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JP3344384B2 - Method for measuring viscosity of green compact, viscosity measuring device for green compact, and computer-readable recording medium recording viscosity measuring method for green compact - Google Patents
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JP3344384B2 - Method for measuring viscosity of green compact, viscosity measuring device for green compact, and computer-readable recording medium recording viscosity measuring method for green compact - Google Patents

Method for measuring viscosity of green compact, viscosity measuring device for green compact, and computer-readable recording medium recording viscosity measuring method for green compact

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Publication number
JP3344384B2
JP3344384B2 JP28321099A JP28321099A JP3344384B2 JP 3344384 B2 JP3344384 B2 JP 3344384B2 JP 28321099 A JP28321099 A JP 28321099A JP 28321099 A JP28321099 A JP 28321099A JP 3344384 B2 JP3344384 B2 JP 3344384B2
Authority
JP
Japan
Prior art keywords
sample
load
viscosity
green compact
sample deformation
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 - Fee Related
Application number
JP28321099A
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Japanese (ja)
Other versions
JP2001108594A (en
Inventor
義人 二輪
洋 鷹木
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.)
Murata Manufacturing Co Ltd
Original Assignee
Murata Manufacturing 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 Murata Manufacturing Co Ltd filed Critical Murata Manufacturing Co Ltd
Priority to JP28321099A priority Critical patent/JP3344384B2/en
Priority to DE10049022A priority patent/DE10049022B4/en
Priority to US09/679,208 priority patent/US6508106B1/en
Publication of JP2001108594A publication Critical patent/JP2001108594A/en
Priority to US10/191,032 priority patent/US6581439B2/en
Application granted granted Critical
Publication of JP3344384B2 publication Critical patent/JP3344384B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、結晶化ガラス粉末
等をプレス成形してなる圧粉成型体の粘度測定方法、及
び、圧粉成型体の粘度測定装置、並びに、圧粉成型体の
粘度測定方法を記録したコンピュータ読み取り可能な記
録媒体に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for measuring the viscosity of a green compact formed by press-molding crystallized glass powder and the like, a device for measuring the viscosity of a green compact, and the viscosity of a green compact. The present invention relates to a computer-readable recording medium on which a measurement method is recorded.

【0002】[0002]

【従来の技術】近年、電子業界においては、高密度実装
や高周波化に対応できるセラミック多層基板や厚膜材料
の研究・開発が盛んに行われている。特に、非晶質ガラ
ス粉末や結晶化ガラス粉末からなる低温焼結セラミック
多層基板は、その比誘電率が小さく、また、比抵抗の小
さなAg等の導体材料と同時焼成できることから、各種
電気特性に優れたセラミック多層基板になり得る。
2. Description of the Related Art In recent years, in the electronics industry, research and development of ceramic multilayer substrates and thick film materials capable of coping with high-density mounting and high frequency have been actively conducted. In particular, a low-temperature sintered ceramic multilayer substrate made of an amorphous glass powder or a crystallized glass powder has a small relative dielectric constant and can be co-fired with a conductive material such as Ag having a small specific resistance, so that it has various electrical characteristics. It can be an excellent ceramic multilayer substrate.

【0003】こうしたセラミック多層基板や厚膜材料に
おいて、非晶質ガラス粉末、結晶化ガラス粉末等の酸化
物無機粉末の物性は、基板特性や厚膜特性に大きく寄与
している。なかでも、その粘度特性は、酸化物無機粉末
の焼結プロセスやAg導体の拡散挙動等を大きく左右す
るものであり、材料設計やプロセス設計上、極めて重要
なパラメータである。
In such ceramic multilayer substrates and thick film materials, the physical properties of oxide inorganic powders such as amorphous glass powder and crystallized glass powder greatly contribute to substrate characteristics and thick film characteristics. Above all, the viscosity characteristics greatly affect the sintering process of the oxide inorganic powder, the diffusion behavior of the Ag conductor, and the like, and are extremely important parameters in material design and process design.

【0004】[0004]

【発明が解決しようとする課題】一般に、これらガラス
粉末の粘度は、おおよそ1010Pa・S以上の高粘度領
域については繊維延伸粘度計、おおよそ104Pa・S
以下の低粘度領域については回転式粘度計(球体引き上
げ粘度計)によって測定されている。そして、これらガ
ラス粉末の焼結プロセスで特に重要な104〜109Pa
・Sの中粘度領域については、平行板加圧粘度計を用い
た粘度測定が行われている。
Generally, the viscosity of these glass powders is about 10 10 Pa · S or more in a high viscosity region of about 10 4 Pa · S
The following low viscosity regions are measured by a rotary viscometer (sphere pulling viscometer). In the sintering process of these glass powders, 10 4 to 10 9 Pa
In the medium viscosity region of S, viscosity measurement using a parallel plate pressure viscometer is performed.

【0005】以下、平行板加圧粘度計による粘度ηの測
定方法を説明する。
Hereinafter, a method of measuring the viscosity η using a parallel plate pressure viscometer will be described.

【0006】まず、図15に示すように、支持台3に固
定された石英板2a上に、その高さH及び体積Vが正確
に測定された被測定物(試料)1を配置する。次いで、
これを石英ロッド4に固定された石英板2bで挟み込ん
だ後、石英ロッド4に一定荷重Mを加え、ヒータ5によ
って装置6内を昇温させながら、石英ロッド4に連動し
た差動トランス(図示省略)により、被測定物1の変位
(高さH)を検出する。そして、この変位を経時的に抽
出することによって被測定物1の試料変形速度dh/d
tを算出する。
First, as shown in FIG. 15, an object (sample) 1 whose height H and volume V are accurately measured is placed on a quartz plate 2a fixed to a support table 3. Then
After being sandwiched by a quartz plate 2b fixed to the quartz rod 4, a constant load M is applied to the quartz rod 4 and the temperature inside the device 6 is increased by the heater 5, and the differential transformer (shown in FIG. (Omitted), the displacement (height H) of the DUT 1 is detected. Then, by extracting this displacement with time, the sample deformation speed dh / d of the DUT 1 is obtained.
Calculate t.

【0007】次に、被測定物の体積V、並びに、試料体
積V、荷重M、試料変形速度dh/dtをGENT式: η=2πMGH5/3V(dh/dt)(2πH3+V) (但し、M:荷重、H:試料高さ、G:重力加速度、
V:試料体積、dh/dt:試料変形速度)にそれぞれ
代入し、被測定物1の粘度ηを算出する(A.N.GENT, BR
ITISH JOURNAL OF APPLIED PHYSICS VOL.11, FEBRUARY
1960参照)。そして、これを各温度について実行し、温
度による粘度ηの変化、すなわち粘度−温度曲線を導き
出す。
Next, the volume V of the object to be measured, the sample volume V, the load M, and the sample deformation speed dh / dt are calculated using the GENT equation: η = 2πMGH 5 / 3V (dh / dt) (2πH 3 + V) , M: load, H: sample height, G: gravitational acceleration,
V: sample volume, dh / dt: sample deformation rate) to calculate the viscosity η of the DUT 1 (ANGENT, BR)
ITISH JOURNAL OF APPLIED PHYSICS VOL.11, FEBRUARY
1960). This is performed for each temperature to derive a change in viscosity η with temperature, that is, a viscosity-temperature curve.

【0008】ところが、上述した平行板加圧粘度計によ
る粘度測定においては、被測定物1としてバルク試料を
用いることが必要である。つまり、GENT式は被測定
物1が非圧縮性流体と仮定できる場合に成立する粘度換
算式であって、例えば、ガラス粉末の粘度測定を行う場
合、ガラス粉末を溶融、急冷してバルク状に成形したバ
ルク試料を用いなければならない。
However, in the above-described viscosity measurement using a parallel plate pressure viscometer, it is necessary to use a bulk sample as the DUT 1. In other words, the GENT formula is a viscosity conversion formula that is established when the DUT 1 can be assumed to be an incompressible fluid. For example, when measuring the viscosity of glass powder, the glass powder is melted, quenched, and bulk-cooled. Molded bulk samples must be used.

【0009】すなわち、上述の方法では、バルク状に成
形したガラスについての粘度測定は可能であるが、粉末
状態のガラス、特に結晶化ガラス粉末についての粘度測
定は困難である。これは、結晶化傾向の強い結晶化ガラ
ス粉末では、バルク試料作製時に結晶が析出してしまう
ことがあるためである。また、バルク試料を作製できた
としても、バルク試料と粉末試料とでは結晶化挙動が本
質的に異なるため、たとえ同種のガラス粉末であって
も、バルク試料と粉末試料とでは、その粘性挙動に違い
が現れてしまう。
[0009] That is, in the above-mentioned method, it is possible to measure the viscosity of glass molded into a bulk, but it is difficult to measure the viscosity of glass in a powder state, particularly crystallized glass powder. This is because a crystallized glass powder having a strong tendency to crystallize may precipitate crystals during the preparation of a bulk sample. Even if a bulk sample can be produced, the crystallization behavior is essentially different between the bulk sample and the powder sample. The difference appears.

【0010】しかしながら、上述したように、セラミッ
ク多層基板や厚膜材料では、結晶化ガラスや非晶質ガラ
ス等を粉末試料として使用することが大部分である。す
なわち、材料設計やプロセス設計上、結晶化ガラスや非
晶質ガラス等について、粉末試料としての粘度特性評価
を行う必要がある。
However, as described above, in the case of ceramic multilayer substrates and thick film materials, crystallized glass, amorphous glass, and the like are mostly used as powder samples. That is, in the material design and the process design, it is necessary to evaluate the viscosity characteristics of a crystallized glass, an amorphous glass, and the like as a powder sample.

【0011】本発明は、上述した実情に鑑みてなされた
ものであり、その目的は、無機粉末をプレス成形してな
る圧粉成型体の粘度を高精度に測定する、圧粉成型体の
粘度測定方法を提供することにある。本発明のさらに他
の目的は、圧粉成型体の粘度を効率良く測定できる圧粉
成型体の粘度測定装置、さらには、圧粉成型体の粘度測
定方法を記録したコンピュータ読み取り可能な記録媒体
を提供することにある。
The present invention has been made in view of the above circumstances, and has as its object to measure the viscosity of a green compact formed by press-molding an inorganic powder with high accuracy. It is to provide a measuring method. Still another object of the present invention is a device for measuring the viscosity of a green compact, which can efficiently measure the viscosity of a green compact, and a computer-readable recording medium that records a method for measuring the viscosity of a green compact. To provide.

【0012】[0012]

【課題を解決するための手段】すなわち、本発明は、無
機粉末をプレス成形してなる圧粉成型体の粘度ηを、G
ENT式: η=2πMGH5/3V(dh/dt)(2πH3+V) (但し、M:荷重、H:試料高さ、G:重力加速度、
V:試料体積、dh/dt:試料変形速度)にしたがっ
て測定する、圧粉成型体の粘度測定方法であって、
(A)前記圧粉成型体の試料体積補正値V’(但し、試
料体積補正値V’は、前記圧 粉成型体中の前記無機粉
末が占める体積)を求めるステップ、(B)前記圧粉成
型体の試料変形速度補正値(dh/dt)’(但し、試
料変形速度 補正値(dh/dt)’は、見かけの試料
変形速度と焼結収縮に伴う試料変形速度との差 )を求
めるステップ、(C)前記圧粉成型体の変位について、
焼結収縮が支配的な温度領域X、塑性変形が 支配的な
温度領域Yを分離するステップ、(D)前記焼結収縮が
支配的な温度領域Xについては、前記GENT式の試料
体積V として前記試料体積補正値V’を適用し、か
つ、試料変形速度dh/dtとして前記試料 変形速度
補正値(dh/dt)’を適用するステップ、(E)前
記塑性変形が支配的な温度領域Yについては、前記GE
NT式の試料体積V として前記試料体積補正値V’を
適用するステップ、を有することを特徴とする圧粉成型
体の粘度測定方法に係るものである。
That is, according to the present invention, the viscosity η of a green compact formed by press-molding an inorganic powder is defined as G
ENT formula: η = 2πMGH 5 / 3V (dh / dt) (2πH 3 + V) (However, M: load, H: sample height, G: gravity acceleration,
V: sample volume, dh / dt: sample deformation rate), which is a method for measuring the viscosity of a green compact,
(A) determining a sample volume correction value V ′ of the green compact (where the sample volume correction value V ′ is the volume occupied by the inorganic powder in the green compact); The sample deformation speed correction value (dh / dt) 'of the molded body (where the sample deformation speed correction value (dh / dt)' is the difference between the apparent sample deformation speed and the sample deformation speed due to sintering shrinkage) Step, (C) Displacement of the green compact,
A step of separating a temperature region X in which sintering shrinkage is dominant and a temperature region Y in which plastic deformation is dominant; (D) The temperature region X in which sintering shrinkage is dominant is defined as a sample volume V of the GENT formula. Applying the sample volume correction value V 'and applying the sample deformation speed correction value (dh / dt)' as the sample deformation speed dh / dt; (E) the temperature region Y in which the plastic deformation is dominant. About the GE
Applying the sample volume correction value V ′ as the NT type sample volume V 1.

