JPH0645015B2 - Method for adjusting particle size distribution of high-concentration coal water slurry - Google Patents

Method for adjusting particle size distribution of high-concentration coal water slurry

Info

Publication number
JPH0645015B2
JPH0645015B2 JP23630484A JP23630484A JPH0645015B2 JP H0645015 B2 JPH0645015 B2 JP H0645015B2 JP 23630484 A JP23630484 A JP 23630484A JP 23630484 A JP23630484 A JP 23630484A JP H0645015 B2 JPH0645015 B2 JP H0645015B2
Authority
JP
Japan
Prior art keywords
slurry
particle size
size distribution
concentration
line
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
JP23630484A
Other languages
Japanese (ja)
Other versions
JPS61114756A (en
Inventor
博久 吉田
敏彦 今本
義 玄後
良茂 植松
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP23630484A priority Critical patent/JPH0645015B2/en
Publication of JPS61114756A publication Critical patent/JPS61114756A/en
Publication of JPH0645015B2 publication Critical patent/JPH0645015B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Disintegrating Or Milling (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、高濃度石炭水スラリの粒度分布調整方法に関
する。
TECHNICAL FIELD The present invention relates to a method for adjusting the particle size distribution of highly concentrated coal water slurry.

[従来の技術と発明が解決しようとする問題点] 我が国の現状では、長期に亙って一定の銘柄の石炭を使
用することは難しく、多くの種類の海外炭や国内炭を使
用している。石炭は、銘柄が変った場合は勿論、同じ銘
柄でも採取場所が異なると石炭性状は異なる。このよう
に石炭性状が変った場合にこれを同じ条件で粉砕すると
次のような問題が発生する。
[Problems to be solved by conventional technology and invention] In the present situation in Japan, it is difficult to use a certain brand of coal for a long period of time, and many types of overseas coal and domestic coal are used. . Coal properties will differ not only when the brand changes but also when the same brand has different collection locations. When the coal properties are changed as described above, the following problems occur when the coal is crushed under the same conditions.

(1)粉砕され易い石炭は、粒度分布が細かくなり過ぎ
て粒子比表面積が増大し、多くの添加剤が必要となり不
経済となる。
(1) Coal that is easily pulverized has a too fine particle size distribution and increases the specific surface area of the particles, which requires many additives and is uneconomical.

(2)逆に粉砕され難い石炭は、粒度分布が粗くなり高
濃度石炭水スラリの安定性が悪くなり、著しい場合は高
濃度石炭水スラリ貯蔵タンク内で流動性がなくなりせっ
かく製造した高濃度石炭水スラリを廃棄処分しなければ
ならない場合が生じる。
(2) On the contrary, for coal that is difficult to be crushed, the particle size distribution becomes coarse and the stability of the high-concentration coal water slurry becomes poor. In some cases, the water slurry must be disposed of.

これらの欠点は、従来の方法は製品高濃度石炭水スラリ
の粒度分布を常時監視していなっかたこと、及び粒度分
布を調整する機能を持っていなっかたことに起因すると
考えられる。
It is considered that these drawbacks are due to the fact that the conventional methods did not constantly monitor the particle size distribution of the product high concentration coal water slurry and did not have the function of adjusting the particle size distribution.

[問題点を解決するための手段] 本発明は、上記問題を解決するために、粒度分布監視計
の出力でに応じて駆動する複数台の超微粉砕ミル使用
し、処理する石炭の粒度分布を前記監視計により常に測
定し、所定の粒度分布よりも粗い場合には前記超微粉砕
ミルの運転台数を前記監視計の出力信号に応じて増加
し、該粒度分布が細かい場合は前記超微粉砕ミルの運転
台数を前記監視計の出力信号に応じて減少する高濃度石
炭水スラリの粒度分布調整方法である。
[Means for Solving the Problems] In order to solve the above problems, the present invention uses a plurality of ultra-fine grinding mills driven according to the output of a particle size distribution monitor, and the particle size distribution of coal to be processed. Is constantly measured by the monitor, and when the particle size distribution is coarser than the predetermined one, the number of operating units of the ultrafine grinding mill is increased according to the output signal of the monitor, and when the particle size distribution is fine, the ultrafine particle This is a method for adjusting the particle size distribution of a high-concentration coal water slurry, in which the number of operating mills is reduced according to the output signal of the monitor.

