JPH0441296B2 - - Google Patents
Info
- Publication number
- JPH0441296B2 JPH0441296B2 JP16392983A JP16392983A JPH0441296B2 JP H0441296 B2 JPH0441296 B2 JP H0441296B2 JP 16392983 A JP16392983 A JP 16392983A JP 16392983 A JP16392983 A JP 16392983A JP H0441296 B2 JPH0441296 B2 JP H0441296B2
- Authority
- JP
- Japan
- Prior art keywords
- particle
- particles
- concentration
- measurement
- centrifugal force
- 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
Links
- 239000002245 particle Substances 0.000 claims description 96
- 238000005259 measurement Methods 0.000 claims description 27
- 238000012937 correction Methods 0.000 claims description 14
- 238000001514 detection method Methods 0.000 claims description 11
- 238000013500 data storage Methods 0.000 claims description 10
- 230000000630 rising effect Effects 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 9
- 238000010586 diagram Methods 0.000 description 5
- 239000000725 suspension Substances 0.000 description 5
- 238000004062 sedimentation Methods 0.000 description 4
- 230000005540 biological transmission Effects 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 238000002835 absorbance Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000013459 approach Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 238000002834 transmittance Methods 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N15/00—Investigating characteristics of particles; Investigating permeability, pore-volume or surface-area of porous materials
- G01N15/04—Investigating sedimentation of particle suspensions
- G01N15/042—Investigating sedimentation of particle suspensions by centrifuging and investigating centrifugates
Landscapes
- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Physics & Mathematics (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Analytical Chemistry (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- General Physics & Mathematics (AREA)
- Immunology (AREA)
- Pathology (AREA)
- Length Measuring Devices By Optical Means (AREA)
- Sampling And Sample Adjustment (AREA)
Description
【発明の詳細な説明】
本発明は媒溶液中に均一に分散させた供試粒子
を遠心力下で上昇させ、ある上昇距離のところで
粒子濃度を検出し、粒子径に関する上昇速度の相
違を利用して供試粒子の粒度分布を求める装置に
関する。Detailed Description of the Invention The present invention involves raising test particles uniformly dispersed in a medium solution under centrifugal force, detecting the particle concentration at a certain lifting distance, and utilizing the difference in rising speed with respect to particle size. This invention relates to an apparatus for determining the particle size distribution of sample particles.
一般に、媒溶液中に媒溶液より密度の小さい粒
子を均一に分散させてこれに遠心力を付与すると
粒子は遠心力方向と反対方向に上昇し、その上昇
速度vは回転中心から粒子の存在点までの距離を
R、回転角速度をω、粒子密度をρp、、媒溶液密
度をρl、粒子径をDp、媒溶液粘度をηとすると、
v=Rω2(ρl−ρp)Dp2/18η……(1)
で表わされる。この式から明らかなように粒子径
Dpが大きい程粒子は速く上昇する。様々な粒子
からなる供試試料を媒溶液中に均一に分散させて
遠心力場にて上昇させる各粒子は(1)式に従つて粒
子径に応じた速度により上昇し、ある一定の浮上
距離のところでこの媒溶液中の濃度を時系列的に
測定して、その各測定点に対応する時間軸上の時
間t、すなわち遠心力付与開始時から各測定時ま
での時間tを測定し、(1)式を変形して距離Rで積
分して得られる
t={1.05η/N2(ρl−ρp)}
・log(R1/R2)・1/Dp2 ……(2)
ただし
N;単位時間(1秒)当り回転数
R2;回転中心と媒溶液容器底面との距離
R2;回転中心と測定位置との距離
によつて各測定点に対応する時間軸上の時間tを
粒子径Dpに換算することによつて、濃度測定位
置を上昇し終えたと考えられる各粒子径とそれに
対応する媒溶液濃度が求められたことになり、こ
れらによつて粒度分布を算出することができる。 Generally, when particles with a lower density than the medium solution are uniformly dispersed in a medium solution and a centrifugal force is applied to the particles, the particles rise in the opposite direction to the direction of the centrifugal force, and the rising speed v is from the center of rotation to the point where the particles exist. If the distance to R is R, the rotational angular velocity is ω, the particle density is ρp, the medium solution density is ρl, the particle diameter is Dp, and the medium solution viscosity is η, then v=Rω 2 (ρl−ρp) Dp 2 /18η… ...(1) As is clear from this formula, the particle size