【0013】本発明の圧粉成型体の粘度測定方法によれ
ば、従来、バルク試料等の非圧縮性流体にしか適用でき
なかった粘度測定について、(A)試料体積の補正→試
料体積補正値V’の抽出ステップ(B)試料変形速度の
補正→試料変形速度補正値(dh/dt)’の抽出ステ
ップ(C)圧粉成型体の変位について、焼結収縮が支配
的な温度領域X、塑性変形が支配 的な温度領域Yの分
離ステップを実行し、さらに、GENT式について、
(D)焼結収縮が支配的な温度領域Xでは、試料体積補
正かつ試料変形速度補正(E)塑性変形が支配的な温度
領域Yでは、試料体積補正を実行することにより、粉末
状態に極めて近い粘性挙動を示す圧粉成型体の粘度を高
精度に測定することができる。
According to the method of measuring the viscosity of a green compact according to the present invention, (A) correction of sample volume → correction value of sample volume for viscosity measurement conventionally applicable only to incompressible fluids such as bulk samples. Extraction step of V ′ (B) Correction of sample deformation speed → Extraction step of sample deformation speed correction value (dh / dt) ′ (C) Regarding displacement of the green compact, temperature range X, where sintering shrinkage is dominant, The separation step of the temperature region Y where the plastic deformation is dominant is executed.
(D) In the temperature region X where sintering shrinkage is dominant, the sample volume is corrected and the sample deformation rate is corrected. (E) In the temperature region Y where the plastic deformation is dominant, the sample volume is extremely corrected by executing the sample volume correction. It is possible to measure the viscosity of a compact having a similar viscous behavior with high accuracy.

【0014】また、本発明は、無機粉末をプレス成形し
てなる圧粉成型体の粘度ηを、GENT式: η=2πMGH5/3V(dh/dt)(2πH3+V) (但し、M:荷重、H:試料高さ、G:重力加速度、
V:試料体積、dh/dt:試料変形速度)にしたがっ
て測定する、圧粉成型体の粘度測定装置であって、
(a)前記圧粉成型体の形状実測値を測定する試料形状
測定部、(b)前記圧粉成型体の見かけの試料変形速度
を測定する試料変形速度測定部、(c)前記圧粉成型体
の形状実測値に基づいて、前記圧粉成型体中の前記無機
粉末が 占める体積を算出し、これを試料体積補正値
V’として出力する演算処理手段、(d)前記見かけの
試料変形速度と、前記圧粉成型体の焼結収縮に伴う試料
変形速度 の差を算出し、前記圧粉成型体の試料変形速
度補正値(dh/dt)’を出力する演算処 理手段、
(e)前記圧粉成型体の変位について、焼結収縮が支配
的な温度領域X、塑性変形が 支配的な温度領域Yの境
界温度を策定する演算処理手段、(f)前記焼結収縮が
支配的な温度領域Xについては、前記GENT式の試料
体積V として前記試料体積補正値V’を適用し、か
つ、試料変形速度dh/dtとして前記試料 変形速度
補正値(dh/dt)’を適用することにより、温度領
域Xでの粘度ηを出力す る演算処理手段、(g)前記
塑性変形が支配的な温度領域Yについては、前記GEN
T式の試料体積V として前記試料体積補正値V’を適
用することにより、温度領域Yでの粘度ηを出力する
演算処理手段、(h)前記温度領域Xでの粘度η、前記
温度領域Yでの粘度ηを表示する表示部、を備えること
を特徴とする圧粉成型体の粘度測定装置を提供するもの
である。
Further, in the present invention, the viscosity η of a green compact formed by press-molding an inorganic powder is determined by the GENT equation: η = 2πMGH 5 / 3V (dh / dt) (2πH 3 + V) (where M: Load, H: sample height, G: gravitational acceleration,
V: a sample volume, dh / dt: sample deformation rate), which is a device for measuring the viscosity of a green compact,
(A) a sample shape measuring unit for measuring an actual measured value of the shape of the green compact; (b) a sample deformation speed measuring unit for measuring an apparent sample deformation speed of the green compact; (c) the green compacting An arithmetic processing means for calculating a volume occupied by the inorganic powder in the green compact based on the actual measured value of the body shape, and outputting the calculated volume as a sample volume correction value V '; (d) the apparent sample deformation speed A calculating means for calculating a difference between a sample deformation speed due to sintering shrinkage of the green compact and a sample deformation speed correction value (dh / dt) 'of the green compact;
(E) With respect to the displacement of the green compact, arithmetic processing means for determining a boundary temperature between a temperature region X in which sintering shrinkage is dominant and a temperature region Y in which plastic deformation is dominant, (f) the sintering shrinkage is For the dominant temperature region X, the sample volume correction value V ′ is applied as the sample volume V 1 of the GENT equation, and the sample deformation speed correction value (dh / dt) ′ is used as the sample deformation speed dh / dt. By applying, the arithmetic processing means for outputting the viscosity η in the temperature region X; (g) For the temperature region Y in which the plastic deformation is dominant, the GEN
The viscosity η in the temperature region Y is output by applying the sample volume correction value V ′ as the sample volume V of the T formula.
A viscosity measuring device for a green compact, comprising: (h) a display unit for displaying the viscosity η in the temperature region X and the viscosity η in the temperature region Y. is there.

【0015】本発明の圧粉成型体の粘度測定装置によれ
ば、(a)試料形状測定部(b)試料変形速度測定部を
備え、さらに、これらの測定部からの測定値に基づき、
(c)試料形状の補正→試料体積補正値V’の抽出
(d)試料変形速度の補正→試料変形速度補正値(dh
/dt)’の抽出(e)焼結収縮が支配的な温度領域
X、塑性変形が支配的な温度領域Yの分離(f)焼結収
縮が支配的な温度領域Xでは、GENT式について試料
体積補正かつ試 料変形速度補正を実行(g)塑性変形
が支配的な温度領域Yでは、GENT式について試料体
積補正を実行する各演算処理手段を備え、そしてこの演
算処理による結果、すなわち、(h)各温度領域での圧
粉成型体の粘度ηを表示する表示部をそれぞれ具備する
ので、従来、バルク試料等の非圧縮性流体にしか適用で
きなかったGENT式を利用して、粉末状態に極めて近
い粘性挙動を示す圧粉成型体の粘度を効率良く測定する
ことができる。
According to the apparatus for measuring the viscosity of a green compact of the present invention, there are provided (a) a sample shape measuring section, and (b) a sample deformation rate measuring section, and further, based on measured values from these measuring sections,
(C) Correction of sample shape → Extraction of sample volume correction value V ′ (d) Correction of sample deformation speed → Sample deformation speed correction value (dh
(E) Separation of temperature region X where sintering shrinkage is dominant and temperature region Y where plastic deformation is dominant (f) In temperature region X where sintering shrinkage is dominant, sample GENT equation (G) In the temperature region Y where plastic deformation is dominant, each temperature processing unit is provided with each processing means for performing the sample volume correction for the GENT equation, and the result of this processing, that is, ( h) Since the display unit for displaying the viscosity η of the green compact in each temperature range is provided, the powder state can be obtained by using the GENT equation, which was conventionally applicable only to incompressible fluids such as bulk samples. It is possible to efficiently measure the viscosity of a compact having a viscous behavior very close to that of a compact.

【0016】さらに、本発明は、本発明の圧粉成型体の
粘度測定方法をコンピュータに実行させるプログラムを
記録したことを特徴とする圧粉成型体の粘度測定方法を
記録したコンピュータ読み取り可能な記録媒体を提供す
るものである。
Further, the present invention provides a computer-readable recording program for recording the method for measuring the viscosity of a green compact, characterized by recording a program for causing a computer to execute the method for measuring the viscosity of a green compact according to the present invention. It provides a medium.

【0017】本発明の圧粉成型体の粘度測定方法を記録
したコンピュータ読み取り可能な記録媒体によれば、本
発明の圧粉成型体の粘度測定方法をコンピュータに実行
させるプログラムを記録しているので、本発明の圧粉成
型体の粘度測定方法について、保存が可能となり、ま
た、その技術移転を容易に行うことができ、多数の者が
容易に利用できるようになる。
According to the computer-readable recording medium on which the method for measuring the viscosity of a green compact according to the present invention is recorded, a program for causing a computer to execute the method for measuring the viscosity of a green compact according to the present invention is recorded. The method for measuring the viscosity of a green compact according to the present invention can be stored, and the technology can be easily transferred, so that many people can use it easily.

【0018】[0018]

【発明の実施の形態】以下、本発明の圧粉成型体の粘度
測定方法を詳細に説明する。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the method for measuring the viscosity of a green compact according to the present invention will be described in detail.

【0019】一般に、平行板加圧粘度計を用いた粘度測
定方法では、下記に示すGENT式によって体積Vの試
料粘度ηを計算する。
In general, in a viscosity measuring method using a parallel plate pressure viscometer, a sample viscosity η of a volume V is calculated by the following GENT formula.

【0020】η=2πMGH5/3V(dh/dt)
(2πH3+V) (但し、M:荷重、H:試料高さ、G:重力加速度、
V:試料体積、dh/dt:試料変形速度)図1は、後
述するSiO2−B23−Al23−CaO系結晶化ガ
ラス粉末のバルク試料及び圧粉成型体について、単純に
GENT式を適用したときの粘度−温度曲線である。な
お、図1中、バルク試料は、前記結晶化ガラス粉末を1
650℃で溶融し、徐冷炉でにて650℃、30分間保
持した後、速度2℃/分で徐冷したものである。他方、
圧粉成型体は、前記結晶化ガラス粉末を有機ビヒクルと
共にプレス成形したものである。
Η = 2πMGH 5 / 3V (dh / dt)
(2πH 3 + V) (However, M: load, H: sample height, G: gravitational acceleration,
V: sample volume, dh / dt: sample deformation rate) FIG. 1 is a schematic view of a bulk sample and a compact of a SiO 2 —B 2 O 3 —Al 2 O 3 —CaO-based crystallized glass powder described later. It is a viscosity-temperature curve at the time of applying a GENT formula. In addition, in FIG. 1, the bulk sample
It was melted at 650 ° C., kept at 650 ° C. for 30 minutes in a slow cooling furnace, and then gradually cooled at a rate of 2 ° C./min. On the other hand,
The green compact is obtained by press-molding the crystallized glass powder together with an organic vehicle.

【0021】図1から分かるように、平行板加圧粘度計
による試料変形速度及び試料体積を単純にGENT式に
適用しただけでは、バルク試料による粘度−温度曲線
と、圧粉成型体による粘度−温度曲線とは一致しない。
すなわち、同種の結晶化ガラス粉末についての粘度測定
にもかかわらず、バルク試料と粉末試料とでは、その粘
性挙動が大きく異なっているように観察される。
As can be seen from FIG. 1, simply applying the sample deformation rate and the sample volume by the parallel plate pressure viscometer to the GENT equation, the viscosity-temperature curve of the bulk sample and the viscosity- Does not match temperature curve.
That is, despite the viscosity measurement of the same type of crystallized glass powder, it is observed that the bulk sample and the powder sample have significantly different viscosity behavior.

【0022】まず、圧粉成型体では830℃付近で粘度
上昇が見られるが、バルク試料ではそれが見られない。
この粘度上昇は、圧粉成型体とバルク試料とではその結
晶化のし易さに相違があることが主な要因である。すな
わち、下記表1に示す熱分析(DSC分析)結果から分
かるように、圧粉成型体の方がバルク試料に比べて、結
晶化開始温度(Tc)、結晶化ピーク温度(Tcp)い
ずれも150℃〜160℃程度低くなっている。
First, a viscosity increase is observed at around 830 ° C. in a green compact, but not in a bulk sample.
This increase in viscosity is mainly due to the difference in the easiness of crystallization between the green compact and the bulk sample. That is, as can be seen from the results of the thermal analysis (DSC analysis) shown in Table 1 below, both the crystallization onset temperature (Tc) and the crystallization peak temperature (Tcp) are 150 for the green compact compared to the bulk sample. About 160 to 160 ° C.

【0023】[0023]

【表1】 [Table 1]

【0024】これは、圧粉成型体は、その比表面積がバ
ルク試料のそれに比べて大きいため、結晶化ガラス粉末
表面からの結晶化(=結晶相の核生成、核成長)が促進
され易く、これによって結晶化温度が低温側へシフトし
たものである。
This is because the powder compact has a larger specific surface area than that of the bulk sample, so that crystallization (= nucleation and growth of crystal phase) from the crystallized glass powder surface is easily promoted. As a result, the crystallization temperature is shifted to a lower temperature side.

【0025】次に、図1から、圧粉成型体による粘度−
温度曲線は、ほぼ全体的にバルク試料による粘度−温度
曲線よりも大きく下回っており、また、粘度107Pa
・s付近よりも低粘度領域では、バルク試料による粘度
−温度曲線に近づいているものの、それよりも低粘度側
に位置していることが分かる。
Next, FIG. 1 shows that the viscosity of the green compact was
Temperature curve is almost entirely viscosity by bulk sample - is far below than the temperature curve, also viscosity 10 7 Pa
-It can be seen that, in the region of lower viscosity than near s, the viscosity-temperature curve of the bulk sample is close to but lower than the viscosity curve.

【0026】上述したように、GENT式は、被測定物
が非圧縮性流体と仮定できる場合に成立する粘度換算式
である。これに対して、無機粉末とビヒクルとをプレス
成型によって固めた圧粉成型体は、その焼成が進むに連
れて焼結収縮等に伴う体積変化が生じるため、これを非
圧縮性流体とみなすことができない。
As described above, the GENT equation is a viscosity conversion equation that is established when an object to be measured can be assumed to be an incompressible fluid. On the other hand, in the case of a green compact formed by press-molding an inorganic powder and a vehicle, the volume changes due to sintering shrinkage and the like occur as the firing proceeds. Can not.

