JP3307082B2 - Particle size distribution analyzer - Google Patents

Particle size distribution analyzer

Info

Publication number
JP3307082B2
JP3307082B2 JP11419994A JP11419994A JP3307082B2 JP 3307082 B2 JP3307082 B2 JP 3307082B2 JP 11419994 A JP11419994 A JP 11419994A JP 11419994 A JP11419994 A JP 11419994A JP 3307082 B2 JP3307082 B2 JP 3307082B2
Authority
JP
Japan
Prior art keywords
sample
particle size
size distribution
stirring
suspension
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
JP11419994A
Other languages
Japanese (ja)
Other versions
JPH07294413A (en
Inventor
哲夫 西村
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.)
Shimadzu Corp
Original Assignee
Shimadzu Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shimadzu Corp filed Critical Shimadzu Corp
Priority to JP11419994A priority Critical patent/JP3307082B2/en
Publication of JPH07294413A publication Critical patent/JPH07294413A/en
Application granted granted Critical
Publication of JP3307082B2 publication Critical patent/JP3307082B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Sampling And Sample Adjustment (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】この発明は、レ−ザ−回折光散乱
を利用したオンライン粒度分布測定装置、より詳しくは
石炭灰、セメント等を生産する分野において使用される
希釈攪拌装置を備えたオンラインでの粒度分布測定装置
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an on-line particle size distribution measuring apparatus utilizing laser diffraction light scattering, and more particularly to an on-line apparatus equipped with a diluting / stirring apparatus used in the field of producing coal ash, cement and the like. And a particle size distribution measuring device.

【0002】[0002]

【従来の技術】一般に、図4に示すオンライン粒度分布
測定装置では、希釈攪拌装置31の攪拌槽32に入れた
水に試料投入管33の枝管34より粉末試料を投入し、
攪拌羽根35で良く攪拌された溶液をポンプ部6で粒度
分布測定部36のフロ−セル37に送りレ−ザ−光を透
過させて粒度分布を測定する。この場合、フロ−セル3
7を通過した溶液は再び攪拌槽32へ戻して循環させる
ようになっている。攪拌槽32の攪拌駆動やフロ−セル
37へのポンプ6による循環送水及び試料の投入操作等
は制御部(CPU)38によって行い、粒度分布測定部
36で測定されたデ−タはパソコン39へインプットし
て分析される。
2. Description of the Related Art In general, in an on-line particle size distribution measuring apparatus shown in FIG. 4, a powder sample is charged from a branch pipe 34 of a sample charging pipe 33 into water put in a stirring tank 32 of a dilution stirring apparatus 31.
The solution well stirred by the stirring blade 35 is sent to the flow cell 37 of the particle size distribution measuring unit 36 by the pump unit 6 and the laser light is transmitted to measure the particle size distribution. In this case, the flow cell 3
The solution that has passed through 7 is returned to the stirring tank 32 and circulated again. The stirring drive of the stirring tank 32, the circulating water supply by the pump 6 to the flow cell 37 and the operation of charging the sample are performed by the control unit (CPU) 38, and the data measured by the particle size distribution measuring unit 36 is sent to the personal computer 39. Input and analyzed.

【0003】図3(A)は従来の希釈攪拌装置31の詳
細図である。粉末試料を投入する試料投入管33にはエ
アノッカ40を設けて試料の付着と閉塞を防止するよう
にしてある。そして攪拌槽32内の溶液を攪拌する攪拌
羽根35はモ−タ41で駆動される軸42に取り付けら
れているが、該軸42には前記フロ−セル37へ送液す
るポンプ6のインペラ18が取り付けられ攪拌と同時に
回転駆動するようにしてある。図3(B)は図3(A)
のY−Y矢視図である。この攪拌槽32には液面センサ
43を設置して水道水用のバルブ11及び排水用のバル
ブ21を自動調節しながら水量を一定に保っている。ま
た、ポンプ6によって粒度分布測定部36のフロ−セル
37を通過した懸濁液は再び攪拌槽32に戻し循環させ
るようになっている。44は超音波振動子であって試料
が内壁やインペラ等に固着するのを防止するためのもの
である。
FIG. 3A is a detailed view of a conventional dilution and stirring device 31. An air knocker 40 is provided in the sample introduction pipe 33 into which the powder sample is introduced to prevent the sample from adhering and blocking. A stirring blade 35 for stirring the solution in the stirring tank 32 is attached to a shaft 42 driven by a motor 41. The shaft 42 has an impeller 18 of the pump 6 for feeding the solution to the flow cell 37. Is mounted and is driven to rotate simultaneously with stirring. FIG. 3 (B) is FIG. 3 (A)
FIG. A liquid level sensor 43 is provided in the stirring tank 32, and the amount of water is kept constant while automatically adjusting the valve 11 for tap water and the valve 21 for drainage. The suspension having passed through the flow cell 37 of the particle size distribution measuring section 36 by the pump 6 is returned to the stirring tank 32 and circulated. Reference numeral 44 denotes an ultrasonic vibrator for preventing the sample from sticking to an inner wall, an impeller, or the like.