The larger Dp is, the faster the particles rise. A test sample consisting of various particles is uniformly dispersed in a medium solution and raised in a centrifugal force field. Each particle rises at a speed according to the particle size according to equation (1), and reaches a certain floating distance. Now, the concentration in this medium solution is measured in time series, and the time t on the time axis corresponding to each measurement point, that is, the time t from the start of applying centrifugal force to the time of each measurement, ( t={1.05η/N 2 (ρl−ρp)} ・log(R 1 /R 2 )・1/Dp 2 ……(2) where N ; Number of revolutions per unit time (1 second) R 2 ; Distance between the center of rotation and the bottom of the medium solution container R 2 ; Calculate the time t on the time axis corresponding to each measurement point by the distance between the center of rotation and the measurement position. By converting to the particle size Dp, each particle size that is considered to have finished rising from the concentration measurement position and the corresponding concentration of the medium solution are determined, and the particle size distribution can be calculated from these. can.
上述の方法による粒度分布測定は、従来の沈降
式粒度分布測定装置では測定できなかつた媒溶液
より密度の小さい粒子の測定に応用されるもので
ある。遠心力場に於いては、上述した如く粒子は
遠心力の働く方向と反対方向に上昇するため、第
1図に示す如く粒子が回転中心に近づくに従つて
回転接線方向と半径方向の粒子間距離が縮小し、
媒溶液単位体積当りの粒子数すなわち濃度は増大
して検出される。 Particle size distribution measurement by the above-described method is applied to the measurement of particles whose density is smaller than that of a medium solution, which could not be measured using a conventional sedimentation type particle size distribution measuring device. In a centrifugal force field, as mentioned above, particles rise in the opposite direction to the direction in which centrifugal force acts, so as the particles approach the center of rotation, as shown in Fig. The distance is reduced,
An increasing number of particles or concentration per unit volume of medium solution is detected.
以上のことをよりわかりやすく説明する為に、
ある一種類の粒子のみからなる供試試料を考える
と、重力場に於いては第2図に示す如く、最初媒
溶液中の粒子は均一な状態に撹拌されているの
で、濃度測定位置に存在している粒子が上昇して
も同時にその下部から濃度測定位置に粒子が補給
されてその位置に於ける濃度は変化せず、媒溶液
容器の底面すなわち最下部に存在していたが粒子
が濃度測定位置を上昇通過して始めて濃度変化が
検出される。遠心力場に於いては、第3図に示す
如く上述の粒子間距離縮小によつて徐々に濃度が
増大、その後減少して検出される。以上のことは
多種類の粒度の粒子からなる試料についても同様
であり、遠心力場に於いては、濃度変化はある粒
度を持つ粒子が濃度測定位置を上昇通過し終えた
ことによるものと粒子間距離縮小によるものとを
含み、従つてこれによつて粒度分布を算出するこ
とは集中による誤差を含んでいる。 In order to explain the above more clearly,
Considering a test sample consisting of only one type of particles, in the gravitational field, as shown in Figure 2, the particles in the medium solution are initially stirred to a uniform state, so they are not present at the concentration measurement position. Even if the particles present at the bottom of the medium solution container rise, particles are simultaneously replenished from the bottom to the concentration measurement position, and the concentration at that position does not change. Concentration changes are detected only after passing over the measurement position. In the centrifugal force field, as shown in FIG. 3, the concentration gradually increases due to the aforementioned reduction in the distance between particles, and then decreases before being detected. The above is also true for samples made of particles of many different sizes; in a centrifugal force field, changes in concentration can be attributed to particles with a certain size finishing rising and passing through the concentration measurement position. Therefore, calculating the particle size distribution using this method includes errors due to concentration.