【0027】つまり、単純に、バルク試料の場合と同様
にして、圧粉成型体の測定データをGENT式に適用
し、その結果を圧粉成型体の粘度を見なすことはでき
ず、GENT式を圧粉成型体にも適用できるようにする
ためには、GENT式中のパラメーターを補正しなけれ
ばならない。
That is, simply as in the case of the bulk sample, the measurement data of the green compact is applied to the GENT equation, and the result cannot be used to determine the viscosity of the green compact. In order to be applicable to a green compact, the parameters in the GENT equation must be corrected.

【0028】そのためには、まず、第1に、バルク試料
と圧粉成型体との実質的な体積の違いを補正するため、
圧粉成型体の見かけの体積に圧粉成型体中の結晶化ガラ
ス粉末の充填率を乗じた体積を、試料体積補正値V’と
し、このV’をGENT式に適用する。なお、結晶化ガ
ラス粉末の充填率は、結晶化ガラス粉末の粉体真比重、
調合比、圧粉成型体の重量から容易に算出できる。
For this purpose, first, in order to correct a substantial difference in volume between the bulk sample and the green compact,
The volume obtained by multiplying the apparent volume of the green compact by the filling rate of the crystallized glass powder in the green compact is defined as a sample volume correction value V ′, and this V ′ is applied to the GENT equation. Incidentally, the filling rate of the crystallized glass powder, the powder specific gravity of the crystallized glass powder,
It can be easily calculated from the mixing ratio and the weight of the green compact.

【0029】例えば、図2のフローチャートに示すよう
に、結晶化ガラス等の無機粉末の重量m1、真比重n1
圧粉成型体の試料重量m、無機粉末の調合量w1、ビヒ
クル成分の調合量w2を測定し、下式にしたがって、試
料体積補正値V’を算出することができる。
For example, as shown in the flowchart of FIG. 2, the weight m 1 of the inorganic powder such as crystallized glass, the true specific gravity n 1 ,
Sample weight m of the green compact, formulated amount w 1 of the inorganic powder, to measure the compounding amount w 2 of vehicle components, in accordance with the following equation, it is possible to calculate the sample volume correction value V '.

【0030】V’=m1/n1、m1=m×{w1/
(w1+w2)} 第2に、圧粉成型体の変位について焼結収縮が支配的な
温度領域では、焼結収縮に伴う試料変形速度を考慮する
ことが必要である。すなわち、図3に示すように、圧粉
成型体の見かけの試料変形速度は、塑性変形に伴う試料
変形速度と焼結収縮に伴う試料変形速度とが含まれてい
るため、この粘度領域については、それを相殺した試料
変形速度、すなわち試料変形速度補正値(dh/d
t)’をGENT式に適用しなければならない。
V ′ = m1 / n1, m1 = m × {w1 /
(W1 + w2)} Secondly, in the temperature region where sintering shrinkage is dominant in the displacement of the green compact, it is necessary to consider the sample deformation speed due to sintering shrinkage. That is, as shown in FIG. 3, the apparent sample deformation rate of the green compact includes the sample deformation rate due to plastic deformation and the sample deformation rate due to sintering shrinkage. , The sample deformation speed that compensates for it, ie, the sample deformation speed correction value (dh / d
t) 'must be applied to the GENT equation.

【0031】ここで、図3に示すように、焼結収縮が支
配的な温度領域Xでは、荷重ゼロでの試料変形速度(d
h/dt)0を焼結収縮に伴う試料変形速度と見なすこ
とができる。したがって、この温度領域Xについての試
料変形速度を導き出すためには、荷重ゼロでの試料変形
速度(dh/dt)0を算出すればよい。
Here, as shown in FIG. 3, in the temperature region X where sintering shrinkage is dominant, the sample deformation rate (d
h / dt) 0 can be regarded as the sample deformation rate accompanying sintering shrinkage. Therefore, in order to derive the sample deformation speed in the temperature region X, the sample deformation speed (dh / dt) 0 at zero load may be calculated.

【0032】荷重ゼロでの試料変形速度(dh/dt)
0は、図3に示すように、荷重A、荷重B、・・・のよ
うに、荷重を振ったときの試料変形速度(dh/dt)
A、(dh/dt)B・・・を測定し、さらに、それぞれ
の温度における荷重と試料変形速度の関係が直線近似で
きると仮定したうえで荷重ゼロに外挿した値を荷重ゼロ
での試料変形速度(dh/dt)0として算出する。
Sample deformation speed at zero load (dh / dt)
0 is a sample deformation speed (dh / dt) when a load is shaken, as shown in FIG. 3, such as load A, load B,.
A , (dh / dt) B ... Were measured, and the value extrapolated to zero load was assumed for the sample at zero load, assuming that the relationship between the load at each temperature and the sample deformation rate could be linearly approximated. The deformation speed (dh / dt) is calculated as 0 .

【0033】具体的には、図4のフローチャートに示す
ように、圧粉成型体について、温度T1のときの荷重A
での試料変形速度(dh/dt)A、荷重Bでの試料変
形速度(dh/dt)Bを測定する。そして、荷重Aで
の試料変形速度(dh/dt)A、荷重Bでの試料変形
速度(dh/dt)Bを用いて最小二乗法による直線近
似を実行することにより、温度T1のときの荷重ゼロで
の試料変形速度(dh/dt)0を算出する。
Specifically, as shown in the flow chart of FIG. 4, a load A at a temperature T 1 is applied to the green compact.
Sample deformation rate at (dh / dt) A, to measure the sample deformation rate (dh / dt) B at load B. By executing the linear fit according to the least square method using the sample deformation rate (dh / dt) A at load A, the sample deformation rate (dh / dt) B at load B, when the temperatures T 1 Calculate the sample deformation speed (dh / dt) 0 at zero load.

【0034】同様にして、温度T2、T3・・・のときの
荷重ゼロでの試料変形速度(dh/dt)0を算出し、
図5に示すように、荷重ゼロでの試料変形速度−温度曲
線((dh/dt)0−T曲線)を作製する。なお、荷
重Aでの試料変形速度−温度曲線、荷重Bでの試料変形
速度−温度曲線を作製し、これらの曲線から荷重ゼロの
での試料変形速度−温度曲線((dh/dt)0−T曲
線)を一括に算出することもできる。
Similarly, the sample deformation speed (dh / dt) 0 at zero load at the temperatures T 2 , T 3, ...
As shown in FIG. 5, a sample deformation speed-temperature curve ((dh / dt) 0 -T curve) at zero load is prepared. A sample deformation speed-temperature curve under load A and a sample deformation speed-temperature curve under load B were prepared. From these curves, a sample deformation speed-temperature curve at zero load ((dh / dt) 0 -T Curve) can be calculated at once.

【0035】次いで、図4のフローチャートに示すよう
に、焼結収縮が支配的な温度領域Xに適用する試料変形
速度補正値(dh/dt)’を算出する。この試料変形
速度補正値(dh/dt)’は、見かけの試料変形速度
と焼結収縮に伴う試料変形速度との差を取ることにより
算出できる。
Next, as shown in the flow chart of FIG. 4, a sample deformation speed correction value (dh / dt) ′ to be applied to the temperature region X where sintering shrinkage is dominant is calculated. The sample deformation speed correction value (dh / dt) 'can be calculated by taking the difference between the apparent sample deformation speed and the sample deformation speed accompanying sintering shrinkage.

【0036】具体的には、見かけの試料変形速度である
荷重Aでの試料変形速度(dh/dt)A、又は、荷重
Bでの試料変形速度(dh/dt)Bから、焼結収縮に
伴う試料変形速度である荷重ゼロでの試料変形速度(d
h/dt)0を差し引いた値を試料変形速度補正値(d
h/dt)’とすることができる。この操作を、温度T
1、T2、T3・・・について行い、各温度での試料変形
速度補正値(dh/dt)’を算出する。
Specifically, it is an apparent sample deformation speed.
Sample deformation rate under load A (dh / dt)AOr load
Sample deformation speed at B (dh / dt)BFrom sintering shrinkage
The sample deformation speed at zero load, which is the sample deformation speed (d
h / dt)0Is subtracted from the sample deformation speed correction value (d
h / dt) '. This operation is performed at the temperature T
1, TTwo, TThree…, Deformation of the sample at each temperature
The speed correction value (dh / dt) 'is calculated.

【0037】さらに、図4のフローチャートに示すよう
に、焼結収縮が支配的な温度領域Xと、塑性変形が支配
的な温度領域Yとを分離する。この分離は、図5に示し
た荷重ゼロのときの試料変形速度−温度曲線((dh/
dt)0−T曲線)に基づき実行できる。
Further, as shown in the flowchart of FIG. 4, a temperature region X in which sintering shrinkage is dominant and a temperature region Y in which plastic deformation is dominant are separated. This separation is caused by the sample deformation rate-temperature curve ((dh /
dt) 0 -T curve).

【0038】具体的には、図5に示すように、荷重ゼロ
での試料変形速度−温度曲線((dh/dt)0−T曲
線)における極小値を、その境界温度Tbと見なし、境
界温度Tbよりも低温度側を焼結収縮が支配的な温度領
域X、境界温度Tbよりも高温度側を塑性変形が支配的
な温度領域Yとする。
Specifically, as shown in FIG. 5, the minimum value in the sample deformation speed-temperature curve ((dh / dt) 0 -T curve) at zero load is regarded as its boundary temperature Tb, A temperature region lower than Tb is defined as a temperature region X in which sintering shrinkage is dominant, and a temperature region higher than the boundary temperature Tb is defined as a temperature region Y in which plastic deformation is dominant.

【0039】そして、図6に示すように、圧粉成型体の
変位について、焼結収縮が支配的な温度領域Xでは、G
ENT式について、 試料体積V→試料体積補正値V’ 試料変形速度dh/dt→試料変形速度補正値(dh/
dt)’ の補正を実行し、他方、塑性変形が支配的な温度領域Y
では、GENT式について、 試料体積V→試料体積補正値V’ の補正を実行する。
As shown in FIG. 6, with respect to the displacement of the green compact, in the temperature region X where sintering shrinkage is dominant, G
Regarding the ENT equation, sample volume V → sample volume correction value V ′ sample deformation speed dh / dt → sample deformation speed correction value (dh /
dt) ′, while plastic deformation is dominant in the temperature region Y
Then, correction of the sample volume V → the sample volume correction value V ′ is performed for the GENT equation.

【0040】本発明によれば、こうした一連の操作によ
って、セラミック多層基板や厚膜材料等に用いられる無
機粉末の「粘度−温度曲線」を高精度に測定することが
でき、非晶質ガラスをはじめとして、結晶化ガラス、ガ
ラスセラミック複合材料等についても、その粉体状態に
極めて近い粘性挙動を示す圧粉成型体の粘度評価を行う
ことができるようになる。
According to the present invention, by such a series of operations, the "viscosity-temperature curve" of the inorganic powder used for the ceramic multilayer substrate, the thick film material and the like can be measured with high accuracy, and the amorphous glass can be used. First, it becomes possible to evaluate the viscosity of a green compact having a viscous behavior very close to the powder state of crystallized glass, glass ceramic composite material and the like.

【0041】すなわち、本発明の圧粉成型体の粘度測定
方法は、無機粉末をプレス成形してなる圧粉成型体の粘
度ηを、GENT式: η=2πMGH5/3V(dh/dt)(2πH3+V) (但し、M:荷重、H:試料高さ、G:重力加速度、
V:試料体積、dh/dt:試料変形速度)にしたがっ
て測定する、圧粉成型体の粘度測定方法であって、
(A)圧粉成型体の試料体積補正値V’(但し、試料体
積補正値V’は、前記圧粉成型体中の前記無機粉末が占
める体積)を求めるステップ、(B)前記圧粉成型体の
試料変形速度補正値(dh/dt)’(但し、試料変形
速度補正値(dh/dt)’は、見かけの試料変形速度
と焼結収縮に伴う試料変形速度との差)を求めるステッ
プ、(C)前記圧粉成型体の変位について、焼結収縮が
支配的な温度領域X、塑性変形が支配的な温度領域Yを
分離するステップ、(D)前記焼結収縮が支配的な温度
領域Xについては、前記GENT式の試料体積Vとして
前記試料体積補正値V’を適用し、かつ、試料変形速度
dh/dtとして前記試料変形速度補正値(dh/d
t)’を適用するステップ、(E)前記塑性変形が支配
的な温度領域Yについては、前記GENT式の試料体積
Vとして前記試料体積補正値V’を適用するステップ、
を有するものである。
That is, according to the method for measuring the viscosity of a green compact of the present invention, the viscosity η of a green compact obtained by press-molding an inorganic powder is determined by the GENT equation: η = 2πMGH 5 / 3V (dh / dt) ( 2πH 3 + V) (However, M: load, H: sample height, G: gravitational acceleration,
V: sample volume, dh / dt: sample deformation rate), which is a method for measuring the viscosity of a green compact,
(A) a step of obtaining a sample volume correction value V 'of the green compact (where the sample volume correction value V' is the volume occupied by the inorganic powder in the green compact); and (B) a green compact. Step of obtaining a sample deformation speed correction value (dh / dt) 'of the body (where the sample deformation speed correction value (dh / dt)' is the difference between the apparent sample deformation speed and the sample deformation speed due to sintering shrinkage). (C) separating a temperature region X where sintering shrinkage is dominant and a temperature region Y where plastic deformation is dominant with respect to the displacement of the green compact, and (D) a temperature where the sintering shrinkage is dominant. For the region X, the sample volume correction value V ′ is applied as the sample volume V of the GENT formula, and the sample deformation speed correction value (dh / d) is used as the sample deformation speed dh / dt.
(E) applying the sample volume correction value V 'as the sample volume V of the GENT equation for the temperature region Y in which the plastic deformation is dominant;
It has.