【0004】[0004]

【発明が解決しようとする課題】上記する従来の希釈攪
拌装置31では、試料投入管33の枝管34から多量の
試料を一度に投入すると、粉体試料の表面引力が大きく
浸透が遅くなるため粉体試料がブロック状態で攪拌槽3
2の底部に沈降してポンプ6のインペラ18に固着し均
一な希釈攪拌が出来にくいという問題がある。また、攪
拌槽32の底面の高濃度液(スラリ−)はボ−ルバルブ
シ−ルを破損し測定フロ−セル37の汚れが著しく長期
測定が出来ないという問題がある。この発明はかかる課
題に鑑みてなされたものであり、投入した粉体試料が攪
拌途中でブロック化するのを防止して均一な懸濁液を得
やすく、また測定用フロ−セルも汚れにくく長期測定が
可能な粒度分布測定装置を提供することを目的とする。
In the above-mentioned conventional diluting and stirring apparatus 31, when a large amount of sample is injected at once from the branch pipe 34 of the sample input pipe 33, the surface attraction of the powder sample becomes large and the penetration becomes slow. Stirring tank 3 with powder sample in block
2 is settled at the bottom of the pump 2 and fixed to the impeller 18 of the pump 6, which makes it difficult to perform uniform dilution and stirring. Further, the high concentration liquid (slurry) on the bottom surface of the stirring tank 32 has a problem that the ball valve seal is broken and the measurement flow cell 37 is extremely contaminated, so that long-term measurement cannot be performed. The present invention has been made in view of the above problems, and prevents a charged powder sample from blocking during the stirring to easily obtain a uniform suspension. An object of the present invention is to provide a particle size distribution measuring device capable of measurement.

【0005】[0005]

【課題を解決するたの手段】即ち、この発明は上記する
課題を解決するために、 希釈攪拌装置と測定部との間
をポンプにより循環させて試料懸濁液の粒度分布を測定
するようにした粒度分布測定装置において、前記希釈攪
拌装置を、攪拌槽と、試料投入管と、内部が該試料投入
管と通じる細長い空間が形成され且つ側壁には多数の小
孔を穿設した攪拌器と、該試料投入管の回転駆動機構
と、で構成すると共に、前記試料投入管には試料投入部
と、水道水供給用管路若しくは粒度分布測定部からの試
料懸濁液を回帰させる循環用管路の少なくとも一方を配
置したことを特徴とする。
That is, in order to solve the above-mentioned problems, the present invention provides a method for measuring the particle size distribution of a sample suspension by circulating a pump between a dilution stirring device and a measuring section. In the particle size distribution measuring device, the dilution stirring device, a stirring tank, a sample introduction pipe, a stirrer in which an elongated space is formed in the interior and communicates with the sample introduction pipe, and a number of small holes are formed in the side wall. And a rotation mechanism for rotating the sample introduction tube, and a sample introduction unit and a circulation tube for returning the sample suspension from the tap water supply line or the particle size distribution measurement unit to the sample introduction tube. At least one of the roads is arranged.

【0006】[0006]

【作用】粒度分布測定装置を上記の手段とすると、試料
投入の際、試料投入管を駆動機構により回転駆動する
と、投入された試料は攪拌器の内部で水に溶けると共に
該攪拌器の小孔より攪拌槽内に分散されて行く。この場
合、試料投入管の上部から循環する試料懸濁液により攪
拌器内の粉末試料はより良く攪拌された状態で攪拌槽へ
分散されていく(図1参照)。
When the particle size distribution measuring device is the above-mentioned means, when the sample introduction tube is rotated by a drive mechanism at the time of sample introduction, the introduced sample dissolves in water inside the stirrer and the small hole of the stirrer. It is more dispersed in the stirring tank. In this case, the powder sample in the stirrer is dispersed into the stirring tank in a well-stirred state by the sample suspension circulating from the upper portion of the sample introduction pipe (see FIG. 1).

