JPH05412A - Cleaning of polishing mineral sludge for use in cutting stone such as granite and method and device for control of its composition - Google Patents

Cleaning of polishing mineral sludge for use in cutting stone such as granite and method and device for control of its composition

Info

Publication number
JPH05412A
JPH05412A JP3032846A JP3284691A JPH05412A JP H05412 A JPH05412 A JP H05412A JP 3032846 A JP3032846 A JP 3032846A JP 3284691 A JP3284691 A JP 3284691A JP H05412 A JPH05412 A JP H05412A
Authority
JP
Japan
Prior art keywords
metal particles
polishing
cleaning
composition
container
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.)
Pending
Application number
JP3032846A
Other languages
Japanese (ja)
Inventor
Giorgio Dinelli
ジオージオ デイネツリ
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.)
GIORGINI MAGGI Srl
Original Assignee
GIORGINI MAGGI Srl
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 GIORGINI MAGGI Srl filed Critical GIORGINI MAGGI Srl
Publication of JPH05412A publication Critical patent/JPH05412A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B28WORKING CEMENT, CLAY, OR STONE
    • B28DWORKING STONE OR STONE-LIKE MATERIALS
    • B28D1/00Working stone or stone-like materials, e.g. brick, concrete or glass, not provided for elsewhere; Machines, devices, tools therefor
    • B28D1/02Working stone or stone-like materials, e.g. brick, concrete or glass, not provided for elsewhere; Machines, devices, tools therefor by sawing
    • B28D1/025Use, recovery or regeneration of abrasive mediums
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B24GRINDING; POLISHING
    • B24CABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
    • B24C7/00Equipment for feeding abrasive material; Controlling the flowability, constitution, or other physical characteristics of abrasive blasts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B24GRINDING; POLISHING
    • B24CABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
    • B24C9/00Appurtenances of abrasive blasting machines or devices, e.g. working chambers, arrangements for handling used abrasive material

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Mining & Mineral Resources (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
  • Paper (AREA)
  • Processing Of Stones Or Stones Resemblance Materials (AREA)

Abstract

PURPOSE: To maintain a prescribed quantity of metal particles existing in the suspension by controlling supply of new metal particles and washing of abrasive particles included in the abrasive slime based on the data on the density of the metal particles of larger diameter and the specific gravity of the abrasive slime. CONSTITUTION: The weight of a prescribed volume of the abrasive slime is measured by a load cell 14, and the prescribed volume of the abrasive slime is deposited in liquid, then the metal particles of larger diameter than a set point are collected. The weight of the collected metal particles is measured by a load cell 15, and the density of the metal particles of larger diameter included in the abrasive slime and the specific gravity of the abrasive slime are calculated by a processor 23. The metal particles of larger diameter are circulated again, and supply of new metal particles and washing of the abrasive particles in the abrasive mineral mud are controlled based on the data on the density of the metal particles of larger diameter and the specific gravity of the abrasive slime.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明はみかげ石等の石材の切断
に用いる研磨鉱泥(abrasive pulps)の洗浄及び組成のコ
ントロール方法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 cleaning and controlling composition of abrasive pulp used for cutting stone materials such as granite.

【0002】又本発明は上記方法を実施するための装置
に関するものである。
The invention also relates to an apparatus for carrying out the above method.

【0003】[0003]

【従来の技術】みかげ石等の石材ブロックは、単一また
は複数の切削刃を備えた切削機によって切断されている
が、その切削研磨剤としては主として鉄粒子をベースに
した研磨混合物が使用されている。そしてこの研磨混合
物は、水との混合の懸濁液の状態で、切削刃の往復動に
よって石材ブロックに形成される溝を、たえまなく循環
している。切削刃の動きに伴った研磨混合物の研磨作用
により石材ブロックが徐々に切断されていく。循環中の
研磨鉱泥は、次第に被切断物のダストや消耗された鉄粉
の含有量が増大し、ついにはきめこまかくなりすぎて、
効果的に切断作業を続行できなくなる。新規の金属粒子
(metalic grit)の粒径は通常およそ1mmであるが、粒
径が0.3mm程度よりもきめこまかい金属粒子(金属
ダスト)は消耗されたものと判断される。
2. Description of the Related Art Stone blocks such as granite are cut by a cutting machine having a single or plural cutting blades, and an abrasive mixture mainly based on iron particles is used as the cutting abrasive. There is. The polishing mixture, in the state of a suspension mixed with water, constantly circulates in the groove formed in the stone block by the reciprocating movement of the cutting blade. The stone block is gradually cut by the polishing action of the polishing mixture accompanying the movement of the cutting blade. The content of the object to be cut and the consumed iron powder gradually increased in the polishing ore in the circulation, and finally it became too fine-grained,
The cutting work cannot be continued effectively. New metal particles
The particle size of (metalic grit) is usually about 1 mm, but it is considered that the metal particles (metal dust) finer than the particle size of about 0.3 mm are consumed.

【0004】[0004]

【発明が解決しようとする課題】この種の研磨混合物の
使用の際の課題はふたつある。ひとつは、研磨鉱泥中に
おいて切断に有効な粒径の金属粒子の最適濃度を維持す
ることである。もうひとつは、消耗金属ダストと被切断
物から発生するダストを除去し、懸濁液中の金属粒子が
一定量存在するように、研磨鉱泥の比重を一定値に維持
することである。
There are two problems with the use of this type of polishing mixture. One is to maintain an optimum concentration of metal particles having a particle size effective for cutting in the polishing ore. The other is to remove the consumable metal dust and the dust generated from the object to be cut, and maintain the specific gravity of the polishing sludge at a constant value so that the metal particles in the suspension are present in a certain amount.