【0042】また、本発明の圧粉成型体の粘度測定方法
においては、前記見かけの試料変形速度として、荷重A
での試料変形速度(dh/dt)A、荷重Bでの試料変
形速度(dh/dt)Bをそれぞれ求め(但し、荷重A
≠荷重B)、前記荷重Aでの試料変形速度(dh/d
t)A、前記荷重Bでの試料変形速度(dh/dt)B
直線近似を行い、荷重ゼロの外挿値を荷重ゼロでの試料
変形速度(dh/dt)0として求め、前記荷重ゼロで
の試料変形速度(dh/dt)0を前記焼結収縮に伴う
試料変形速度と見なし、前記荷重Aでの試料変形速度
(dh/dt)A、又は、前記荷重Bでの試料変形速度
(dh/dt)Bから、前記荷重ゼロでの試料変形速度
(dh/dt)0を差し引いた値を、前記試料変形速度
補正値(dh/dt)’とすることができる。
In the method for measuring the viscosity of a green compact according to the present invention, a load A
The sample deformation speed (dh / dt) A at , and the sample deformation speed (dh / dt) B at load B are determined (however, the load A
≠ Load B), Sample deformation rate under the load A (dh / d
t) A, performs linear approximation of the sample deformation rate (dh / dt) B at the load B, obtains the extrapolated value of zero load as a sample deformation rate (dh / dt) 0 at zero load, the zero load The sample deformation rate (dh / dt) 0 at is regarded as the sample deformation rate due to the sintering shrinkage, and the sample deformation rate (dh / dt) A at the load A or the sample deformation rate at the load B ( A value obtained by subtracting the sample deformation speed (dh / dt) 0 at zero load from dh / dt) B can be used as the sample deformation speed correction value (dh / dt) ′.

【0043】但し、3点以上の異なる荷重(例えば、荷
重A、荷重B及び荷重C:但し、荷重A≠荷重B≠荷重
C)での試料変形速度から、荷重ゼロでの試料変形速度
(dh/dt)0を直線近似によって求めることが望ま
しい。その方が荷重ゼロでの試料変形速度(dh/d
t)0をより正確に抽出できるからである。
However, from the sample deformation speed at three or more different loads (for example, load A, load B and load C: where load A ≠ load B ≠ load C), the sample deformation speed at zero load (dh) / Dt) It is desirable to obtain 0 by linear approximation. The sample deformation rate at zero load (dh / d
This is because t) 0 can be extracted more accurately.

【0044】この場合、特に、前記荷重Aと前記荷重B
の関係を、荷重A<荷重Bとし、荷重Bでの試料変形速
度(dh/dt)Bと、前記荷重ゼロでの試料変形速度
(dh/dt)0との差を前記試料変形速度補正値(d
h/dt)’とすることが望ましい。試料変形速度補正
値(dh/dt)’を算出する際の見かけの試料変形速
度を荷重小のときの試料変形速度とすると、試料変形速
度補正値を抽出する際のバラツキが大きくなってしまう
傾向がある。
In this case, in particular, the load A and the load B
Is the load A <load B, and the difference between the sample deformation speed (dh / dt) B at load B and the sample deformation speed (dh / dt) 0 at zero load is the sample deformation speed correction value. (D
h / dt) ′. If the apparent sample deformation speed at the time of calculating the sample deformation speed correction value (dh / dt) ′ is the sample deformation speed when the load is small, the variation in extracting the sample deformation speed correction value tends to increase. There is.

【0045】また、本発明の圧粉成型体の粘度測定方法
においては、前記荷重ゼロでの試料変形速度(dh/d
t)0にしたがって荷重ゼロでの試料変形速度−温度曲
線を作製し、その極小値を境界温度Tbとして、境界温
度Tbよりも低温側を前記焼結収縮が支配的な温度領域
X、境界温度Tbよりも高温側を前記塑性変形が支配的
な温度領域Yとすることができる。
In the method of measuring the viscosity of a green compact according to the present invention, the sample deformation rate (dh / d
t) A sample deformation speed-temperature curve at zero load is prepared according to 0 , and a minimum value thereof is defined as a boundary temperature Tb. The higher temperature side than Tb can be set as the temperature region Y where the plastic deformation is dominant.

【0046】但し、境界温度の抽出方法は、上記の方法
に限定されるものではなく、例えば、バルク試料につい
ての試料変形速度−温度曲線を作製し、荷重ゼロでの試
料変形速度−温度曲線が、バルク試料についての試料変
形速度−温度曲線に追随する温度領域を塑性変形が支配
的な温度領域Yと見なすこともできる。
However, the method of extracting the boundary temperature is not limited to the above method. For example, a sample deformation speed-temperature curve for a bulk sample is prepared, and the sample deformation speed-temperature curve at zero load is obtained. The temperature region following the sample deformation speed-temperature curve of the bulk sample can be regarded as a temperature region Y in which plastic deformation is dominant.

【0047】また、本発明の圧粉成型体の粘度測定方法
においては、前記見かけの試料変形速度、すなわち、荷
重Aでの試料変形速度(dh/dt)A、荷重Bでの試
料変形速度(dh/dt)Bを、平行板加圧粘度計によ
って測定することができる。3点以上の異なる荷重につ
いての試料変形速度を測定する際にも、同様の平行板加
圧粘度計を用いることができる。なお、この平行板加圧
粘度計は、図15に示したように、平行板の間に被測定
物(圧粉成型体)を挟み込み、一定荷重を加えながら昇
温させることによって、被測定物の試料変形速度を検出
する装置である。
Further, in the method of measuring the viscosity of a green compact according to the present invention, the apparent sample deformation speed, ie, the sample deformation speed (dh / dt) A under the load A , and the sample deformation speed (D) under the load B ( dh / dt) B can be measured by a parallel plate pressure viscometer. A similar parallel plate pressure viscometer can be used when measuring the sample deformation rate for three or more different loads. As shown in FIG. 15, the parallel plate pressure viscometer sandwiches the object to be measured (compact molded body) between the parallel plates and raises the temperature while applying a constant load, thereby obtaining a sample of the object to be measured. This is a device that detects the deformation speed.

【0048】また、本発明の圧粉成型体の粘度測定方法
においては、前記無機粉末として、結晶化ガラス粉末、
非晶質ガラス粉末、及び、ガラスセラミック複合粉末か
らなる群より選ばれる1種の酸化物無機粉末を使用する
ことができる。これら粉末の粘度を測定することによっ
て、セラミック多層基板や厚膜材料の特性を制御コント
ロールする粘度パラメータを正確に把握することができ
る。
In the method for measuring the viscosity of a green compact according to the present invention, a crystallized glass powder,
One kind of oxide inorganic powder selected from the group consisting of amorphous glass powder and glass-ceramic composite powder can be used. By measuring the viscosities of these powders, it is possible to accurately grasp the viscosity parameters that control and control the characteristics of the ceramic multilayer substrate and the thick film material.

【0049】なお、本発明においては、これらの酸化物
無機粉末をプレス成形してなる圧粉成型体の粘度測定に
限定されるものではなく、例えば、酸化物セラミック粉
末、非酸化物系セラミック粉末の粘度測定にも応用可能
である。
The present invention is not limited to the measurement of the viscosity of a green compact formed by press-molding these oxide inorganic powders. For example, oxide ceramic powder, non-oxide ceramic powder It can also be applied to the viscosity measurement.

【0050】次に、本発明の圧粉成型体の粘度測定装置
を説明する。
Next, an apparatus for measuring the viscosity of a green compact according to the present invention will be described.

【0051】本発明の圧粉成型体の粘度測定装置は、無
機粉末をプレス成形してなる圧粉成型体の粘度ηを、G
ENT式: η=2πMGH5/3V(dh/dt)(2πH3+V) (但し、M:荷重、H:試料高さ、G:重力加速度、
V:試料体積、dh/dt:試料変形速度)にしたがっ
て測定する、圧粉成型体の粘度測定装置であって、
(a)前記圧粉成型体の形状実測値を測定する試料形状
測定部、(b)前記圧粉成型体の見かけの試料変形速度
を測定する試料変形速度測定部、(c)前記圧粉成型体
の形状実測値に基づいて、前記圧粉成型体中の前記無機
粉末が占める体積を算出し、これを試料体積補正値V’
として出力する演算処理手段、(d)前記見かけの試料
変形速度と、前記圧粉成型体の焼結収縮に伴う試料変形
速度の差を算出し、前記圧粉成型体の試料変形速度補正
値(dh/dt)’を出力する演算処理手段、(e)前
記圧粉成型体の変位について、焼結収縮が支配的な温度
領域X、塑性変形が支配的な温度領域Yの境界温度を策
定する演算処理手段、(f)前記焼結収縮が支配的な温
度領域Xについては、前記GENT式の試料体積Vとし
て前記試料体積補正値V’を適用し、かつ、試料変形速
度dh/dtとして前記試料変形速度補正値(dh/d
t)’を適用することにより、温度領域Xでの粘度ηを
出力する演算処理手段、(g)前記塑性変形が支配的な
温度領域Yについては、前記GENT式の試料体積Vと
して前記試料体積補正値V’を適用することにより、温
度領域Yでの粘度ηを出力する演算処理手段、(h)前
記温度領域Xでの粘度η、前記温度領域Yでの粘度ηを
表示する表示部、を備えるものである。
The apparatus for measuring the viscosity of a green compact according to the present invention measures the viscosity η of a green compact obtained by press-molding an inorganic powder.
ENT formula: η = 2πMGH 5 / 3V (dh / dt) (2πH 3 + V) (However, M: load, H: sample height, G: gravity acceleration,
V: a sample volume, dh / dt: sample deformation rate), which is a device for measuring the viscosity of a green compact,
(A) a sample shape measuring unit for measuring an actual measured value of the shape of the green compact; (b) a sample deformation speed measuring unit for measuring an apparent sample deformation speed of the green compact; (c) the green compacting Based on the measured shape of the body, the volume occupied by the inorganic powder in the green compact is calculated, and this is calculated as a sample volume correction value V ′.
(D) calculating the difference between the apparent sample deformation speed and the sample deformation speed associated with the sintering shrinkage of the green compact, and correcting the sample deformation speed of the green compact ( dh / dt) ′, and (e) formulating a boundary temperature between a temperature region X in which sintering shrinkage is dominant and a temperature region Y in which plastic deformation is dominant with respect to the displacement of the green compact. (F) For the temperature region X in which the sintering shrinkage is dominant, the sample volume correction value V ′ is applied as the sample volume V of the GENT equation, and the sample deformation speed dh / dt is set as the sample deformation speed dh / dt. Sample deformation speed correction value (dh / d
t) ′, an arithmetic processing means for outputting the viscosity η in the temperature region X, (g) in the temperature region Y where the plastic deformation is dominant, the sample volume V of the GENT equation is used as the sample volume Arithmetic processing means for outputting the viscosity η in the temperature region Y by applying the correction value V ′; (h) a display unit for displaying the viscosity η in the temperature region X and the viscosity η in the temperature region Y; It is provided with.

【0052】本発明の圧粉成型体の粘度測定装置におい
ては、前記見かけの試料変形速度として、荷重Aでの試
料変形速度(dh/dt)A、荷重Bでの試料変形速度
(dh/dt)Bをそれぞれ出力する試料変形速度測定
部(但し、荷重A≠荷重B)、前記荷重Aでの試料変形
速度(dh/dt)A、前記荷重Bでの試料変形速度
(dh/dt)Bの直線近似によって、荷重ゼロに外挿
した値、すなわち荷重ゼロでの試料変形速度(dh/d
t)0を出力する演算処理手段、前記荷重ゼロでの試料
変形速度(dh/dt)0を前記焼結収縮に伴う試料変
形速度と見なし、前記荷重Aでの試料変形速度(dh/
dt)A、又は、前記荷重Bでの試料変形速度(dh/
dt)Bから、前記荷重ゼロでの試料変形速度(dh/
dt)0を差し引いた値を、前記試料変形速度補正値
(dh/dt)’として出力する演算処理手段、をそれ
ぞれ備えていることが望ましい。
In the apparatus for measuring the viscosity of a green compact according to the present invention, the apparent sample deformation rate is a sample deformation rate (dh / dt) A under a load A , and a sample deformation rate (dh / dt) under a load B. ) A sample deformation speed measurement unit (where load A ≠ load B) that outputs B respectively, a sample deformation speed (dh / dt) A under the load A, and a sample deformation speed (dh / dt) B under the load B Is a value extrapolated to zero load, that is, the sample deformation rate at zero load (dh / d
t) 0, which outputs the sample deformation speed at the load A (dh / dt), considering the sample deformation speed at zero load (dh / dt) 0 as the sample deformation speed accompanying the sintering shrinkage.
dt) A or the sample deformation rate at the load B (dh /
dt) From B , the sample deformation rate at the zero load (dh /
dt) It is preferable that the apparatus further comprises arithmetic processing means for outputting a value obtained by subtracting 0 as the sample deformation speed correction value (dh / dt) ′.