[作用] 本発明に係る高濃度石炭水スラリの粒度分布調整方法
は、石炭の粒度分布監視計と超微粉砕ミルとを連動させ
て石炭の粒度分布に応じて超微粉砕ミルの運転台数を調
整することにより、超微粒スラリの製品高濃度スラリへ
の添加率を調整し、また、超微粒スラリの粒度分布を調
整して、超微粒含有率を調整して、製品高濃度スラリの
粒度分布を常に一定に調節できるのもである。
[Operation] The particle size distribution adjusting method for a high-concentration coal water slurry according to the present invention links the particle size distribution monitor for coal and the ultrafine grinding mill to determine the number of operating ultrafine grinding mills according to the particle size distribution of coal. By adjusting the addition ratio of the ultrafine particle slurry to the product high concentration slurry, and also adjusting the particle size distribution of the ultrafine particle slurry, adjusting the ultrafine particle content rate, the particle size distribution of the product high concentration slurry Is always constant.

而して、本発明方法は、第3図乃至第6図に示すような
高濃度石炭水スラリの製造装置に適用できるものであ
る。第3図に示す高濃度石炭水スラリの製造装置は、貯
留槽1の石炭をタンク3の粗粉砕ミル供給水をライン
2,4を介して粗粉砕ミル6に供給し、低濃度で粉砕処
理した石炭の20〜60重量%の低濃度スラリを作るよ
うになっている。この低濃度スラリをライン7によって
分級器8に送り、粗粒カット低濃度スラリと粗粒含有低
濃度スラリとに分離して、粗粒含有低濃度スラリはライ
ン10によりミル6に戻し再粉砕するようになってい
る。また、粗粒カット低濃度スラリは、ライン9により
脱水器11に送り脱水して生じる脱水水は、ライン12
から脱水水の分配器13を介して再利用ライン14,1
5,16へ送り再利用するようになっている。一方、脱
水ケーキは、ライン25を介してスラリ調整タンク26
に送り、ここで水分濃度を調整するために調整水用タン
ク18からライン22を介して送られる調整水及び添加
剤用タンク20からライン24を介して送られる添加剤
と一緒に攪拌して製品高濃度スラリを作るようになって
いる。この製品高濃度スラリは、ライン27を介して分
配器28により超微粉砕ミル用スラリと貯留用スラリと
に分配し、貯留用スラリは、ライン29を介して製品高
濃度スラリ貯留タンク33に送り貯蔵するようになって
いる。また、超微粉砕ミル用スラリは、ライン30を介
して微粉砕ミル31に送って超微粉砕し、得られた超微
粉砕スラリはライン32を介してタンク26へ添加する
ようになっている。また、このミル31の入口では、水
分濃度を調整するために、調整水タンク17からライン
21を介して調整水、及び添加剤用タンク19からライ
ン23を介して送られる添加剤とを供給するようになっ
ている。このようにして、超微粉砕ミル31で得られる
超微粒スラリを適正量添加することにより、所定の粒度
分布に調整した良好な製品高濃度スラリを得ることがで
きるものである。
Thus, the method of the present invention can be applied to the apparatus for producing a high-concentration coal water slurry as shown in FIGS. 3 to 6. The apparatus for producing high-concentration coal water slurry shown in FIG. 3 supplies the coal in the storage tank 1 to the coarse crushing mill 6 through the lines 2 and 4 to supply the coarse crushing mill feed water from the tank 3 to the crushing process at a low concentration. It is designed to make a low concentration slurry of 20 to 60% by weight of the coal. This low-concentration slurry is sent to a classifier 8 through a line 7 and separated into a coarse-particle-cut low-concentration slurry and a coarse-particle-containing low-concentration slurry, and the coarse-particle-containing low-concentration slurry is returned to a mill 6 by a line 10 for re-grinding. It is like this. The coarse-grain-cut low-concentration slurry is sent to the dehydrator 11 through the line 9 and dehydrated.
From the dehydration water distributor 13 to the reuse line 14, 1
It is sent to 5, 16 for reuse. On the other hand, the dehydrated cake is sent to the slurry adjustment tank 26 via the line 25.
And the product is prepared by stirring with the adjusted water sent from the adjusted water tank 18 through the line 22 and the additive sent from the additive tank 20 through the line 24 to adjust the water concentration. It is designed to make highly concentrated slurries. This product high-concentration slurry is distributed via line 27 to a slurry for ultrafine grinding mill and storage slurry by a distributor 28, and the storage slurry is sent to a product high-concentration slurry storage tank 33 via line 29. It is designed to be stored. Further, the slurry for the ultra-fine crushing mill is sent to the fine crushing mill 31 through the line 30 to be subjected to the ultra-fine crushing, and the obtained ultra-fine crushing slurry is added to the tank 26 through the line 32. . At the inlet of the mill 31, adjusted water is supplied from the adjusted water tank 17 via the line 21 and the additive sent from the additive tank 19 via the line 23 to adjust the water concentration. It is like this. In this way, by adding an appropriate amount of the ultrafine particle slurry obtained by the ultrafine crushing mill 31, it is possible to obtain a good product high-concentration slurry adjusted to a predetermined particle size distribution.

