1と、試
料Sの熱抵抗率Rsの和であらわされる。すなわち、 Rt=(δ1+δs)/λt R1=δ1/λ1′ Rs=δs/λs であり、 Rt=R1+Rs であるから、したがって、 (δ1+δs)/λt =(δ1/λ1′)+(δs/λs)……(5) の関係が成り立つ。Qt = {λt / (δ 1 + δs)} A (T−t 0 ) ... (4) = (λ 1 ′ / δ 1 ) A (t 1 ′ −t 0 ) …… (4) ′ = (λs / Δs) A (T−t 1 ′) (4) ″ Therefore, if the equation (4) ′ = (4) ″ is given, (λ 1 ′ / δ 1 ) A (t 1 ′ −t 0 ). = (Λs / δs) A (T−t 1 ′) (4) On the other hand, the total thermal resistivity Rt between the sample S and the standard heat transfer plate 24 in this state is the thermal resistivity of the standard heat transfer plate 24. It is represented by the sum of R 1 and the thermal resistivity Rs of the sample S. That is, Rt = (δ 1 + δs) / λt R 1 = δ 1 / λ 1 ′ Rs = δs / λs, and Rt = R 1 + Rs, therefore (δ 1 + δs) / λt = (δ 1 / Λ 1 ′) + (δs / λs) (5).
上記の各式において、λsが最終的に求めたい試料Sの
温度Tにおける熱伝導率であり、また、λ1′、t1′は
未知数であるが、λ1′は上面温度t1′、かつ下面温度t
0における標準伝熱板24の熱伝導率であるから、上記
(3)式から λ1′=Φ(t1′) ……(3)′ である。したがって、上記の(4)式、(5)式、
(3)′式の3つの式からなる連立方程式を解けば、上
記の3つの未知数λs,λ1′,t1′をいずれも求めるこ
とができる。なお、この計算はマイクロコンピュータを
用いれば極めて簡単に行うことができる。また、標準伝
熱板24の熱伝導率λ1と上面温度t1との関係を表す関
数Φを求めずとも、第3図のような熱伝導率λ1と上面
温度t1の関係を表すグラフから、(4)式、(5)式
の関係を満足するλ1′,t1′の値を読み取るようにし
ても良い。In the above equations, λs is the thermal conductivity of the sample S to be finally obtained at the temperature T, and λ 1 ′ and t 1 ′ are unknowns, but λ 1 ′ is the upper surface temperature t 1 ′, And lower surface temperature t
Since it is the thermal conductivity of the standard heat transfer plate 24 at 0 , from the above formula (3), λ 1 ′ = Φ (t 1 ′) (3) ′. Therefore, the above equations (4), (5),
By solving the simultaneous equations consisting of the three equations (3) ′, all of the above three unknowns λs, λ 1 ′ and t 1 ′ can be obtained. It should be noted that this calculation can be performed extremely easily by using a microcomputer. Also, without seeking function Φ representing the relationship between the thermal conductivity lambda 1 and the upper surface temperature t 1 of the standard heat transfer plate 24, representing the thermal conductivity lambda 1 and the relationship of the upper surface temperature t 1, such as Figure 3 It is also possible to read the values of λ 1 ′ and t 1 ′ that satisfy the relationships of equations (4) and (5) from the graph.
以上で説明したように、上記の方法によれば、標準伝熱
板24の上面に接していて従来においては正確な計測を
行うことが困難であった試料Sの下面温度t1′を直接的
に計測せずとも、試料Sの熱伝伝導率λsを計算によっ
て求めることができ、したがって、標準伝熱板24を省
略することのできない特に高温における熱伝導率の測定
に際して採用して好適であるし、熱入伝導率測定装置の
構成も簡略化することができる。As described above, according to the above method, the lower surface temperature t 1 ′ of the sample S which is in contact with the upper surface of the standard heat transfer plate 24 and which has been difficult to perform accurate measurement in the past is directly measured. It is possible to obtain the thermal conductivity λs of the sample S by calculation without performing the measurement, and therefore, it is preferable to adopt it when measuring the thermal conductivity at a particularly high temperature where the standard heat transfer plate 24 cannot be omitted. However, the configuration of the heat input conductivity measuring device can be simplified.
なお、常に同一の標準伝熱板を用いるのであれば、その
熱伝導率の測定は当初に一度だけ行って第3図に示すよ
うなグラフを作成し、関数Φを求めておけば良く、試料
の測定に際してその都度標準伝熱板の熱伝導率の測定を
行う必要はない。If the same standard heat transfer plate is always used, it is sufficient to measure its thermal conductivity only once at the beginning to create a graph as shown in Fig. 3 and obtain the function Φ. It is not necessary to measure the thermal conductivity of the standard heat transfer plate each time.
「発明の効果」 以上で詳細に説明したように、この発明の熱伝導率測定
方法は、まず標準伝熱板の熱伝導率を求め、次いで、標
準伝熱板に試料を重ね合わせてそれらの総合伝導率を求
め、それらの値に基づいて試料の熱伝導率を算出するの
で、従来においては測定が困難であり、かつ、測定によ
りその測定装置を通して流れる熱のため誤差の原因とも
なっていた、標準伝熱板に接している試料の下面温度を
直接的に計測することなく試料の熱伝導率を求めること
ができ、したがって、標準伝熱板を省略することのでき
ない特に高温における熱伝導率の測定に際して採用して
好適であるし、熱伝導率測定装置の構成も簡略化するこ
とができる、という効果を奏する。"Effects of the Invention" As described in detail above, the thermal conductivity measuring method of the present invention first determines the thermal conductivity of the standard heat transfer plate, and then superimposes the sample on the standard heat transfer plate to obtain the Since the total conductivity is obtained and the thermal conductivity of the sample is calculated based on those values, it has been difficult to measure in the past, and the heat flowing through the measuring device caused the error. The thermal conductivity of the sample can be obtained without directly measuring the lower surface temperature of the sample that is in contact with the standard heat transfer plate. It is suitable for use in the measurement, and the structure of the thermal conductivity measuring device can be simplified.