【0053】また、本発明の圧粉成型体の粘度測定装置
は、前記荷重Aと前記荷重Bの関係を、荷重A<荷重B
とし、荷重Bでの試料変形速度(dh/dt)Bと、前
記荷重ゼロでの試料変形速度(dh/dt)0との差
を、前記試料変形速度補正値(dh/dt)’として出
力する演算処理手段を備えていることが望ましい。
Further, the apparatus for measuring the viscosity of a green compact according to the present invention determines the relationship between the load A and the load B by the following equation: load A <load B
The difference between the sample deformation speed at load B (dh / dt) B and the sample deformation speed at zero load (dh / dt) 0 is output as the sample deformation speed correction value (dh / dt) ′. It is desirable to provide arithmetic processing means for performing the above.

【0054】また、本発明の圧粉成型体の粘度測定装置
は、前記荷重ゼロでの試料変形速度(dh/dt)0
したがって荷重ゼロでの試料変形速度−温度曲線を作製
し、その極小値を境界温度Tbとして、境界温度Tbよ
りも低温側を前記焼結収縮が支配的な温度領域X、境界
温度Tbよりも高温側を前記塑性変形が支配的な温度領
域Yとして抽出する演算処理手段を備えていることが望
ましい。
The apparatus for measuring the viscosity of a green compact according to the present invention produces a sample deformation speed at zero load-temperature curve according to the sample deformation speed at zero load (dh / dt) 0 , With the value as the boundary temperature Tb, a calculation process for extracting a temperature lower than the boundary temperature Tb as a temperature region X in which the sintering shrinkage is dominant and extracting a temperature higher than the boundary temperature Tb as a temperature region Y in which the plastic deformation is dominant It is desirable to have means.

【0055】また、本発明の圧粉成型体の粘度測定装置
において、前記見かけの試料変形速度を実測する試料変
形速度測定部は、例えば図15に示したような平行板加
圧粘度計を備えていることが望ましい。
Further, in the apparatus for measuring the viscosity of a green compact according to the present invention, the sample deformation speed measuring section for actually measuring the apparent sample deformation speed includes, for example, a parallel plate pressure viscometer as shown in FIG. Is desirable.

【0056】また、本発明の圧粉成型体の粘度測定装置
は、前記の各演算処理手段を有したコンピュータを備え
ていることが望ましい。すなわち、上述した一連の演算
処理を実行するプログラムを備えたコンピュータを用い
れば、それに試料形状、試料変形速度等を入力するだけ
で、圧粉成型体の粘度ηが測定される。
Further, it is preferable that the apparatus for measuring the viscosity of a green compact according to the present invention comprises a computer having each of the above-mentioned arithmetic processing means. That is, if a computer having a program for executing the above-described series of arithmetic processing is used, the viscosity η of the green compact is measured simply by inputting the sample shape, the sample deformation speed, and the like.

【0057】次に、図7を参照に、本発明の圧粉成型体
の粘度測定装置について、その概略を説明する。
Next, an outline of the apparatus for measuring the viscosity of a green compact according to the present invention will be described with reference to FIG.

【0058】図7に示した圧粉成型体の粘度測定装置
は、圧粉成型体の高さ、体積、さらには無機粉末の重
量、充填率等の形状実測値を測定する試料形状測定部
(a)、複数の荷重について見かけの試料変形速度を実
測する試料変形速度測定部(b)、を備え、また、試料
形状測定部からの実測データに基づいて、圧粉成型体中
の無機粉末が占める体積を算出し、これを試料体積補正
値V’として出力する演算処理手段(c)、試料変形速
度測定部からの測定値に基づく見かけの試料変形速度
と、圧粉成型体の焼結収縮に伴う試料変形速度の差を算
出し、圧粉成型体の試料変形速度補正値(dh/d
t)’を出力する演算処理手段(d)、圧粉成型体の変
位について、焼結収縮が支配的な温度領域X、塑性変形
が支配的な温度領域Yの境界温度Tbを策定する演算処
理手段(e)、焼結収縮が支配的な温度領域Xについて
は、GENT式の試料体積Vとして試料体積補正値V’
を適用し、かつ、試料変形速度dh/dtとして試料変
形速度補正値(dh/dt)’を適用することにより、
温度領域Xでの粘度ηを出力する演算処理手段(f)、
塑性変形が支配的な温度領域Yについては、GENT式
の試料体積Vとして試料体積補正値V’を適用すること
により、温度領域Yでの粘度ηを出力する演算処理手段
(g)、からなる各演算処理手段を有し、さらに、温度
領域Xでの粘度η、温度領域Yでの粘度ηを表示する表
示部(h)、を具備している。
The apparatus for measuring the viscosity of a green compact shown in FIG. 7 uses a sample shape measuring section (a sample shape measuring section (height, volume, filling rate, etc.) of a green compact to measure actual measured values. a), a sample deformation speed measuring unit (b) for actually measuring an apparent sample deformation speed with respect to a plurality of loads, and based on actual measurement data from the sample shape measuring unit, the inorganic powder in the green compact is formed. An arithmetic processing means (c) for calculating the occupied volume and outputting this as a sample volume correction value V ', an apparent sample deformation speed based on a measurement value from a sample deformation speed measurement unit, and sintering shrinkage of the green compact; The difference in sample deformation speed due to the above is calculated, and the sample deformation speed correction value (dh / d
calculation processing means (d) for outputting t) ′, calculation processing for determining the boundary temperature Tb of the temperature region X where sintering shrinkage is dominant and the temperature region Y where plastic deformation is dominant for the displacement of the green compact. Means (e), for the temperature region X in which sintering shrinkage is dominant, the sample volume correction value V ′ is defined as the sample volume V in the GENT formula.
And applying the sample deformation speed correction value (dh / dt) ′ as the sample deformation speed dh / dt,
Arithmetic processing means (f) for outputting the viscosity η in the temperature region X;
An arithmetic processing unit (g) for outputting the viscosity η in the temperature region Y by applying the sample volume correction value V ′ as the sample volume V in the GENT equation for the temperature region Y where plastic deformation is dominant. A display unit (h) for displaying the viscosity η in the temperature region X and the viscosity η in the temperature region Y.

【0059】次に、この装置の具体的適用例について図
8を参照に説明する。
Next, a specific application example of this device will be described with reference to FIG.

【0060】まず、図8に示すように、試料形状測定部
10において、圧粉成型体の高さ(試料高さ)、体積
(試料体積)、重量(試料重量)、無機粉末の重量、真
比重、調合量、さらにはバインダ、溶剤等のビヒクル調
合量等を、ピクノメーターや電子天秤等によって正確に
測定する。
First, as shown in FIG. 8, in the sample shape measuring section 10, the height (sample height), volume (sample volume), weight (sample weight), weight of inorganic powder, The specific gravity, the amount of the mixture, and the amount of the vehicle such as the binder and the solvent are accurately measured by a pycnometer, an electronic balance, or the like.

【0061】他方、試料変形速度測定部11において、
荷重Aでの試料変形速度(dh/dt)A、荷重Bでの
試料変形速度(dh/dt)Bをそれぞれ実測する。な
お、平行板加圧粘度計を備える試料変形速度測定部の場
合、平行板加圧粘度計から経時的な温度データ及び試料
高さデータが出力されるので、これらのデータを加工す
ることによって(dh/dt)A、(dh/dt)Bをそ
れぞれ算出する。また、この実測データに基づいて、荷
重Aでの試料変形速度−温度曲線{(dh/dt)A
T曲線}、並びに、荷重Bでの試料変形速度−温度曲線
{(dh/dt)B−T曲線}を同時に作製する。
On the other hand, in the sample deformation speed measuring section 11,
Actually measured sample deformation rate at a load A (dh / dt) A, sample deformation rate of a load B a (dh / dt) B, respectively. In the case of a sample deformation rate measuring unit provided with a parallel plate pressure viscometer, temperature data and sample height data over time are output from the parallel plate pressure viscometer, and by processing these data, dh / dt) A and (dh / dt) B are calculated. Further, based on the actually measured data, the sample deformation rate at the load A-temperature curve {(dh / dt) A
A T curve} and a sample deformation rate-temperature curve under load B {(dh / dt) B -T curve} are simultaneously produced.

【0062】次いで、演算処理手段12において、試料
形状測定部10からの実測データに基づき、圧粉成型体
中の無機粉末が占める体積を算出し、これを試料体積補
正値V’として出力する。
Next, the arithmetic processing means 12 calculates the volume occupied by the inorganic powder in the green compact based on the actually measured data from the sample shape measuring section 10 and outputs this as a sample volume correction value V '.

【0063】また、演算処理手段13においては、試料
変形速度測定部11から出力された実測データ(或いは
加工済みデータ)に基づいて、荷重ゼロでの試料変形速
度(dh/dt)0を出力する。具体的には、荷重Aで
の試料変形速度(dh/dt)A、荷重Bでの試料変形
速度(dh/dt)Bについて最小二乗法を用いた直線
近似を実行することにより、外挿値として、荷重ゼロで
の試料変形速度(dh/dt)0を出力する。
The arithmetic processing means 13 outputs a sample deformation speed (dh / dt) 0 at zero load based on the actually measured data (or processed data) output from the sample deformation speed measuring section 11. . Specifically, by performing linear approximation using the least squares method the sample deformation rate at a load A (dh / dt) A, the sample deformation rate (dh / dt) B at load B, extrapolated value Output the sample deformation speed (dh / dt) 0 at zero load.

【0064】そして、演算処理手段14において、荷重
Aでの試料変形速度(dh/dt) A、又は、前記荷重
Bでの試料変形速度(dh/dt)Bから、荷重ゼロで
の試料変形速度(dh/dt)0を差し引いた値を試料
変形速度補正値(dh/dt)’として出力する。
Then, in the arithmetic processing means 14, the load
Sample deformation speed at A (dh / dt) AOr the load
Sample deformation speed at B (dh / dt)BFrom zero load
Sample deformation speed (dh / dt)0Subtract the value from the sample
It is output as a deformation speed correction value (dh / dt) '.

【0065】他方、演算処理手段15では、演算処理手
段13からの荷重ゼロでの試料変形速度−温度曲線
{(dh/dt)0−T曲線}にしたがい、その極小値
を抽出し、極小値を取るときの温度を境界温度Tbとし
て策定する。そして、境界温度Tbよりも低温側を焼結
収縮が支配的な温度領域X、境界温度Tbよりも高温側
を塑性変形が支配的な温度領域Yとして、演算処理手段
16、演算処理手段17にぞれぞれ出力する。
On the other hand, the arithmetic processing means 15 extracts the minimum value according to the sample deformation speed-temperature curve {(dh / dt) 0 -T curve} from the arithmetic processing means 13 when the load is zero, and extracts the minimum value. Is determined as the boundary temperature Tb. The lower temperature side of the boundary temperature Tb is defined as a temperature region X in which sintering shrinkage is dominant, and the higher temperature side of the boundary temperature Tb is defined as a temperature region Y in which plastic deformation is dominant. Output each one.

【0066】次いで、焼結収縮が支配的な温度領域Xに
ついて、演算処理手段12からの試料体積補正値V’、
演算処理手段14からの試料変形速度補正値(dh/d
t)’をそれぞれ演算処理手段18に入力する。他方、
塑性変形が支配的な温度領域Yについて、演算処理手段
12からの試料体積補正値V’を演算処理手段18に入
力する。
Next, for the temperature region X where sintering shrinkage is dominant, the sample volume correction value V ′,
The sample deformation speed correction value (dh / d
t) ′ are input to the arithmetic processing means 18. On the other hand,
The sample volume correction value V ′ from the arithmetic processing unit 12 is input to the arithmetic processing unit 18 for the temperature region Y in which plastic deformation is dominant.

【0067】次いで、演算処理手段18において、焼結
収縮が支配的な温度領域X、塑性変形が支配的な温度領
域Yについて、各補正値をGENT式へ上述したように
適用し、粘度ηを算出する。なお、GENT式において
は、圧粉成型体の試料高さHのデータが必要であるた
め、試料形状測定部10からこのデータを演算処理手段
18に入力する。
Next, the arithmetic processing means 18 applies the respective correction values to the GENT equation in the temperature region X where sintering shrinkage is dominant and the temperature region Y where plastic deformation is dominant as described above, and calculates the viscosity η. calculate. Since the data of the sample height H of the green compact is required in the GENT equation, this data is input from the sample shape measuring unit 10 to the arithmetic processing unit 18.

【0068】そして、演算処理手段18によって算出さ
れた粘度ηを、CRTやLCD等の表示部19にて表示
する。表示部19では、各温度における粘度ηを表形式
で表示してもよいし、粘度−温度曲線として表示するこ
ともできる。
Then, the viscosity η calculated by the arithmetic processing means 18 is displayed on a display unit 19 such as a CRT or LCD. In the display unit 19, the viscosity η at each temperature may be displayed in a table format, or may be displayed as a viscosity-temperature curve.