また、第4図に示す高濃度石炭水スラリの製造装置は、
超微粉砕ミル31の入口スラリとして粗粉砕ミル6の出
口スラリをライン7aを介して使用するものである。第
5図に示す高濃度石炭水スラリの製造装置は、分級器8
の粗粒カット側スラリを分配器34を介してライン9a
より、超微粉砕ミル31へ送るものである。第6図に示
す高濃度石炭水スラリの製造装置は、粉砕前の石炭を混
合そう35でスラリ化して、ライン36より超微粉砕ミ
ル31に送るものである。なお、第4図乃至第6図に示
す高濃度石炭水スラリの製造装置は、いずれも第3図に
示す高濃度石炭水スラリの製造装置に比べて超微粉砕ミ
ル31の入口スラリが異なるだけでその他の構成は、第
3図に示す高濃度石炭水スラリの製造装置と同様であ
る。
The high-concentration coal water slurry manufacturing apparatus shown in FIG.
The outlet slurry of the coarse crushing mill 6 is used as the inlet slurry of the ultrafine crushing mill 31 via the line 7a. The high-concentration coal water slurry manufacturing apparatus shown in FIG.
The coarse-grain-cut side slurry is passed through the distributor 34 to the line 9a.
It is then sent to the ultra-fine crushing mill 31. The apparatus for producing high-concentration coal water slurry shown in FIG. 6 converts coal before crushing into slurry in a mixing vessel 35 and sends it to the ultrafine crushing mill 31 through a line 36. It should be noted that all of the high-concentration coal water slurry production apparatuses shown in FIGS. 4 to 6 differ from the high-concentration coal water slurry production apparatus shown in FIG. 3 only in the inlet slurry of the ultrafine grinding mill 31. The other configurations are the same as those of the high-concentration coal water slurry manufacturing apparatus shown in FIG.

[発明の効果] 本発明に係る高濃度石炭水スラリの粒度分布調整方法に
よれば、製品高濃度スラリの輸送ライン中で粒度分布を
迅速に測定し、超微粒スラリの添加量をを調整するよう
にしたので、次の効果を有する。
EFFECTS OF THE INVENTION According to the method for adjusting the particle size distribution of high-concentration coal water slurry according to the present invention, the particle size distribution is quickly measured in the transportation line of the product high-concentration slurry, and the addition amount of the ultrafine particle slurry is adjusted. Since it does so, it has the following effects.

(1)粒度分布の粗い所謂悪質製品高濃度スラリの発生
量を著しく低減できる。
(1) The amount of so-called malicious product high-concentration slurry having a coarse particle size distribution can be significantly reduced.