第1図ないし第4図はこの発明の実施例を説明するため
の図である。第1図はこの発明方法の実施に用いて好適
な熱伝導率測定装置の立断面図である。第2図は標準伝
熱板の熱伝導率の測定状態を説明するための模式図、第
3図は標準伝熱板の熱伝導率と上面温度との関係を表す
図、第4図は標準伝熱板と試料を重ねた状態での総合熱
伝導率の計測状態を説明するための図である。 第5図は熱伝導率と温度との関係を示す図、第6図は従
来の熱伝導率測定装置と概略構成を示す立断面図であ
る。 S……試料、24……標準伝熱板、 T……測定温度、 t0……標準伝熱板の下面温度、 t1,t1′……標準伝熱板の上面温度、 λ1……標準伝熱板の熱伝導率、 λt……総合熱伝導率、 λs……試料の熱伝導率。1 to 4 are views for explaining an embodiment of the present invention. FIG. 1 is a vertical sectional view of a thermal conductivity measuring device suitable for carrying out the method of the present invention. FIG. 2 is a schematic diagram for explaining the measurement state of the thermal conductivity of the standard heat transfer plate, FIG. 3 is a diagram showing the relationship between the thermal conductivity of the standard heat transfer plate and the upper surface temperature, and FIG. 4 is the standard. It is a figure for demonstrating the measurement state of the total thermal conductivity in the state which the heat transfer plate and the sample were piled up. FIG. 5 is a diagram showing the relationship between thermal conductivity and temperature, and FIG. 6 is a vertical cross-sectional view showing a conventional thermal conductivity measuring device and its schematic configuration. S ...... sample, 24 ...... standard heat transfer plate, T ...... measured temperature, t 0 ...... underside temperature of the standard heat transfer plate, t 1, t 1 '...... top temperature of the standard heat transfer plate, lambda 1 ... … The thermal conductivity of the standard heat transfer plate, λt …… Total thermal conductivity, λs …… The thermal conductivity of the sample.
Claims (1)
λsを測定するに際し、まず、標準伝熱板の下面温度t0
を一定に保持しつつ、かつ上面温度t1を段階的に変化さ
せつつ、この標準伝熱板の各温度における熱伝導率λ1
を求め、次いで、標準伝熱板の上面に試料を重ね合わ
せ、標準伝熱板の下面温度をそのまま上記の温度t0に保
持するとともに、試料の上面温度を測定温度Tに保持し
て、この状態における標準伝熱板と試料との総合熱伝導
率λtを求め、その総合伝導率λtの値と、前記標準伝熱
板の各温度における熱伝導率λ1の値に基づいて試料の
測定温度Tにおける熱伝導率λsを算出することを特徴
とする熱伝導率測定方法。1. When measuring the thermal conductivity λs of a sample at a predetermined measurement temperature T, first, the lower surface temperature t 0 of a standard heat transfer plate is measured.
While the temperature is kept constant and the upper surface temperature t 1 is changed stepwise, the thermal conductivity λ 1 at each temperature of this standard heat transfer plate is increased.
Then, the sample is superposed on the upper surface of the standard heat transfer plate, and the lower surface temperature of the standard heat transfer plate is maintained at the above temperature t 0 as it is, and the upper surface temperature of the sample is maintained at the measurement temperature T. Determine the total thermal conductivity λt of the standard heat transfer plate and the sample in the state, the value of the total conductivity λt and the measured temperature of the sample based on the value of the thermal conductivity λ 1 at each temperature of the standard heat transfer plate A method for measuring thermal conductivity, characterized in that the thermal conductivity λs at T is calculated.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP780188A JPH0625741B2 (en) | 1988-01-18 | 1988-01-18 | Thermal conductivity measurement method |
| EP19890300473 EP0325441B1 (en) | 1988-01-18 | 1989-01-18 | A method for measuring thermal conductivity |
| DE1989627938 DE68927938T2 (en) | 1988-01-18 | 1989-01-18 | Method for measuring thermal conductivity |
| US07/795,308 US5258929A (en) | 1988-01-18 | 1991-11-21 | Method for measuring thermal conductivity |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP780188A JPH0625741B2 (en) | 1988-01-18 | 1988-01-18 | Thermal conductivity measurement method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01184448A JPH01184448A (en) | 1989-07-24 |
| JPH0625741B2 true JPH0625741B2 (en) | 1994-04-06 |
Family
ID=11675735
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP780188A Expired - Lifetime JPH0625741B2 (en) | 1988-01-18 | 1988-01-18 | Thermal conductivity measurement method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0625741B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5827097B2 (en) * | 2011-10-17 | 2015-12-02 | ニチアス株式会社 | Thermal conductivity measurement method |
| BR112016020874B1 (en) | 2014-03-10 | 2023-11-21 | Progressive Sterilization, Llc | APPARATUS FOR STERILIZING AND STORING EQUIPMENT |
-
1988
- 1988-01-18 JP JP780188A patent/JPH0625741B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01184448A (en) | 1989-07-24 |
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