本発明は上記に鑑みなされたものであつて、遠
心力場に於ける粒子集中による誤差を自動的に補
正してより正しい粒度分布を求め得る粒度分布測
定装置の提供を目的とする。 The present invention has been made in view of the above, and an object of the present invention is to provide a particle size distribution measuring device that can automatically correct errors caused by particle concentration in a centrifugal force field to determine a more accurate particle size distribution.
以下、本発明実施例を図面に基づいて説明す
る。 Embodiments of the present invention will be described below based on the drawings.
第4図は本発明実施例の構成を示すブロツク図
である。 FIG. 4 is a block diagram showing the configuration of an embodiment of the present invention.
装置は、媒溶液中に均一に撹拌され懸濁液の状
態にされた試料を密封する容器1と、これを装着
する回転円盤2、その回転円盤2を回転駆動する
遠心器モータ3、回転中心から一定の距離に設け
られ回転中の懸濁液の濃度を光透過法により検出
する光源4とその光をスリツト6を介して受光す
る受光素子5および回転中の容器1がその光源4
の受光素子5に対して所定の位置にきたときのみ
受光素子5の出力を抽出する測定位置検出装置7
とから成る濃度検出装置、受光素子5の出力を増
巾する増巾器8およびそのアナログ量をデジタル
量に変換するA−D変換器9、試料に遠心力付与
してからの時間を計測するタイマ10、計測プロ
グラムや遠心力付与後の時間tと粒子径Dpに係
る上述の関数式(2)および後述する遠心力場に於け
る粒子拡散による誤差を補正する為の補正式を記
憶するプログラム記憶装置11、計測プログラム
の実行や上記関数式および上記補正式の演算を行
う演算制御装置12、およびそれに付属する入出
力ポート13,14、あらかじめ投入される測定
条件と上記関数式(2)および補正式により算出され
た値を逐次記憶するデータ記憶装置15、測定条
件や測定開始命令等を演算制御装置12に入力す
るためのキーボード16、演算制御装置12によ
つて算出された補正後の濃度に基づく粒度分布等
を表示する表示器17およびプリンタ18等から
成つている。 The apparatus consists of a container 1 that seals a sample that has been uniformly stirred into a suspension in a medium solution, a rotating disk 2 to which the container is attached, a centrifuge motor 3 that rotationally drives the rotating disk 2, and a rotation center. The light source 4 is located at a certain distance from the rotating suspension and detects the concentration of the rotating suspension by a light transmission method, the light receiving element 5 receives the light through the slit 6, and the rotating container 1 is connected to the light source 4.
measurement position detection device 7 that extracts the output of the light receiving element 5 only when it comes to a predetermined position with respect to the light receiving element 5;
an amplifier 8 that amplifies the output of the light-receiving element 5; an A-D converter 9 that converts the analog value into a digital value; and an A-D converter 9 that measures the time after centrifugal force is applied to the sample. Timer 10, a program that stores the measurement program, the above-mentioned functional equation (2) related to the time t after applying centrifugal force and the particle diameter Dp, and the correction equation for correcting errors due to particle diffusion in the centrifugal force field, which will be described later. A storage device 11, an arithmetic and control device 12 that executes the measurement program and calculates the above-mentioned function formula and the above-mentioned correction formula, and input/output ports 13 and 14 attached thereto, the measurement conditions entered in advance and the above-mentioned function formula (2) and A data storage device 15 that sequentially stores values calculated by the correction formula, a keyboard 16 for inputting measurement conditions, measurement start commands, etc. to the arithmetic and control device 12, and a concentration after correction calculated by the arithmetic and control device 12. It consists of a display 17 that displays the particle size distribution based on the data, a printer 18, and the like.