(2)粒度分布の細かい所謂添加剤の沢山必要な不経済
な製品高濃度スラリの発生量を著しく低減できる。
(2) The amount of uneconomical product high-concentration slurry that requires a large amount of so-called additives with a fine particle size distribution can be significantly reduced.

これらの結果、石炭性状が変化した場合も経済的で一定
の粒度分布を持つ製品高濃度スラリを常に製造できる。
As a result, it is possible to constantly produce an economical product high-concentration slurry having a uniform particle size distribution even when the coal properties change.

[実施例] 第1図は、本発明方法を通用する高濃度石炭水スラリの
製造装置の要部の構成を示す説明図である。製品高濃度
石炭水スラリは、ライン29の途中(ライン27の途中
でも良い)でサンプリングライン41を通じて少量採取
されて、粒度分布測定器40で石炭粒子の粒度分布が測
定されるようになっている。この粒度分布の測定時間
は、例えばレーザ粒度分布測定器を使用した場合3〜5
分である。この実施例では、超微粉砕ミルを3台設置の
場合は通常はミル31aと31bの2台が運転されてお
り、前述の粒度分布測定結果が設定の粒度分布より粗い
場合はライン43を介して流量計41にライン30を通
る流量を増加する様に信号が送られ、分配器28aと2
8bにより所定の流量にまでスラリ流量が増加され、こ
れと同時に開閉弁37cと38cが開き、ミル31cも
運転し始めるようになっている。
[Examples] FIG. 1 is an explanatory view showing a configuration of a main part of a device for producing a high-concentration coal water slurry that applies the method of the present invention. A small amount of the product high-concentration coal water slurry is collected through the sampling line 41 in the middle of the line 29 (may be in the middle of the line 27), and the particle size distribution measuring device 40 measures the particle size distribution of the coal particles. . This particle size distribution measurement time is, for example, 3 to 5 when a laser particle size distribution measuring instrument is used.
Minutes. In this embodiment, when three ultrafine grinding mills are installed, usually two mills 31a and 31b are operated, and when the above-mentioned particle size distribution measurement result is coarser than the set particle size distribution, the line 43 is used. A signal is sent to the flowmeter 41 so as to increase the flow rate through the line 30, and the distributors 28a and 2
The slurry flow rate is increased to a predetermined flow rate by 8b, and at the same time, the opening / closing valves 37c and 38c are opened and the mill 31c is also started to operate.

この結果として、ライン32を介してタンク26へ送ら
れる超微粉スラリ量が増加し、製品高濃度スラリの粗か
った粒度分布は所定の粒度分布に回復する。設定の粒度
分布よりも細い場合には逆の作用となり、流量を減らす
と同時に開閉弁37bと38bが閉じてミル31bも停
止し、ミル31a1台だけの運転となり、製品高濃度ス
ラリの細か過ぎた粒度分布は所定の粒度分布に回復す
る。
As a result, the amount of the ultrafine powder slurry sent to the tank 26 through the line 32 increases, and the coarse particle size distribution of the product high-concentration slurry is restored to the predetermined particle size distribution. When the particle size distribution is smaller than the set particle size distribution, the opposite effect occurs. At the same time as the flow rate is reduced, the on-off valves 37b and 38b are closed and the mill 31b is stopped, and only one mill 31a is operated, and the product high-concentration slurry is too fine. The particle size distribution is restored to a predetermined particle size distribution.

第2図は超微粉砕ミルを直列に並べた他の実施例であ
り、作用は第1図の実施例と全く同じである。
FIG. 2 shows another embodiment in which ultrafine grinding mills are arranged in series, and the operation is exactly the same as that of the embodiment shown in FIG.