【0007】[0007]

【実施例】以下、この発明の具体的実施例について図面
を参照して説明する。図1(A)はこの発明の粒度分布
測定装で使用する希釈攪拌装置1の断面図である。この
希釈攪拌装置1は、攪拌槽2と試料投入管3と該試料投
入管3の回転駆動用モ−タ4とポンプ6と掻き取りワイ
ヤ8とで構成されている。前記試料投入管3には上部に
蓋7を載置するが、該蓋7には、試料投入部(投入用枝
管9)と掻き取りワイヤ8の回転駆動用モ−タ10とバ
ルブ11を設置した水道水供給用管路12と粒度分布測
定用フロ−セル37(図3参照)から懸濁液を回帰させ
る試料懸濁液循環用管路13とが設けられている(これ
らの管路12、13は図のように途中で一つの管路に合
流しても良い)。尚、前記試料投入管3はエアノッカ4
0で振動を与えるようにしてある。また、前記試料投入
管3にはプ−リ14が設けてありベルト駆動によりモ−
タ4で回転させるが該試料投入管3は他の回転駆動機構
であっても良い。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1A is a cross-sectional view of a dilution stirrer 1 used in the particle size distribution measuring device of the present invention. The dilution stirring apparatus 1 includes a stirring tank 2, a sample introduction pipe 3, a motor 4 for rotating the sample introduction pipe 3, a pump 6, and a scraping wire 8. A lid 7 is placed on the upper part of the sample input tube 3. The lid 7 is provided with a sample input section (input branch pipe 9), a motor 10 for rotationally driving the scraping wire 8, and a valve 11. The installed tap water supply line 12 and the sample suspension circulation line 13 for returning the suspension from the particle size distribution measurement flow cell 37 (see FIG. 3) are provided (these lines). 12 and 13 may be merged into one pipe as shown in the figure). The sample input tube 3 is connected to an air knocker 4.
Vibration is given at 0. Further, a pulley 14 is provided in the sample input tube 3 and is driven by a belt.
The sample input tube 3 may be another rotation driving mechanism.

【0008】前記試料投入管3の下部には後述する攪拌
器5が設けてあり、更に該攪拌器5の下側には軸15が
固定され、該軸15の先端部にはポンプ6のインペラ1
8を取り付けられている。このポンプ6を駆動すること
により粒度分布の測定部36のフロ−セル37(図3参
照)にバルブ19を配置した管路20より試料懸濁液が
送液され、バルブ21を配置した管路22からは懸濁液
が排水されるようになっている。また、前記攪拌槽2に
は液面センサ43が設置され前記バルブ11及び21を
制御することにより水が規定量満たされるようにしてあ
る。
A stirrer 5 to be described later is provided below the sample introduction pipe 3, and a shaft 15 is fixed below the stirrer 5, and an impeller of a pump 6 is attached to a tip end of the shaft 15. 1
8 is attached. By driving the pump 6, the sample suspension is sent to the flow cell 37 (see FIG. 3) of the particle size distribution measuring unit 36 from the pipe 20 in which the valve 19 is disposed, and the pipe in which the valve 21 is disposed. From 22, the suspension is drained. Further, a liquid level sensor 43 is provided in the stirring tank 2 and the valves 11 and 21 are controlled so that a predetermined amount of water is filled.

【0009】前記試料投入管3の上部に設置された蓋7
に取り付けられた掻き取りワイヤ8はモ−タ10により
回転駆動して投入試料を投入管3内で良く攪拌して該試
料がブロック状態となったり、管内壁に付着するのを防
止する役目をする。尚、試料投入管3自体をモ−タ4に
よって回転駆動するので掻き取りワイヤ8はモ−タ10
で駆動しなくても試料投入管3内を攪拌する役目をす
る。
A lid 7 installed on the upper part of the sample input tube 3
The scraping wire 8 attached to the motor is driven to rotate by the motor 10 to stir the input sample well in the input tube 3 to prevent the sample from blocking or adhering to the inner wall of the tube. I do. Since the sample input tube 3 itself is driven to rotate by the motor 4, the scraping wire 8 is connected to the motor 10.
This serves to stir the inside of the sample introduction tube 3 even if it is not driven.