以上の様に構成された本発明実施例の作用を以
下に説明すると、粒度分布を測定しようとする試
料を媒溶液中に均一に分散する様撹拌して容器1
に封入して回転円盤2に装着する。キーボード1
6によつて測定開始命令を演算制御装置12に入
力すると、あらかじめプログラム記憶装置11に
記憶させてある計測プログラムに従つて入出力ポ
ート14を経て遠心器モータ3を回転させる為の
信号が出て遠心器モータ3は回転し容器1内の粒
子は回転内側に上昇し始める。その上昇速度vは
上述の式(1)に従い、大きな粒子程速く上昇する。
これを第4図に示す如く回転中心から一定の距離
のところで光源4および受光素子5によつて光透
過法によりその濃度を測定するとその時間−濃度
相関にて表わされる上昇過程曲線は第5図に示す
如くなる。すなわち上昇の初期では粒子の集中が
起り次に速度の速い大きな粒子が第4図の光線B
より回転中心に向つて上昇して行つて光線Bの位
置には存在しなくなり、時間が経過するに従い順
次小さな粒子も光線Bよりも内側に浮上する。こ
のように、上述の粒子間距離縮小のため検出濃度
は一度初期状態より大きくなりそして減少する。
プログラム記憶装置11にあらかじめ上述の関数
式(2)を記憶させておき、測定に先立つてキーボー
ド16によつて測定条件η、N、ρp、ρl、R1、
R2をデータ記憶装置15に記憶させる。回転し
ている容器1を通過する光源4からの光線Bを受
光する受光素子5からの出力信号をあらかじめプ
ログラム記憶装置1に記憶させてある計測プログ
ラムに従い一定時間毎に増巾器8、A−D変換器
9、入出力ポート13を介して演算制御装置12
に取り入れ、これを逐次データ記憶装置15に記
憶し、同時にタイマ10で計測される上記信号取
り入れに対応する遠心力付与開始後の時間tを上
記プログラム記憶装置11に記憶された関数式(2)
によつて演算制御装置12にて粒子径Dpに換算
してこれをデータ記憶装置15に記憶すると、デ
ータ記憶装置15には濃度検出位置を通過し終え
たと考えられる粒子径とそれに対応する試料の濃
度信号が記憶されていることになり、計測プログ
ラムに従つて測定終了後演算制御装置12にて粒
子径と粒子量との関係すなわち粒度分布を算出す
ることができる。しかしながら、上述した如く遠
心力場に於いては、試料の濃度信号には、粒子の
上昇方向に係る粒子間距離縮小にともなう粒子集
中による誤差が存在しているので、これを以下に
示す如く補正する。プログラム記憶装置11に、
上記の誤差を補正する下記の式を記憶させてお
く。Coを試料粒子の粒子径の無限に小さいとこ
ろすなわちDp=0のときのオーバーサイズ濃度、
C1、C2…C2nを遠心場に於ける集中を補正した後
のオーバーサイズ濃度、r1、r2…r2nを検出装置
から与えられた集中を補正する前の吸光度に係る
値、添字1…2nを粒子区間を表わす数字すなわ
ち数字が小さいと粒子径が小さいことを表わす数
字、kを回転中心から懸濁液の容器底面までの距
離と回転中心から濃度検出位置との距離によつて
決まる定数とすると、
C1=Co+2k/(1−2k)e2K-1・r1
上述の如く粒子径とそれに対応する濃度信号を
測定が終了するまである時間間隔毎にデータ記憶
装置15に取り入れ記憶させ、このときの濃度信
号は光源4と受光素子5とによる光透過法によつ
て得られる信号を増巾器8およびA−D変換器に
て所定の電気信号に変換された上記の補正式のr1
…r2nに当る。測定の終了はその濃度信号があら
かじめ計測プログラムに設定された一定値以下に
なつた時点として演算制御装置12にて判断さ
れ、濃度信号の取り入れ間隔は同じく計測プログ
ラムに設定された極く短い時間間隔とする。演算
制御装置12による上記補正式を用いた粒子集中
に起因する濃度検出誤差の補正の仕方は、上記の
測定終了時点におけるオーバーサイズ濃度すなわ
ち上記補正式のCoをCo=1とする。なぜならば、
粒子径の無限に小さいところすなわちDp=0よ
り試料の全粒子が大きいと考えられる為である。
そして上記濃度信号取り入れ間隔毎の遠心力付与
開始時よりのタイマ10による時間を上述の関数
式(2)により粒子径に換算してDp1…Dp2nとし、こ
れに対応する時間の濃度検出装置からのデータ記
憶装置15に記憶された濃度信号r1…r2nを計測
プログラムに従い上記補正式に順次代入して演算
制御装置12にて計算してデータ記憶装置15に
逐次記憶しておく。このCiが遠心力場に於ける粒
子の集中を補正したDpiよりも大きな粒子の濃度
すなわちオーバーサイズ濃度である。このデータ
記憶装置15のC1…C2nを表示器17あるいはプ
リンタ18に出力すると粒度分布が得られること
になる。 The operation of the embodiment of the present invention configured as described above will be explained below.A sample whose particle size distribution is to be measured is stirred in a medium solution and placed in a container.