なお、超微粒スラリの添加率即ち、超微粉砕ミルへのス
ラリ供給量を加減することにより、製品高濃度スラリの
粒度分布を調整する方法を述べたが、超微粉砕ミルへの
スラリ供給量が一定でも目的を達することができる。即
ち、製品高濃度スラリの粒度分布が粗くなった場合は、
ライン30のスラリ供給量は一定でミル31a,31
b,31c,3台共に運転すれば、それぞれのミル内の
粉砕時間が増し、その結果、ライン32から供給される
超微粒スラリをより超微粒とすることができ、製品高濃
度スラリの粒度分布を所定の粒度分布に回復することが
できる。また製品高濃度スラリの粒度分布が細かい場合
は逆に超微粉砕ミルの運転台数を減らせば良い。
The method of adjusting the particle size distribution of the product high-concentration slurry by adjusting the addition rate of the ultrafine-grained slurry, that is, the amount of slurry supplied to the ultrafine-mill, was described. The goal can be achieved even if the value is constant. That is, when the particle size distribution of the product high-concentration slurry becomes coarse,
The amount of slurry supplied to the line 30 is constant and the mills 31a, 31
If all three b, 31c, and 3 units are operated, the grinding time in each mill will increase, and as a result, the ultrafine particles slurry supplied from the line 32 can be made into ultrafine particles, and the particle size distribution of the product high-concentration slurry will be increased. Can be restored to a predetermined particle size distribution. When the particle size distribution of the product high-concentration slurry is fine, conversely, the number of operating ultrafine grinding mills should be reduced.