【0010】次に、前記試料投入管3の下部に設けられ
た攪拌器5は、図1(A)のX−X矢視図である図1
(B)に示すように、内部には試料投入管3に通じる細
長い空間5aが形成され且つ側壁5b、5cには多数の
小孔5dが穿設さている。即ち、試料投入管3をモ−タ
4により回転駆動すると、投入された試料は攪拌器5の
内部で水に溶けると共に該攪拌器5の小孔5d、5dよ
り攪拌槽2内に分散されて行く。この場合、試料投入管
3の上部から循環する試料懸濁液により攪拌器5内の粉
末試料はより良く攪拌された状態で攪拌槽2へ分散され
ていく。
Next, the stirrer 5 provided at the lower part of the sample introduction tube 3 is a view taken along the line XX of FIG.
As shown in (B), an elongated space 5a communicating with the sample inlet tube 3 is formed inside, and a number of small holes 5d are formed in the side walls 5b and 5c. That is, when the sample input tube 3 is driven to rotate by the motor 4, the input sample is dissolved in water inside the stirrer 5 and dispersed into the stirring tank 2 through the small holes 5d and 5d of the stirrer 5. go. In this case, the powder sample in the stirrer 5 is dispersed into the stirring tank 2 in a well-stirred state by the sample suspension circulating from the upper part of the sample introduction pipe 3.

【0011】この粒度分布測定装置の希釈攪拌装置1は
以上のような構成から成り、図3に示す希釈攪拌装置3
1に代えて設置するが、次のように作動させる。 (1)希釈攪拌装置1の攪拌槽2には水道水を規定量満
たして待機させる。 (2)オンラインでの操作者の入力信号により掻き取り
ワイヤ8の駆動用モ−タ10、エアノッカ40、試料投
入管3を回転駆動するモ−タ4、ポンプ6等が動作して
試料投入用の枝管9よりラインから採取した試料を投入
する。 (3)投入された試料は試料投入管3内部の掻き取りワ
イヤ8及び循環用管路20から循環する懸濁液で混合さ
れ、攪拌器5の分散用小孔5dから攪拌槽2に分散され
る。 (4)試料の投入が終わればエアノッカ40は停止し、
攪拌槽2下部に設置された超音波振動子23が規定時間
動作する(この場合、掻き取りワイヤ8や試料投入管3
は回転駆動されている)。 (5)攪拌槽2のポンプ部6で駆動された試料懸濁液
は、図3に示す粒度分布測定部36のフロ−セル37に
おいて濃度チェックされ、規定濃度になるまで供給水
(水道水)用バルブ11とと試料排出用バルブ21との
調整を行いながら規定濃度範囲になるよう自動調整す
る。 (6)規定濃度となった試料懸濁液をフロ−セル37で
測定した後、水道水と排水管路22とで試料投入管3や
攪拌器5や攪拌槽2等の洗浄を行い、水の清浄度が測定
許容範囲となるまでフロ−セル37でチェックしながら
洗浄を繰り返す。 (7)攪拌槽2内が測定許容範囲となったら規定水量満
たして次の粒度分布測定のために待機する。
The diluting / stirring apparatus 1 of this particle size distribution measuring apparatus has the above-described configuration, and is a diluting / stirring apparatus 3 shown in FIG.
It is installed in place of 1, but operates as follows. (1) The stirring tank 2 of the dilution stirrer 1 is filled with a predetermined amount of tap water and put on standby. (2) The motor for driving the scraping wire 8, the air knocker 40, the motor 4 for rotating and driving the sample injection tube 3, the pump 6, etc. are operated by the input signal of the operator online to input the sample. A sample collected from the line through the branch pipe 9 is supplied. (3) The introduced sample is mixed with the scraping wire 8 inside the sample introduction tube 3 and the suspension circulating from the circulation line 20, and dispersed into the stirring tank 2 through the small holes 5 d of the stirring device 5. You. (4) When the sample has been charged, the air knocker 40 stops,
The ultrasonic vibrator 23 installed at the lower part of the stirring tank 2 operates for a specified time (in this case, the scraping wire 8 and the sample introduction pipe 3).
Is rotationally driven). (5) The concentration of the sample suspension driven by the pump unit 6 of the stirring tank 2 is checked in the flow cell 37 of the particle size distribution measuring unit 36 shown in FIG. While adjusting the valve 11 and the sample discharge valve 21, automatic adjustment is performed so as to be within a specified concentration range. (6) After measuring the sample suspension having the specified concentration with the flow cell 37, the sample injection pipe 3, the stirrer 5, the stirring tank 2, etc. are washed with tap water and the drain pipe 22, and the water is washed. The washing is repeated while checking with the flow cell 37 until the cleanliness of the sample is within the permissible range of measurement. (7) When the inside of the stirring tank 2 is within the measurement allowable range, the specified amount of water is filled and the apparatus stands by for the next particle size distribution measurement.