and mounted on the rotating disk 2. keyboard 1
When a measurement start command is inputted to the arithmetic and control unit 12 by 6, a signal is outputted to rotate the centrifuge motor 3 via the input/output port 14 according to the measurement program stored in the program storage device 11 in advance. The centrifuge motor 3 rotates and the particles in the container 1 begin to rise inside the rotation. The rising speed v of the particle rises faster as the particle becomes larger, according to the above equation (1).
When the concentration is measured by the light transmission method using the light source 4 and the light receiving element 5 at a certain distance from the center of rotation as shown in FIG. 4, the rising process curve represented by the time-concentration correlation is shown in FIG. The result will be as shown below. In other words, at the beginning of the ascent, particles are concentrated, and large particles with the next highest velocity are ray B in Figure 4.
As the particles move higher toward the center of rotation, they no longer exist at the position of the light beam B, and as time passes, smaller particles also float to the inside of the light beam B. In this way, the detected concentration once becomes larger than the initial state and then decreases due to the aforementioned reduction in the interparticle distance.
The above function equation (2) is stored in advance in the program storage device 11, and measurement conditions η, N, ρp, ρl, R 1 ,
R 2 is stored in the data storage device 15. The output signal from the light receiving element 5 that receives the light beam B from the light source 4 passing through the rotating container 1 is sent to the amplifier 8, A- at regular intervals according to a measurement program stored in advance in the program storage device 1. Arithmetic and control device 12 via D converter 9 and input/output port 13
This is sequentially stored in the data storage device 15, and at the same time, the time t after the start of applying the centrifugal force corresponding to the signal reception, which is measured by the timer 10, is calculated by the function equation (2) stored in the program storage device 11.
When the arithmetic and control unit 12 converts the particle size Dp into a particle size Dp and stores it in the data storage device 15, the data storage device 15 stores the particle size that is considered to have passed the concentration detection position and the corresponding sample size. Since the concentration signal is stored, the relationship between the particle diameter and the particle amount, that is, the particle size distribution, can be calculated by the arithmetic and control unit 12 after the measurement is completed according to the measurement program. However, as mentioned above, in a centrifugal force field, there is an error in the concentration signal of the sample due to particle concentration due to a reduction in the distance between particles in the upward direction of the particles, so this can be corrected as shown below. do. In the program storage device 11,
The following formula for correcting the above error is memorized. Co is the oversize concentration at the infinitely small particle size of the sample particle, that is, when Dp = 0,
C 1 , C 2 ... C 2 n is the oversize concentration after correcting the concentration in the centrifugal field, r 1 , r 2 ... r 2 n is the absorbance given by the detection device before correcting the concentration. value, the subscript 1...2n is a number representing the particle section, that is, the smaller the number, the smaller the particle diameter, and k is the distance from the center of rotation to the bottom of the suspension container and the distance from the center of rotation to the concentration detection position. C 1 = Co + 2k/(1-2k)e 2K-1・r 1 As described above, the particle diameter and the corresponding concentration signal are taken and stored in the data storage device 15 at certain time intervals until the measurement is completed, and the concentration signal at this time is obtained by the light transmission method using the light source 4 and the light receiving element 5. r 1 of the above correction formula, which is converted into a predetermined electrical signal by the amplifier 8 and the A-D converter.