【0069】以上、本発明の圧粉成型体の粘度測定装置
によれば、上述した一連の操作によって、セラミック多
層基板や厚膜材料等に用いられる無機粉末の「粘度」を
効率良く測定することができ、非晶質ガラス粉末をはじ
めとして、結晶化ガラス、ガラスセラミック複合材料等
についても、その粉体状態に極めて近い粘性挙動を示す
圧粉成型体についての粘度評価を行うことができる。
According to the apparatus for measuring the viscosity of a green compact of the present invention, the "viscosity" of inorganic powder used for a ceramic multilayer substrate or a thick film material can be efficiently measured by the above-described series of operations. In addition to amorphous glass powder, crystallized glass, glass-ceramic composite materials, and the like, it is possible to evaluate the viscosity of a green compact having a viscous behavior very close to the powder state.

【0070】なお、本発明の圧粉成型体の粘度測定方法
を記録したコンピュータ読み取り可能な記録媒体は、上
述した本発明の圧粉成型体の粘度測定方法における一連
のステップを記録したコンピュータ読み取り可能な記録
媒体であり、例えば、コンピュータの磁気ディスクや半
導体メモリ等の記録媒体に記録させものや、持ち運び可
能な磁気テープや磁気ディスク、光ディスク等の記録媒
体である。
The computer-readable recording medium on which the method for measuring the viscosity of the compact of the present invention is recorded is a computer-readable recording medium on which a series of steps in the method for measuring the viscosity of the compact of the present invention described above are recorded. Examples of the recording medium include a recording medium such as a magnetic disk of a computer and a recording medium such as a semiconductor memory, and a recording medium such as a portable magnetic tape, a magnetic disk, and an optical disk.

【0071】[0071]

【実施例】以下、本発明を具体的な実施例について説明
する。試料作製 まず、SiO2−B23−Al23−CaO系の結晶化
ガラスを作製した。このガラスの組成系、粉体特性等を
下記表2に示す。
The present invention will be described below with reference to specific examples. Sample preparation was first produced crystallized glass of SiO 2 -B 2 O 3 -Al 2 O 3 -CaO based. Table 2 below shows the composition system, powder characteristics, and the like of this glass.

【0072】[0072]

【表2】 [Table 2]

【0073】次に、表2に示した組成系の結晶化ガラス
粉末にトルエン、エキネン等の有機ビヒクルを加え、ボ
ールミルを用いて混合、分散した。その後、これをプレ
ス金型(φ7mm)を用いてプレス成形し、高さ8〜
8.5mm、直径7〜7.5mmの円柱状圧粉成型体
(試料A、試料B、試料C)を作製した。そして、試料
A、試料B、試料Cについて、その直径、高さをマイク
ロメーターにて測定し、試料重量を電子天秤によって測
定した。試料形状の測定結果を下記表3に示す。
Next, an organic vehicle such as toluene or echinene was added to the crystallized glass powder having the composition shown in Table 2 and mixed and dispersed using a ball mill. Thereafter, this is press-formed using a press die (φ7 mm), and a height of 8 to
Columnar compacts having a diameter of 8.5 mm and a diameter of 7 to 7.5 mm (samples A, B, and C) were prepared. And about Sample A, Sample B, and Sample C, the diameter and height were measured with a micrometer, and the sample weight was measured with the electronic balance. Table 3 below shows the measurement results of the sample shapes.

【0074】[0074]

【表3】 [Table 3]

【0075】また、比較のため、表2に示した組成系の
ガラス粉末を用いて、バルク試料を作製した。このバル
ク試料は、ガラス粉末を白金るつぼ中に溶融温度165
0℃で流し込み、650℃から室温まで徐冷した後、試
料の平行度を出すため、研磨装置にて研磨を行った。得
られた試料は、高さ6mm、直径7mmの円柱状バルク
試料である。試料体積補正 次に、試料A、試料B、試料Cの試料体積補正値V’を
算出した。試料体積補正値V’は、各試料の見かけの体
積Vに結晶化ガラス粉末の充填率を乗じた値である。そ
の試料体積補正結果を下記表4に示す。
For comparison, a bulk sample was prepared using a glass powder having the composition shown in Table 2. This bulk sample was prepared by placing glass powder in a platinum crucible at a melting temperature of 165.
After pouring at 0 ° C. and gradually cooling from 650 ° C. to room temperature, the sample was polished with a polishing apparatus to obtain parallelism. The obtained sample is a cylindrical bulk sample having a height of 6 mm and a diameter of 7 mm. Sample Volume Correction Next, the sample volume correction values V ′ of the samples A, B, and C were calculated. The sample volume correction value V ′ is a value obtained by multiplying the apparent volume V of each sample by the filling rate of the crystallized glass powder. The results of the sample volume correction are shown in Table 4 below.

【0076】[0076]

【表4】 [Table 4]

【0077】試料変形速度補正並びに境界温度抽出 次に、圧粉成型体(試料A、試料B、試料C)につい
て、図15に示した構成のガラス平行板加圧粘度計(オ
プト企業社製)を用いて試料変形速度を測定した。試料
Aについては荷重56.8g、試料Bについては荷重1
38.8g、試料Cについては荷重408.8gを加
え、平行板加圧粘度計の昇温速度は5℃/分とした。ま
た、同様にしてバルク試料の試料変形速度を測定した
(荷重138.8g)。各温度における試料変形速度の
測定結果を図9に示す。
Correction of Sample Deformation Speed and Extraction of Boundary Temperature Next, for a green compact (sample A, sample B, sample C), a glass parallel plate pressure viscometer (manufactured by Opto Corporation) having the structure shown in FIG. Was used to measure the sample deformation rate. For sample A, load 56.8 g; for sample B, load 1
A load of 408.8 g was applied to 38.8 g of Sample C, and the rate of temperature rise of the parallel plate pressure viscometer was 5 ° C./min. Similarly, the sample deformation rate of the bulk sample was measured (load: 138.8 g). FIG. 9 shows the measurement results of the sample deformation speed at each temperature.

【0078】また、試料A(荷重56.8g)、試料B
(荷重138.8g)、試料C(荷重408.8g)に
ついて、図4に示したように、最小二乗法による直線近
似によって、荷重ゼロに外挿した値、すなわち荷重ゼロ
での試料変形速度(dh/dt)0を算出した。各温度
における荷重ゼロでの試料変形速度(dh/dt)0
図9に併せて示す。
Sample A (load: 56.8 g), Sample B
As shown in FIG. 4, a value extrapolated to zero load by a linear approximation by the least squares method, ie, a sample deformation rate at zero load (load: 138.8 g) and sample C (load: 408.8 g) ( dh / dt) 0 was calculated. FIG. 9 also shows the sample deformation rate (dh / dt) 0 at zero load at each temperature.

【0079】図9に示すように、荷重ゼロでの試料変形
速度(dh/dt)0とバルク試料の試料変形速度と
は、760℃付近までは両者の間に大きな相違が見られ
るが、760℃付近から830℃付近までは両者の試料
変形速度はほぼ一致する。なお、830℃付近以上では
両者が一致しないのは、圧粉成型体が結晶化し、荷重ゼ
ロでの試料変形速度がバルク試料の試料変形速度に追随
しなくなるためである。
As shown in FIG. 9, the sample deformation rate (dh / dt) 0 at zero load and the sample deformation rate of the bulk sample have a large difference up to around 760 ° C. From around ℃ to around 830 ° C, the sample deformation rates of both samples are almost the same. The reason why the two do not coincide with each other at about 830 ° C. or higher is that the green compact is crystallized and the sample deformation speed at zero load does not follow the sample deformation speed of the bulk sample.

【0080】このことから、760℃までは焼結収縮が
支配的な温度領域Xであると考えられる。したがって、
荷重ゼロでの試料変形速度(dh/dt)0を焼結収縮
に伴う変形速度とみなしてよい。そこで、760℃まで
の領域では、圧粉成型体の見かけの試料変形速度(つま
り、試料A、試料B又は試料Cの試料変形速度)の測定
値から、荷重ゼロでの試料変形速度(dh/dt)0
差し引いた値を試料変形速度補正値V’とする。
From this, it is considered that the temperature range X up to 760 ° C. is where the sintering shrinkage is dominant. Therefore,
The sample deformation speed (dh / dt) 0 at zero load may be regarded as the deformation speed accompanying sintering shrinkage. Therefore, in the region up to 760 ° C., the sample deformation rate (dh / dh) at zero load is determined from the measured value of the apparent sample deformation rate of the green compact (that is, the sample deformation rate of sample A, sample B or sample C). dt) The value obtained by subtracting 0 is defined as a sample deformation speed correction value V ′.

【0081】また、高荷重になるほど試料変形速度に対
する粘性流動の影響が大きくなり、焼結収縮に対する荷
重の影響が小さくなるので、ここでは、試料C(荷重4
08.8g)の試料変形速度から荷重ゼロでの試料変形
速度を差し引いた値を試料変形速度補正値(dh/d
t)’とした。
In addition, the higher the load, the greater the effect of viscous flow on the sample deformation rate and the smaller the effect of the load on sintering shrinkage.
The value obtained by subtracting the sample deformation speed at zero load from the sample deformation speed of 08.8 g) is the sample deformation speed correction value (dh / d).
t) ′.

【0082】また、760℃以上(830℃まで)は、
荷重ゼロでの試料変形速度(dh/dt)0がバルク試
料の試料変形速度に近似しており、粘性流動による塑性
変形が支配的な温度領域であると考えられる。但し、図
9から分かるように、荷重を大きくするにつれて、試料
変形速度−温度曲線が低温側にシフトしている(荷重が
56.8gでは、荷重ゼロとほぼ同様な挙動を示してい
る)。このことから、荷重を大きくすると塑性変形に荷
重の影響(=荷重によって焼結が促進される効果)によ
る試料変形が加わることが示唆されるが、GENT式で
荷重は考慮されており、この影響は粘度値に対して反映
されていると考えられる。
When the temperature is 760 ° C. or higher (up to 830 ° C.),
The sample deformation speed (dh / dt) 0 at zero load is close to the sample deformation speed of the bulk sample, and it is considered that the plastic deformation due to viscous flow is the dominant temperature region. However, as can be seen from FIG. 9, as the load is increased, the sample deformation speed-temperature curve shifts to a lower temperature side (when the load is 56.8 g, the behavior is almost the same as when the load is zero). This suggests that when the load is increased, sample deformation is added to the plastic deformation due to the effect of the load (= the effect of promoting the sintering by the load). However, the load is taken into account by the GENT formula, and this effect is considered. Is considered to be reflected on the viscosity value.

【0083】したがって、ここでは760℃を境界温度
とし、760℃よりも低温側を焼結収縮が支配的な温度
領域X、760℃よりも高温側を塑性変形が支配的な温
度領域Yとする。なお、図9に示した荷重ゼロでの試料
変形速度−温度曲線の極小値は、この境界温度と一致し
ており、荷重ゼロでの試料変形速度−温度曲線の極小値
は、焼結収縮が支配的な温度領域X、塑性変形が支配的
な温度領域Yの境界温度に相当していることが分かる。粘度の算出(GENT式への適用) 次に、以上のようにして求めた試料体積補正値V’、試
料変形速度補正値(dh/dt)’をGENT式に適用
し、各試料の粘度を測定する。すなわち、焼結収縮が支
配的な温度領域Xでは、GENT式の試料体積Vとして
試料体積補正値V’を適用し、かつ、試料変形速度dh
/dtとして試料変形速度補正値(dh/dt)’を適
用する。また、塑性変形が支配的な温度領域Yでは、G
ENT式の試料体積Vとして試料体積補正値V’を適用
する。
Therefore, here, the boundary temperature is set to 760 ° C., and the temperature range X where the sintering shrinkage is dominant on the side lower than 760 ° C. and the temperature range Y where the plastic deformation is dominant on the side higher than 760 ° C. . Note that the minimum value of the sample deformation speed-temperature curve at zero load shown in FIG. 9 matches this boundary temperature, and the minimum value of the sample deformation speed-temperature curve at zero load is that the sintering shrinkage is small. It can be seen that the dominant temperature region X and the plastic deformation correspond to the boundary temperature of the dominant temperature region Y. Calculation of Viscosity (Application to GENT Equation) Next, the sample volume correction value V ′ and the sample deformation speed correction value (dh / dt) ′ obtained as described above are applied to the GENT equation, and the viscosity of each sample is calculated. Measure. That is, in the temperature region X where sintering shrinkage is dominant, the sample volume correction value V ′ is applied as the sample volume V of the GENT equation, and the sample deformation speed dh
The sample deformation speed correction value (dh / dt) 'is applied as / dt. In the temperature region Y where plastic deformation is dominant, G
The sample volume correction value V ′ is applied as the sample volume V of the ENT formula.

【0084】GENT式にしたがって作製した粘度−温
度曲線を図10〜図12に示す。試料A(荷重56.8
g)についての粘度−温度曲線を図10、試料B(荷重
138.8g)についての粘度−温度曲線を図11、試
料C(荷重408.8g)についての粘度−温度曲線を
図12にそれぞれ示す。
The viscosity-temperature curves prepared according to the GENT equation are shown in FIGS. Sample A (load 56.8
FIG. 10 shows the viscosity-temperature curve for g), FIG. 11 shows the viscosity-temperature curve for sample B (load 138.8 g), and FIG. 12 shows the viscosity-temperature curve for sample C (load 408.8 g). .