【0012】図2はこの発明の粒度分布測定装置で使用
する希釈攪拌装置の変形実施例である。即ち、図3
(A)に示す攪拌槽32に攪拌用の回転羽根35を取り
付けた軸42を設け、水道水及びフロ−セル37からの
試料懸濁液を循環させ、粉末試料を投入する試料投入管
33に掻き取りワイヤ8を垂設し、試料投入時該掻き取
りワイヤ8をモ−タ10で駆動するようにするものであ
る。このような構成により粉末試料を試料投入管33の
枝管34より投入しつつ攪拌槽32内の懸濁液を攪拌羽
根35で攪拌し且つ掻き取りワイヤ8を回転させれば試
料投入管33への試料の付着や攪拌時の試料のブロック
化を防止することが出来る。
FIG. 2 shows a modified embodiment of the dilution stirring device used in the particle size distribution measuring device of the present invention. That is, FIG.
A shaft 42 having a rotating blade 35 for stirring is provided in a stirring tank 32 shown in (A), and tap water and a sample suspension from a flow cell 37 are circulated, and the sample suspension tube 33 into which a powder sample is charged is provided. The scraping wire 8 is provided vertically, and the scraping wire 8 is driven by the motor 10 when a sample is loaded. With such a configuration, the suspension in the stirring tank 32 is stirred by the stirring blade 35 while the powder sample is injected from the branch pipe 34 of the sample injection pipe 33, and the scraping wire 8 is rotated. Of the sample and blocking of the sample during stirring can be prevented.

【0013】[0013]

【発明の効果】この発明の粒度分布測定装置は以上詳述
したような構成としたので、粉末試料が攪拌槽2内でブ
ロック状態になることはなく、また攪拌槽2の底部に沈
降してインペラ18等に固着することは殆どなくなる。
そしてバルブシ−ルの耐久性も向上し測定フロ−セルの
汚れも少なくなるので長期測定が可能となる。
According to the particle size distribution measuring apparatus of the present invention, the powder sample is not blocked in the stirring tank 2 and settles at the bottom of the stirring tank 2 because it has the configuration as described in detail above. It hardly adheres to the impeller 18 or the like.
Further, the durability of the valve seal is improved and the contamination of the measurement flow cell is reduced, so that long-term measurement can be performed.

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

【図1】図1(A)はこの発明の粒度分布測定装で使用
する希釈攪拌装置の断面図であり、図1(B)は図1
(A)のX−X矢視図である。
FIG. 1A is a cross-sectional view of a dilution stirrer used in the particle size distribution measuring apparatus of the present invention, and FIG.
It is an XX arrow line view of (A).

【図2】この発明の粒度分布測定装置で使用する希釈攪
拌装置の変形実施例を示す図である。
FIG. 2 is a view showing a modified embodiment of a dilution stirring device used in the particle size distribution measuring device of the present invention.

【図3】図3(A)は従来の希釈攪拌装置の詳細断面図
であり、図3(B)は図3(A)のY−Y矢視図であ
る。
FIG. 3 (A) is a detailed sectional view of a conventional dilution and stirring device, and FIG. 3 (B) is a view taken along the line YY of FIG. 3 (A).

【図4】オンライン粒度分布測定装置の構成概要を示す
図である。
FIG. 4 is a diagram showing a schematic configuration of an online particle size distribution measuring device.

【符号の説明】[Explanation of symbols]

1 希釈攪拌装置 2 攪拌槽 3 試料投入管 5 攪拌器 6 ポンプ 7 蓋 8 掻き取りワイヤ 9 試料投
入用枝管 11 バルブ 12 水道
水供給管路 13 懸濁液循環用管路 15 軸 18 インペラ 19、21 バル
ブ 36 粒度分布測定部 37 フロ−セル
DESCRIPTION OF SYMBOLS 1 Dilution stirrer 2 Stirring tank 3 Sample supply pipe 5 Stirrer 6 Pump 7 Lid 8 Scraping wire 9 Sample supply branch pipe 11 Valve 12 Tap water supply pipe 13 Suspension circulation pipe 15 Shaft 18 Impeller 19, 21 Valve 36 Particle size distribution measuring unit 37 Flow cell