…corresponds to r 2 n. The end of the measurement is determined by the arithmetic and control unit 12 when the concentration signal becomes less than a certain value set in advance in the measurement program, and the interval at which the concentration signal is taken in is set at an extremely short time interval also set in the measurement program. shall be. The way the arithmetic and control unit 12 corrects the concentration detection error caused by particle concentration using the above correction equation is to set the oversize concentration at the end of the measurement, that is, Co in the above correction equation, to Co=1. because,
This is because all the particles in the sample are considered to be larger than the point where the particle diameter is infinitely small, that is, Dp=0.
Then, the time measured by the timer 10 from the start of centrifugal force application at each concentration signal intake interval is converted into a particle diameter using the above - mentioned function formula ( 2 ), and the concentration is detected at the corresponding time. Concentration signals r 1 ... r 2 n stored in the data storage device 15 from the device are sequentially substituted into the above correction formula according to the measurement program, calculated by the arithmetic and control device 12, and sequentially stored in the data storage device 15. . This Ci is the concentration of particles larger than Dpi, which corrects the concentration of particles in the centrifugal force field, that is, the oversize concentration. When the C 1 .
上述の本発明実施例の濃度取り入れ間隔は、上
述の如く決めてもよいし、あるいは記憶容量の少
ない場合には上記補正式を行う粒子径をあらかじ
め決めておき、関数式(2)によつてその粒子径に相
当する沈降時間を計算しそれらの沈降時間になつ
た時の濃度信号のみを記憶しておいてもよい。 The concentration intake interval in the embodiment of the present invention described above may be determined as described above, or if the storage capacity is small, the particle diameter for performing the above correction formula may be determined in advance, and the concentration intake interval may be determined using the function equation (2). It is also possible to calculate the sedimentation time corresponding to the particle size and to store only the concentration signal when the sedimentation time reaches the sedimentation time.
また、上述の実施例において濃度の検出に光を
使用したが、他の電磁波を使用してもよいし、吸
光度は透過率であつてもよい。また、無接触検出
でなく、たとえば直接サンプリング秤量という方
法でもよい。 Further, although light was used to detect the concentration in the above embodiments, other electromagnetic waves may be used, and the absorbance may be the transmittance. Moreover, instead of non-contact detection, for example, a method of direct sampling and weighing may be used.
以上説明した様に、本発明によつては遠心力場
に於ける粒子集中にともなう誤差を補正して粒度
分布を計算する為、より正確な粒度分布を求める
ことができ、第6図に従来装置による粒度分布測
定結果と本発明実施例による粒度分布測定結果を
オーバーサイズ濃度(%)で示すグラフを例とし
て掲げるが、この供試粒子は15μmから0μm付近
までの粒度範囲をもつ試料であつて従来装置によ
れば9μm以上の粒子が見掛け上存在していない
ものが、本発明実施例によると試料の粒度分布の
通り15μmまでの分布がされているのがよくわか
る。 As explained above, according to the present invention, since the particle size distribution is calculated by correcting the error caused by particle concentration in the centrifugal force field, a more accurate particle size distribution can be obtained. A graph showing the particle size distribution measurement results by the device and the particle size distribution measurement results by the examples of the present invention in terms of oversize concentration (%) is shown as an example, but the sample particles have a particle size range from 15 μm to around 0 μm. It can be clearly seen that although there are apparently no particles of 9 μm or more in the conventional apparatus, according to the present invention, particles of up to 15 μm are distributed according to the particle size distribution of the sample.