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

第1図及び第2図は、本発明方法を適用する高濃度石炭
水スラリの製造装置の要部の構成を示す説明図、第3図
乃至第6図は、本発明方法を適用できる高濃度石炭水ス
ラリの製造装置の概略構成を示す説明図である。 1,1a…石炭の供給貯留層、2,2a…石炭の供給ラ
イン、3…粗粉砕ミル供給水用タンク、4…粗粉砕ミル
供給水の供給ライン、5…補充水供給ライン、6…粗粉
砕ミル、7…低濃度スラリの輸送ライン、8…分級器、
9…粗粒カット低濃度スラリの輸送ライン10…粗粒含
有低濃度スラリの返送循環ライン、11…脱水機、12
…脱水水の排水ライン、13…脱水水の分配器、14,
15,16,16a…脱水水の再利用ライン、17,1
8,18a…調整水用タンク、19,20…添加剤用タ
ンク、21,22,22a…調整水用供給ライン、2
3,24…添加剤供給ライン、25…粗粒カット脱水ケ
ーキの輸送ライン、26…スラリ調整タンク、27…製
品高濃度スラリ排出ライン、28…製品高濃度スラリ分
配器、29…製品高濃度スラリ輸送ライン、30…製品
高濃度スラリの超微粉砕ミルの供給ライン、31…攪拌
型超微粉砕ミル、32…超微粒スラリ輸送ライン、33
…製品高濃度スラリ貯留タンク、7a…低濃度スラリの
超微粉砕ミルへの供給ライン、9a…粗粒カット低濃度
スラリの超微粉砕ミルへの供給ライン、34…粗粒カッ
ト低濃度スラリの分配器、35…粉砕前石炭と水との混
合槽、36…粉砕前石炭と水とのスラリ超微粉砕ミルへ
の供給ライン、28a,28b…分配器、30a,39
b,30c…製品高濃度スラリの超微粉砕ミルへの供給
ライン、31a,31b,31c…超微粉砕ミル、39
…製品高濃度スラリの輸送ポンプ、40…粒度分布測定
器、41…流量計、37a,37b,37c,38a,
38b,38c…開閉弁、42…スラリのサンプリング
ライン、43,44,45,46…信号ライン、47,
47a,47b,47c…超微粒スライ輸送ライン。
FIG. 1 and FIG. 2 are explanatory views showing the configuration of the main part of a high-concentration coal water slurry production apparatus to which the method of the present invention is applied, and FIGS. It is explanatory drawing which shows schematic structure of the manufacturing apparatus of a coal water slurry. 1, 1a ... Coal supply reservoir, 2, 2a ... Coal supply line, 3 ... Coarse crushing mill supply water tank, 4 ... Coarse crushing mill supply water supply line, 5 ... Replenishment water supply line, 6 ... Coarse Grinding mill, 7 ... Low-concentration slurry transportation line, 8 ... Classifier,
9 ... Transport line for coarse-grain-cut low-concentration slurry 10 ... Return circulation line for coarse-grain-containing low-concentration slurry, 11 ... Dehydrator, 12
… Dehydration water drain line, 13… Dehydration water distributor, 14,
15, 16, 16a ... Dehydration water reuse line, 17, 1
8, 18a ... Adjusted water tank, 19, 20 ... Additive tank 21, 21, 22a ... Adjusted water supply line, 2
3, 24 ... Additive supply line, 25 ... Coarse grain cut dehydrated cake transportation line, 26 ... Slurry adjusting tank, 27 ... Product high-concentration slurry discharge line, 28 ... Product high-concentration slurry distributor, 29 ... Product high-concentration slurry Transportation line, 30 ... Supply line of ultra-fine grinding mill for product high-concentration slurry, 31 ... Agitation-type ultra-fine grinding mill, 32 ... Ultra-fine grain slurry transportation line, 33
... Product high-concentration slurry storage tank, 7a ... Supply line of low-concentration slurry to ultrafine grinding mill, 9a ... Supply line of coarse-grain cutting low-concentration slurry to ultrafine-milling machine, 34 ... Coarse-grain cutting low-concentration slurry Distributor, 35 ... Mixing tank of coal and water before crushing, 36 ... Supply line to slurry ultrafine crushing mill of coal and water before crushing, 28a, 28b ... Distributor, 30a, 39
b, 30c ... Supply line of product high-concentration slurry to ultrafine grinding mill, 31a, 31b, 31c ... Ultrafine grinding mill, 39
... Transportation pump for product high-concentration slurry, 40 ... Particle size distribution measuring device, 41 ... Flowmeter, 37a, 37b, 37c, 38a,
38b, 38c ... On-off valve, 42 ... Slurry sampling line, 43, 44, 45, 46 ... Signal line, 47,
47a, 47b, 47c ... Ultra fine grain sly transportation line.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】粒度分布監視計の出力でに応じて駆動する
複数台の超微粉砕ミル使用し、処理する石炭の粒度分布
を前記監視計により常に測定し、所定の粒度分布よりも
粗い場合には前記超微粉砕ミルの運転台数を前記監視計
の出力信号に応じて増加し、該粒度分布が細かい場合は
前記超微粉砕ミルの運転台数を前記監視計の出力信号に
応じて減少することを特徴とする高濃度石炭水スラリの
粒度分布調整方法。
1. When a plurality of ultra-fine grinding mills driven according to the output of a particle size distribution monitor are used and the particle size distribution of coal to be treated is constantly measured by the monitor, and the particle size distribution is coarser than a predetermined particle size distribution. To increase the operating number of the ultra-fine grinding mill according to the output signal of the monitor, and when the particle size distribution is fine, decrease the operating number of the ultra-fine grinding mill according to the output signal of the monitor. A method for adjusting the particle size distribution of a high-concentration coal water slurry, which comprises:
JP23630484A 1984-11-09 1984-11-09 Method for adjusting particle size distribution of high-concentration coal water slurry Expired - Fee Related JPH0645015B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23630484A JPH0645015B2 (en) 1984-11-09 1984-11-09 Method for adjusting particle size distribution of high-concentration coal water slurry

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23630484A JPH0645015B2 (en) 1984-11-09 1984-11-09 Method for adjusting particle size distribution of high-concentration coal water slurry

Publications (2)

Publication Number Publication Date
JPS61114756A JPS61114756A (en) 1986-06-02
JPH0645015B2 true JPH0645015B2 (en) 1994-06-15

Family

ID=16998808

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23630484A Expired - Fee Related JPH0645015B2 (en) 1984-11-09 1984-11-09 Method for adjusting particle size distribution of high-concentration coal water slurry

Country Status (1)

Country Link
JP (1) JPH0645015B2 (en)

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Publication number Priority date Publication date Assignee Title
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Also Published As

Publication number Publication date
JPS61114756A (en) 1986-06-02

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