【0085】また、試料A(荷重56.8g)、試料B
(荷重138.8g)、試料C(荷重408.8g)に
ついて、焼結収縮が支配的な温度領域X、塑性変形が支
配的な温度領域Y、生データ値(補正を行わずにGEN
T式に適用したときの値)及びバルク試料の温度と、粘
度との関係を下記表5に示す。
Sample A (load: 56.8 g), Sample B
(Load 138.8 g) and sample C (load 408.8 g), temperature region X where sintering shrinkage is dominant, temperature region Y where plastic deformation is dominant, raw data values (GEN without correction)
Table 5 below shows the relationship between the viscosity and the viscosity of the bulk sample (value when applied to the T formula).

【0086】[0086]

【表5】 [Table 5]

【0087】図10〜図12、表5から分かるように、
焼結収縮が支配的な温度領域Xでは、GENT式の試料
体積Vとして試料体積補正値V’を適用し、かつ、試料
変形速度dh/dtとして試料変形速度補正値(dh/
dt)’を適用することによって、また、塑性変形が支
配的な温度領域Yでは、GENT式の試料体積Vとして
試料体積補正値V’を適用することによって、バルク試
料における粘度測定結果とのずれを5℃〜10℃程度に
まで近づけることができた。なお、さらに試料体積(初
期値)の取り扱いやその他の誤差要因を補正すれば、そ
の粘性挙動をバルク試料のそれにより近づけることが可
能である。
As can be seen from FIGS. 10 to 12 and Table 5,
In the temperature region X where sintering shrinkage is dominant, the sample volume correction value V ′ is applied as the sample volume V in the GENT equation, and the sample deformation speed correction value (dh / dt) is used as the sample deformation speed dh / dt.
dt) ′, and in the temperature region Y where plastic deformation is dominant, by applying the sample volume correction value V ′ as the sample volume V of the GENT equation, the deviation from the viscosity measurement result in the bulk sample is obtained. Could be approached to about 5 ° C. to 10 ° C. If the handling of the sample volume (initial value) and other error factors are further corrected, the viscosity behavior can be made closer to that of the bulk sample.

【0088】また、図10〜図12、表5から分かるよ
うに、バルク試料については圧粉成型体で見られる結晶
化に起因する粘度上昇が見られないことが分かった。な
お、圧粉成型体の粘度上昇は、図13及び図14のDS
Cによる分析結果に示すように、結晶化開始温度Tcと
ほぼ一致していた。
As can be seen from FIGS. 10 to 12 and Table 5, it was found that the bulk sample did not show an increase in viscosity due to crystallization seen in the compact. The increase in the viscosity of the green compact was determined by the DS in FIGS. 13 and 14.
As shown in the analysis result by C, it almost coincided with the crystallization start temperature Tc.

【0089】以上、GENT式に対して、以下の補正を
行うことにより、圧粉成型体の粘度測定を高精度に効率
良く行うことができた。 (1)圧粉成型体の変位について、焼結収縮が支配的な
温度領域Xと、塑性変形が支配的な温度領域Yを分離。
つまり、試料変形速度(測定値)に含まれる焼結収縮に
伴う変形速度と塑性変形に伴う変形速度との分離。 (2)焼結収縮が支配的な温度領域Xでは、試料体積補
正、試料変形速度補正を実行。 (3)塑性変形が支配的な温度領域Yでは、試料体積補
正を実行。
As described above, by performing the following corrections to the GENT formula, the viscosity measurement of the compact was able to be performed with high precision and efficiency. (1) Regarding the displacement of the green compact, a temperature region X in which sintering shrinkage is dominant and a temperature region Y in which plastic deformation is dominant are separated.
In other words, the separation between the deformation speed associated with sintering shrinkage and the deformation speed associated with plastic deformation included in the sample deformation speed (measured value). (2) In the temperature region X where sintering shrinkage is dominant, sample volume correction and sample deformation speed correction are performed. (3) In the temperature region Y where plastic deformation is dominant, sample volume correction is performed.

【0090】[0090]

【発明の効果】本発明の圧粉成型体の粘度測定方法によ
れば、結晶化ガラス粉末、非晶質ガラス粉末、ガラスセ
ラミック複合粉末等の無機粉末をプレス成型してなる圧
粉成型体の粘度について、上述した各ステップにしたが
って測定するので、特に、焼結プロセス等で極めて重要
な104〜109Pa・Sの中粘度領域について、圧粉成
型体の粘性挙動を高精度に評価・測定できる。
According to the method for measuring the viscosity of a green compact according to the present invention, a green compact formed by press-molding an inorganic powder such as a crystallized glass powder, an amorphous glass powder or a glass-ceramic composite powder can be obtained. Since the viscosity is measured according to the above-described steps, the viscosity behavior of the green compact is evaluated with high accuracy, particularly in the medium viscosity range of 10 4 to 10 9 Pa · S, which is extremely important in the sintering process and the like. Can be measured.

【0091】本発明の圧粉成型体の粘度測定装置によれ
ば、無機粉末をプレス成型してなる圧粉成型体の粘度に
ついて、上述した試料形状測定部、試料変形速度測定部
並びに各演算処理手段を備えているので、圧粉成型体の
粘性挙動を効率良く測定することができる。
According to the apparatus for measuring the viscosity of a green compact according to the present invention, the viscosity of a green compact obtained by press-molding an inorganic powder is measured using the above-described sample shape measuring section, sample deformation rate measuring section, and various arithmetic processing. Since the means is provided, the viscous behavior of the green compact can be measured efficiently.

【0092】本発明の圧粉成型体の粘度測定方法を記録
したコンピュータ読み取り可能な記録媒体は、上述した
本発明の圧粉成型体の粘度測定方法を記録したコンピュ
ータ読み取り可能な記録媒体であり、これによって、本
発明の圧粉成型体の粘度測定方法について、保存が可能
となり、また、その技術移転を容易に行うことができ、
多数の者が容易に利用できるようになる。
The computer-readable recording medium on which the method for measuring the viscosity of the green compact according to the present invention is a computer-readable recording medium on which the method for measuring the viscosity of the green compact according to the present invention is described. Thereby, the method for measuring the viscosity of the green compact of the present invention can be stored, and the technology can be easily transferred.
Many people can use it easily.

【図面の簡単な説明】[Brief description of the drawings]

【図1】圧粉成型体とバルク試料の粘性挙動の違いを示
す粘度−温度曲線である。
FIG. 1 is a viscosity-temperature curve showing the difference in the viscosity behavior between a green compact and a bulk sample.

【図2】本発明の圧粉成型体の粘度測定方法について、
試料体積補正値の抽出ステップを説明するためのフロー
チャートである。
FIG. 2 shows a method for measuring the viscosity of a green compact according to the present invention.
5 is a flowchart for explaining a step of extracting a sample volume correction value.

【図3】本発明の圧粉成型体の粘度測定方法について、
試料変形速度補正を概念的に説明するための試料変形速
度−温度曲線である。
FIG. 3 shows a method for measuring the viscosity of a green compact according to the present invention.
5 is a sample deformation speed-temperature curve for conceptually explaining sample deformation speed correction.

【図4】本発明の圧粉成型体の粘度測定方法について、
試料変形速度補正値の抽出ステップ、並びに、焼結収縮
が支配的な温度領域と塑性変形が支配的な温度領域との
境界温度の策定ステップを説明するためのフローチャー
トである。
FIG. 4 shows a method for measuring the viscosity of a green compact according to the present invention.
5 is a flowchart for explaining a step of extracting a sample deformation speed correction value and a step of determining a boundary temperature between a temperature region in which sintering shrinkage is dominant and a temperature region in which plastic deformation is dominant.

【図5】本発明の圧粉成型体の粘度測定方法について、
焼結収縮が支配的な温度領域と塑性変形が支配的な温度
領域との境界温度策定を説明するための試料変形速度−
温度曲線である。
FIG. 5 shows a method for measuring the viscosity of a green compact according to the present invention.
Sample deformation rate to explain the boundary temperature between the temperature region where sintering shrinkage is dominant and the temperature region where plastic deformation is dominant-
It is a temperature curve.

【図6】本発明の圧粉成型体の粘度測定方法について、
GENT式への試料体積補正値、試料変形速度補正値の
適用方法を説明するためのフローチャートである。
FIG. 6 shows a method for measuring the viscosity of a green compact according to the present invention.
9 is a flowchart for explaining a method of applying a sample volume correction value and a sample deformation speed correction value to a GENT formula.

【図7】本発明の圧粉成型体の粘度測定装置についての
概略フロー図である。
FIG. 7 is a schematic flow chart of the apparatus for measuring the viscosity of a green compact of the present invention.

【図8】本発明の圧粉成型体の粘度測定装置についての
具体的な適用例を示すブロック図である。
FIG. 8 is a block diagram showing a specific application example of the viscosity measuring device for a green compact according to the present invention.

【図9】本発明の実施例の荷重による試料変形速度の相
違を示す試料変形速度−温度曲線である。
FIG. 9 is a sample deformation speed-temperature curve showing a difference in sample deformation speed due to a load in the example of the present invention.

【図10】本発明の実施例による試料A(荷重56.8
g)の粘度−温度曲線である。
FIG. 10 shows a sample A (with a load of 56.8) according to an embodiment of the present invention.
g) is a viscosity-temperature curve.

【図11】本発明の実施例による試料B(荷重138.
8g)の粘度−温度曲線である。
FIG. 11 shows a sample B (load 138. load) according to an embodiment of the present invention.
8g) is a viscosity-temperature curve.

【図12】本発明の実施例による試料C(荷重408.
8g)の粘度−温度曲線である。
FIG. 12 shows a sample C (with a load of 408.C.) according to the embodiment of the present invention.
8g) is a viscosity-temperature curve.

【図13】本発明の実施例による圧粉成型体についての
DSC分析結果を示すグラフである。
FIG. 13 is a graph showing a DSC analysis result of a green compact according to an example of the present invention.

【図14】本発明の実施例によるバルク試料についての
DSC分析結果を示すグラフである。
FIG. 14 is a graph showing a DSC analysis result of a bulk sample according to an example of the present invention.

【図15】平行板加圧粘度計の概略断面図である。FIG. 15 is a schematic sectional view of a parallel plate pressure viscometer.

【符号の説明】[Explanation of symbols]

1…被測定物 2a、2b…石英板 3…支持台 4…石英ロッド 5…ヒータ 6…装置 DESCRIPTION OF SYMBOLS 1 ... Measurement object 2a, 2b ... Quartz plate 3 ... Support base 4 ... Quartz rod 5 ... Heater 6 ... Device

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) G01N 11/00 - 11/16 G01N 3/00 JICSTファイル(JOIS)──────────────────────────────────────────────────続 き Continuation of the front page (58) Field surveyed (Int. Cl. 7 , DB name) G01N 11/00-11/16 G01N 3/00 JICST file (JOIS)