第1図は遠心力場に於ける粒子上昇の作用説明
図、第2図及び第3図は重量場および遠心力場で
の懸濁液濃度の特性図、第4図は本発明実施例の
構成を示すブロツク図、第5図は上昇過程の特性
曲線図、第6図は粒度分布測定の従来装置と本発
明実施例による比較を示すグラフである。
1……容器、2……回転円盤、3……遠心器モ
ータ、4……光源、5……受光素子、8……増巾
器、9……A−D変換器、10……タイマ、11
……プログラム記憶装置、12……演算制御装
置、15……データ記憶装置、16……キーボー
ド。
Fig. 1 is an explanatory diagram of the effect of particle rise in a centrifugal force field, Figs. 2 and 3 are characteristic diagrams of suspension concentration in a gravimetric field and a centrifugal force field, and Fig. 4 is an illustration of an example of the present invention. FIG. 5 is a block diagram showing the configuration, FIG. 5 is a characteristic curve diagram of the rising process, and FIG. 6 is a graph showing a comparison between a conventional particle size distribution measurement apparatus and an embodiment of the present invention. DESCRIPTION OF SYMBOLS 1... Container, 2... Rotating disk, 3... Centrifuge motor, 4... Light source, 5... Light receiving element, 8... Amplifier, 9... A-D converter, 10... Timer, 11
...Program storage device, 12... Arithmetic control device, 15... Data storage device, 16... Keyboard.
Claims (1)
する容器と;その容器を取り付けて供試粒子に遠
心力を与える為の遠心器と;供試粒子の上昇過程
に於ける粒子濃度を検出する検出装置と;その検
出値を所定の電気信号に変換する変換器と;遠心
力付与開始時点からの時間を計測する計時手段
と;粒子径に係る上昇速度を上昇時間に換算した
関数式と、遠心力場に於ける各粒子上昇軌跡の粒
子浮上距離に係る回転接線方向および半径方向粒
子間距離縮小にともなう粒子集中による上記検出
装置の検出誤差を補正する補正式と、計測プログ
ラムとを記憶するプログラム記憶装置と;上記計
測プログラムの実行と、上記計時手段による各経
過時間から上記関数式を用いた各粒子径の算出
と、全粒子浮上後上記補正式を用いて上記検出装
置の上記検出誤差の補正を実行する演算制御装置
と;あらかじめ投入される測定条件と、上記関数
式を用いて算出された各経過時間に関する各粒子
径と、上記検出装置による各経過時間毎の検出値
と、上記補正式を用いて算出される補正結果とを
逐次記憶するデータ記憶装置とを有し、上記検出
装置によつて得られる供給粒子の媒溶液内上昇過
程を示す粒子濃度変化曲線に含まれる遠心力場に
於ける粒子集中による誤差を補正してより正しい
粒度分布を求め得る粒度分布測定装置。1 A container for enclosing supply particles uniformly dispersed in a medium solution; A centrifuge for attaching the container to apply centrifugal force to the sample particles; Detecting the particle concentration in the rising process of the sample particles a converter that converts the detected value into a predetermined electric signal; a timer that measures the time from the start of applying centrifugal force; a functional formula that converts the rising speed related to the particle diameter into the rising time; , a correction formula for correcting the detection error of the above-mentioned detection device due to particle concentration due to a reduction in the distance between particles in the rotation tangential direction and radial direction related to the particle floating distance of each particle upward trajectory in a centrifugal force field, and a measurement program are stored. a program storage device that executes the measurement program, calculates each particle diameter using the function formula from each elapsed time by the time measurement means, and performs the detection by the detection device using the correction formula after all the particles float. an arithmetic and control device that performs error correction; measurement conditions entered in advance, particle diameters for each elapsed time calculated using the above functional formula, and detected values for each elapsed time by the detection device; a data storage device that sequentially stores the correction results calculated using the above correction formula; A particle size distribution measurement device that corrects errors caused by particle concentration in a force field to obtain a more accurate particle size distribution.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16392983A JPS6055245A (en) | 1983-09-05 | 1983-09-05 | Measuring device of particle size distribution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16392983A JPS6055245A (en) | 1983-09-05 | 1983-09-05 | Measuring device of particle size distribution |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6055245A JPS6055245A (en) | 1985-03-30 |
| JPH0441296B2 true JPH0441296B2 (en) | 1992-07-07 |
Family
ID=15783504
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16392983A Granted JPS6055245A (en) | 1983-09-05 | 1983-09-05 | Measuring device of particle size distribution |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6055245A (en) |
-
1983
- 1983-09-05 JP JP16392983A patent/JPS6055245A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6055245A (en) | 1985-03-30 |
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