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 希釈攪拌装置と測定部との間をポンプに
より循環させて試料懸濁液の粒度分布を測定するように
した粒度分布測定装置において、前記希釈攪拌装置を、
攪拌槽と、試料投入管と、内部が該試料投入管と通じる
細長い空間が形成され且つ側壁には多数の小孔を穿設し
た攪拌器と、該試料投入管の回転駆動機構と、で構成す
ると共に、前記試料投入管には試料投入部と、水道水供
給用管路若しくは粒度分布測定部からの試料懸濁液を回
帰させる循環用管路の少なくとも一方を配置したことを
特徴とする粒度分布測定装置。
1. A particle size distribution measuring device in which a particle suspension is circulated between a dilution stirring device and a measuring section by a pump to measure a particle size distribution of a sample suspension.
A stirring tank, a sample input tube, a stirrer having an elongated space formed therein communicating with the sample input tube and having a number of small holes formed in the side wall, and a rotation driving mechanism for the sample input tube. In addition, the sample introduction pipe is provided with a sample introduction section and at least one of a circulation pipe for returning the sample suspension from the tap water supply pipe or the particle size distribution measurement section. Distribution measuring device.
JP11419994A 1994-04-28 1994-04-28 Particle size distribution analyzer Expired - Fee Related JP3307082B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11419994A JP3307082B2 (en) 1994-04-28 1994-04-28 Particle size distribution analyzer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11419994A JP3307082B2 (en) 1994-04-28 1994-04-28 Particle size distribution analyzer

Publications (2)

Publication Number Publication Date
JPH07294413A JPH07294413A (en) 1995-11-10
JP3307082B2 true JP3307082B2 (en) 2002-07-24

Family

ID=14631693

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11419994A Expired - Fee Related JP3307082B2 (en) 1994-04-28 1994-04-28 Particle size distribution analyzer

Country Status (1)

Country Link
JP (1) JP3307082B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002062248A (en) * 2000-07-01 2002-02-28 Malvern Instruments Ltd Device and method for specifying particle size distribution
JP2002116134A (en) * 2000-10-10 2002-04-19 Shimadzu Corp Measuring apparatus for suspended particulate matter
JP6161922B2 (en) * 2013-03-12 2017-07-12 住友精密工業株式会社 Underwater combustion type vaporizer

Also Published As

Publication number Publication date
JPH07294413A (en) 1995-11-10

Similar Documents

Publication Publication Date Title
JP2008058163A (en) Automalyzer
JP3411111B2 (en) Sample stirring device and sample suction device
US5746983A (en) Apparatus and process for calcification
US6197256B1 (en) Device for analyzing fluid samples
JP3307082B2 (en) Particle size distribution analyzer
US6773672B2 (en) Automatic analysis apparatus
JP2000338113A (en) Chemical analyzer
CN204177625U (en) A kind of sampler measuring grain size of sediment
KR101593976B1 (en) Evaluation apparatus and method for agitator of drillship
JP3425093B2 (en) Drainage method of sample liquid and cleaning liquid in light scattering type particle size distribution measuring device
JP2570823B2 (en) Suspension sampling device for particle size distribution measurement
WO1999046601A1 (en) Automatic analyzer and automatic analysis method
CN215169836U (en) Drilling fluid sedimentation stability monitoring devices
KR100275801B1 (en) Automatic measuring equipment for physical properties of cellulose derivative solution
US3456494A (en) Method and apparatus for determining the viscosity of fluids
JPH06103296B2 (en) Coagulation sedimentation test equipment
JP3422699B2 (en) Particle size distribution analyzer
JPH0712821A (en) Sample mixing device and fluorescence detector using the device
KR100848505B1 (en) Device for solidifying radioactive waste
KR100934097B1 (en) Scour rate measuring device
JP4505158B2 (en) Particle size distribution measuring device and control program for particle size distribution measuring device
US5849064A (en) System and method for evenly suspending and circulating particles in a liquid
JPH0587725A (en) Grain size distribution measuring device
JP3422707B2 (en) Light scattering particle size distribution analyzer
KR20040049129A (en) An apparatus for automatically picking liquid sample

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080517

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090517

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100517

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100517

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110517

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110517

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120517

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130517

Year of fee payment: 11

LAPS Cancellation because of no payment of annual fees