Claims (13)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 無機粉末をプレス成形してなる圧粉成型
体の粘度ηを、GENT式: η=2πMGH5/3V(dh/dt)(2πH3+V) (但し、M:荷重、H:試料高さ、G:重力加速度、
V:試料体積、dh/dt:試料変形速度)にしたがっ
て測定する、圧粉成型体の粘度測定方法であって、
(A)前記圧粉成型体の試料体積補正値V’(但し、試
料体積補正値V’は、前記圧粉成型体中の前記無機粉末
が占める体積)を求めるステップ、(B)前記圧粉成型
体の試料変形速度補正値(dh/dt)’(但し、試料
変形速度補正値(dh/dt)’は、見かけの試料変形
速度と焼結収縮に伴う試料変形速度との差)を求めるス
テップ、(C)前記圧粉成型体の変位について、焼結収
縮が支配的な温度領域X、塑性変形が支配的な温度領域
Yを分離するステップ、(D)前記焼結収縮が支配的な
温度領域Xについては、前記GENT式の試料体積Vと
して前記試料体積補正値V’を適用し、かつ、試料変形
速度dh/dtとして前記試料変形速度補正値(dh/
dt)’を適用するステップ、(E)前記塑性変形が支
配的な温度領域Yについては、前記GENT式の試料体
積Vとして前記試料体積補正値V’を適用するステッ
プ、を有することを特徴とする、圧粉成型体の粘度測定
方法。
1. The viscosity η of a green compact formed by press-molding an inorganic powder is determined by the GENT formula: η = 2πMGH 5 / 3V (dh / dt) (2πH 3 + V) (where M: load, H: Sample height, G: gravitational acceleration,
V: sample volume, dh / dt: sample deformation rate), which is a method for measuring the viscosity of a green compact,
(A) a step of determining a sample volume correction value V ′ of the green compact (where the sample volume correction value V ′ is the volume occupied by the inorganic powder in the green compact); The sample deformation speed correction value (dh / dt) 'of the molded body (where the sample deformation speed correction value (dh / dt)' is the difference between the apparent sample deformation speed and the sample deformation speed due to sintering shrinkage) is determined. (C) separating a temperature region X where sintering shrinkage is dominant and a temperature region Y where plastic deformation is dominant with respect to the displacement of the green compact, and (D) the sintering shrinkage is dominant. For the temperature region X, the sample volume correction value V ′ is applied as the sample volume V of the GENT equation, and the sample deformation speed correction value (dh / dh) is used as the sample deformation speed dh / dt.
dt) ′, and (E) applying the sample volume correction value V ′ as the sample volume V of the GENT equation for the temperature region Y where the plastic deformation is dominant. A method for measuring the viscosity of a green compact.
【請求項2】 前記見かけの試料変形速度として、荷重
Aでの試料変形速度(dh/dt)A、荷重Bでの試料
変形速度(dh/dt)Bをそれぞれ求め(但し、荷重
A≠荷重B)、前記荷重Aでの試料変形速度(dh/d
t)A、前記荷重Bでの試料変形速度(dh/dt)B
直線近似によって、荷重ゼロでの試料変形速度(dh/
dt)0を求め、 前記荷重ゼロでの試料変形速度(dh/dt)0を前記
焼結収縮に伴う試料変形速度と見なし、前記荷重Aでの
試料変形速度(dh/dt)A、又は、前記荷重Bでの
試料変形速度(dh/dt)Bから、前記荷重ゼロでの
試料変形速度(dh/dt)0を差し引いた値を、前記
試料変形速度補正値(dh/dt)’とすることを特徴
とする、請求項1に記載の圧粉成型体の粘度測定方法。
Wherein the sample deformation rate of the apparent determined sample deformation rate (dh / dt) A at load A, the sample deformation rate under a load B a (dh / dt) B respectively (where load A ≠ load B), the sample deformation rate under the load A (dh / d
t) A , Sample deformation speed at load B (dh / dt) By linear approximation of B , sample deformation speed at zero load (dh / dt)
dt) 0 is determined, and the sample deformation speed at the load of zero (dh / dt) 0 is regarded as the sample deformation speed accompanying the sintering shrinkage, and the sample deformation speed at the load A (dh / dt) A or from the sample deformation rate (dh / dt) B at the load B, and the value obtained by subtracting the sample deformation rate (dh / dt) 0 at the zero load, and the sample deformation rate correction value (dh / dt) ' The method for measuring the viscosity of a green compact according to claim 1, wherein:
【請求項3】 前記荷重Aと前記荷重Bの関係を、荷重
A<荷重Bとし、荷重Bでの試料変形速度(dh/d
t)Bと、前記荷重ゼロでの試料変形速度(dh/d
t)0との差を、前記試料変形速度補正値(dh/d
t)’とすることを特徴とする、請求項1又は2に記載
の圧粉成型体の粘度測定方法。
3. The relationship between the load A and the load B is defined as load A <load B, and the sample deformation speed (dh / d
t) B and the sample deformation rate at the zero load (dh / d)
t) The difference from 0 is calculated as the sample deformation speed correction value (dh / d
The method for measuring the viscosity of a green compact according to claim 1, wherein t) ′.
【請求項4】 前記荷重ゼロでの試料変形速度(dh/
dt)0にしたがって荷重ゼロでの試料変形速度−温度
曲線を作製し、その極小値を境界温度Tbとして、境界
温度Tbよりも低温側を前記焼結収縮が支配的な温度領
域X、境界温度Tbよりも高温側を前記塑性変形が支配
的な温度領域Yとすることを特徴とする、請求項1乃至
3のいずれかに記載の圧粉成型体の粘度測定方法。
4. The sample deformation rate at zero load (dh /
dt) A sample deformation speed-temperature curve at zero load is prepared according to 0 , and a minimum value thereof is defined as a boundary temperature Tb. The method for measuring the viscosity of a green compact according to any one of claims 1 to 3, wherein a higher temperature side than Tb is defined as a temperature region Y in which the plastic deformation is dominant.
【請求項5】 前記見かけの試料変形速度を平行板加圧
粘度計によって測定することを特徴とする、請求項1乃
至4のいずれかに記載の圧粉成型体の粘度測定方法。
5. The method of measuring the viscosity of a green compact according to claim 1, wherein the apparent deformation rate of the sample is measured by a parallel plate pressure viscometer.
【請求項6】 前記無機粉末を、結晶化ガラス粉末、非
晶質ガラス粉末、及び、ガラスセラミック複合粉末から
なる群より選ばれる1種の酸化物無機粉末とすることを
特徴とする、請求項1乃至5のいずれかに記載の圧粉成
型体の粘度測定方法。
6. The method according to claim 1, wherein the inorganic powder is one kind of oxide inorganic powder selected from the group consisting of crystallized glass powder, amorphous glass powder, and glass-ceramic composite powder. 6. The method for measuring the viscosity of a green compact according to any one of 1 to 5.
【請求項7】 無機粉末をプレス成形してなる圧粉成型
体の粘度ηを、GENT式: η=2πMGH5/3V(dh/dt)(2πH3+V) (但し、M:荷重、H:試料高さ、G:重力加速度、
V:試料体積、dh/dt:試料変形速度)にしたがっ
て測定する、圧粉成型体の粘度測定装置であって、
(a)前記圧粉成型体の形状実測値を測定する試料形状
測定部、(b)前記圧粉成型体の見かけの試料変形速度
を測定する試料変形速度測定部、(c)前記圧粉成型体
の形状実測値に基づいて、前記圧粉成型体中の前記無機
粉末が占める体積を算出し、これを試料体積補正値V’
として出力する演算処理手段、(d)前記見かけの試料
変形速度と、前記圧粉成型体の焼結収縮に伴う試料変形
速度の差を算出し、前記圧粉成型体の試料変形速度補正
値(dh/dt)’を出力する演算処理手段、(e)前
記圧粉成型体の変位について、焼結収縮が支配的な温度
領域X、塑性変形が支配的な温度領域Yの境界温度を策
定する演算処理手段、(f)前記焼結収縮が支配的な温
度領域Xについては、前記GENT式の試料体積Vとし
て前記試料体積補正値V’を適用し、かつ、試料変形速
度dh/dtとして前記試料変形速度補正値(dh/d
t)’を適用することにより、温度領域Xでの粘度ηを
出力する演算処理手段、(g)前記塑性変形が支配的な
温度領域Yについては、前記GENT式の試料体積Vと
して前記試料体積補正値V’を適用することにより、温
度領域Yでの粘度ηを出力する演算処理手段、(h)前
記温度領域Xでの粘度η、前記温度領域Yでの粘度ηを
表示する表示部、を備えることを特徴とする、圧粉成型
体の粘度測定装置。
7. The viscosity η of a green compact formed by press-molding an inorganic powder is determined by the GENT formula: η = 2πMGH 5 / 3V (dh / dt) (2πH 3 + V) (where M: load, H: Sample height, G: gravitational acceleration,
V: a sample volume, dh / dt: sample deformation rate), which is a device for measuring the viscosity of a green compact,
(A) a sample shape measuring unit for measuring an actual measured value of the shape of the green compact; (b) a sample deformation speed measuring unit for measuring an apparent sample deformation speed of the green compact; (c) the green compacting Based on the measured shape of the body, the volume occupied by the inorganic powder in the green compact is calculated, and this is calculated as a sample volume correction value V ′.
(D) calculating the difference between the apparent sample deformation speed and the sample deformation speed associated with the sintering shrinkage of the green compact, and correcting the sample deformation speed of the green compact ( dh / dt) ′, and (e) formulating a boundary temperature between a temperature region X in which sintering shrinkage is dominant and a temperature region Y in which plastic deformation is dominant with respect to the displacement of the green compact. (F) For the temperature region X in which the sintering shrinkage is dominant, the sample volume correction value V ′ is applied as the sample volume V of the GENT equation, and the sample deformation speed dh / dt is set as the sample deformation speed dh / dt. Sample deformation speed correction value (dh / d
t) ′, a processing means for outputting the viscosity η in the temperature region X, (g) in the temperature region Y where the plastic deformation is dominant, the sample volume V of the GENT formula is used as the sample volume Arithmetic processing means for outputting the viscosity η in the temperature region Y by applying the correction value V ′; (h) a display unit for displaying the viscosity η in the temperature region X and the viscosity η in the temperature region Y; A device for measuring the viscosity of a green compact, comprising:
【請求項8】 前記見かけの試料変形速度として、荷重
Aでの試料変形速度(dh/dt)A、荷重Bでの試料
変形速度(dh/dt)Bをそれぞれ出力する試料変形
速度測定部(但し、荷重A≠荷重B)、 前記荷重Aでの試料変形速度(dh/dt)A、前記荷
重Bでの試料変形速度(dh/dt)Bの直線近似によ
って、荷重ゼロに外挿した値、すなわち荷重ゼロでの試
料変形速度(dh/dt)0を出力する演算処理手段、 前記荷重ゼロでの試料変形速度(dh/dt)0を前記
焼結収縮に伴う試料変形速度と見なし、前記荷重Aでの
試料変形速度(dh/dt)A、又は、前記荷重Bでの
試料変形速度(dh/dt)Bから、前記荷重ゼロでの
試料変形速度(dh/dt)0を差し引いた値を、前記
試料変形速度補正値(dh/dt)’として出力する演
算処理手段、を備えることを特徴とする、請求項7に記
載の圧粉成型体の粘度測定装置。
8. As a sample deformation rate of the apparent sample deformation rate at a load A (dh / dt) A, the sample deformation rate (dh / dt) sample deformation rate measuring unit for outputting B each with a load B ( However, the load a ≠ load B), the load sample deformation rate (dh / dt in a) a, by the sample deformation rate (linear approximation of dh / dt) B at the load B, extrapolated to zero load value , i.e. the arithmetic processing means for outputting a sample deformation rate (dh / dt) 0 at zero load, the sample deformation rate (dh / dt) 0 at the zero load regarded as a sample deformation rate caused by the sintering shrinkage, the A value obtained by subtracting the sample deformation speed (dh / dt) 0 at the zero load from the sample deformation speed (dh / dt) A at the load A or the sample deformation speed (dh / dt) B at the load B. With the sample deformation speed correction value (dh / dt) ′ The viscosity measuring device for a green compact according to claim 7, further comprising an arithmetic processing unit that outputs the result.
【請求項9】 前記荷重Aと前記荷重Bの関係を、荷重
A<荷重Bとし、荷重Bでの試料変形速度(dh/d
t)Bと、前記荷重ゼロでの試料変形速度(dh/d
t)0との差を、前記試料変形速度補正値(dh/d
t)’として出力する演算処理手段を備えることを特徴
とする、請求項7又は8に記載の圧粉成型体の粘度測定
装置。
9. The relationship between the load A and the load B is defined as load A <load B, and the sample deformation speed (dh / d
t) B and the sample deformation rate at the zero load (dh / d)
t) The difference from 0 is calculated as the sample deformation speed correction value (dh / d
The device for measuring the viscosity of a green compact according to claim 7, further comprising an arithmetic processing unit that outputs the data as t) ′.
【請求項10】 前記荷重ゼロでの試料変形速度(dh
/dt)0にしたがって荷重ゼロでの試料変形速度−温
度曲線を作製し、その極小値を境界温度Tbとして、境
界温度Tbよりも低温側を前記焼結収縮が支配的な温度
領域X、境界温度Tbよりも高温側を前記塑性変形が支
配的な温度領域Yとして抽出する演算処理手段を備える
ことを特徴とする、請求項7乃至9のいずれかに記載の
圧粉成型体の粘度測定装置。
10. The sample deformation speed (dh) at zero load.
/ Dt) A sample deformation speed-temperature curve at zero load is prepared according to 0 , and a minimum value thereof is defined as a boundary temperature Tb. The viscosity measuring device for a green compact according to any one of claims 7 to 9, further comprising an arithmetic processing unit for extracting a higher temperature side than the temperature Tb as a temperature region Y in which the plastic deformation is dominant. .
【請求項11】 前記見かけの試料変形速度を測定する
試料変形速度測定部は平行板加圧粘度計を備えることを
特徴とする、請求項7乃至10のいずれかに記載の圧粉
成型体の粘度測定装置。
11. The green compact according to claim 7, wherein the sample deformation rate measuring unit for measuring the apparent sample deformation rate comprises a parallel plate pressure viscometer. Viscosity measuring device.
【請求項12】 前記の各演算処理手段を有したコンピ
ュータを備えることを特徴とする、請求項7乃至11の
いずれかに記載の圧粉成型体の粘度測定装置。
12. The apparatus for measuring the viscosity of a green compact according to claim 7, further comprising a computer having said arithmetic processing means.
【請求項13】 請求項1乃至6のいずれかに記載の圧
粉成型体の粘度測定方法をコンピュータに実行させるプ
ログラムを記録することを特徴とする、圧粉成型体の粘
度測定方法を記録したコンピュータ読み取り可能な記録
媒体。
13. A method for measuring the viscosity of a green compact, characterized by recording a program for causing a computer to execute the method for measuring the viscosity of a green compact according to any one of claims 1 to 6. Computer readable recording medium.
JP28321099A 1999-10-04 1999-10-04 Method for measuring viscosity of green compact, viscosity measuring device for green compact, and computer-readable recording medium recording viscosity measuring method for green compact Expired - Fee Related JP3344384B2 (en)

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DE10049022A DE10049022B4 (en) 1999-10-04 2000-10-04 Method and device for measuring the viscosity of green compacts and computer-readable recording medium for storing the method for measuring the viscosity of green compacts
US09/679,208 US6508106B1 (en) 1999-10-04 2000-10-04 Method and apparatus for measuring viscosity of green compact, and computer readable recording medium for storing method for measuring viscosity of green compact
US10/191,032 US6581439B2 (en) 1999-10-04 2002-07-02 Method and apparatus for measuring viscosity of green compact sample, and computer readable medium for storing method for measuring viscosity of green compact sample

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