【0005】金属粒子の消耗量は被切断物の種類によっ
て異なるので、その補充量とその研磨鉱泥の濃度は従来
より経験と実験データにたよってきている。その結果、
研磨鉱泥の組成を最適なものとすることが困難で、金属
粒子の消耗率の増加や切断効率の低下を招いている。
Since the amount of consumption of metal particles varies depending on the type of material to be cut, the amount of replenishment and the concentration of the polishing mud have conventionally been based on experience and experimental data. as a result,
It is difficult to optimize the composition of the polishing sludge, resulting in an increase in the consumption rate of metal particles and a decrease in cutting efficiency.

【0006】最近研磨鉱泥の洗浄は遠心洗浄機によりな
されることが一般となっている。しかし別の方法では、
磁石により金属粒子を分離し、次いで異なる粒径のもの
をメカニカルフィルタによって分別することが行われて
いる。更に別の方法では、圧力洗浄水の水流によって研
磨鉱泥を逆流洗浄することが行われている。研磨鉱泥を
取り扱う際に使用されているこれ等の方法や他のシステ
ムの主な不便さは、あまり信頼が置けない点にある。す
なわち、フィルタの詰まりや、洗浄水圧の変動や、遠心
洗浄機の洗浄選別能力に関しての精度の不十分さが、信
頼性に欠けるものとしている。従って、きめこまかい粒
子(≦0.3mm)をこれより大きな粒子から選別する
ことはかなり難しい。また従来の方法では、みかげ石等
の被切断物の種類によって、金属粒子の供給量を前もっ
て決めておかなければならず、また実際の消耗に対応し
た金属粒子の補充量を正確に決定することは不可能であ
った。
[0006] Recently, the washing of the polishing ore is generally performed by a centrifugal washing machine. But in another way,
It is practiced to separate metal particles with a magnet and then to separate particles having different particle diameters with a mechanical filter. In yet another method, backwashing of the polishing sludge is carried out with a stream of pressure wash water. The major inconvenience of these methods and other systems used in handling abrasive sludge is that they are not very reliable. That is, clogging of the filter, fluctuation of the washing water pressure, and insufficient accuracy of the washing / sorting ability of the centrifugal washing machine are unreliable. Therefore, it is quite difficult to sort out fine particles (≦ 0.3 mm) from particles larger than this. Further, in the conventional method, the amount of metal particles to be supplied must be determined in advance depending on the type of the object to be cut such as granite, and it is impossible to accurately determine the amount of metal particles to be replenished corresponding to actual wear. It was impossible.

【0007】本発明の目的は、既知の類似の方法による
不便さを解消した、みかげ石等の石材の切断に用いる研
磨鉱泥の洗浄及び組成のコントロール方法を提供するこ
とにある。
It is an object of the present invention to provide a method for cleaning and controlling the composition of abrasive ore used for cutting stone materials such as granite, which eliminates the inconvenience of known similar methods.

【0008】特に本発明は、研磨鉱泥の比重の測定、及
び設定値より大きな粒径又は小さな粒径の金属粒子の研
磨鉱泥リットルあたりの重量の測定を可能にし、かつ研
磨鉱泥洗浄の自動的なコントロールと、推測によらず実
際の金属粒子の消耗量にもとづき、どの種類のみかげ石
等の石材に対しても最適な条件となる研磨鉱泥が得られ
るように新規の金属粒子を自動的に補充できるようにす
ることを目的とする。
In particular, the present invention makes it possible to measure the specific gravity of the polishing ore and the weight of metal particles having a particle size larger or smaller than a set value per liter of the polishing ore and for cleaning the polishing ore. Automatic control and automatic estimation of new metal particles based on the actual amount of metal particles consumed, without guessing, to obtain polishing mud that is the optimum condition for stone materials such as granite The purpose is to be able to supplement.

【0009】本発明のもうひとつの目的は、上記方法に
より機能する、みかげ石等の石材の切断に用いる研磨鉱
泥の洗浄及び組成のコントロールを行う装置を提供する
ことにある。
[0009] Another object of the present invention is to provide a device which functions by the above-mentioned method and which cleans and controls the composition of abrasive mud used for cutting stone materials such as granite.

【0010】[0010]

【課題を解決するための手段とその作用】本発明による
研磨鉱泥の洗浄及び組成のコントロール方法において
は、先ず所定体積の研磨鉱泥の重量を計測し、次いで大
きな粒径の固体分離物を収集するために前記研磨鉱泥を
液中に沈澱させる。
Means for Solving the Problem and Its Action In the method for cleaning and controlling the composition of polishing mud according to the present invention, first, the weight of a predetermined volume of polishing mud is measured, and then a solid separated product having a large particle size is obtained. The abrasive sludge is allowed to settle in the liquor for collection.

【0011】前記固体分離物はその重量を計測された
後、研磨鉱泥が循環している回路に配置した収集タンク
へと戻される。研磨鉱泥の重量データ及び体積データ
と、前記大きな粒径の固体分離物の重量データとから、
研磨鉱泥の比重と循環する金属鉱泥中における前記大き
な粒径の金属粒子の実際の濃度が決定される。前記比重
及び濃度を対応する最適の比重及び濃度と比較すること
により、金属粒子の補充量と洗浄回数が決定される。好
ましくは、前記比重、濃度及び補充量の計算はコンピュ
ータによって行われる。そしてこのコンピュータは、洗
浄回数のコントロールを行う上に、種々の運転操作の過
程を正確にコントロールし、ときどき補充される金属粒
子を計量する装置の動作をもコントロールする。
After the weight of the solid separated product is measured, the solid separated product is returned to a collecting tank arranged in a circuit in which the polishing sludge is circulated. From the weight data and volume data of the polishing mud, and the weight data of the solid separated matter of the large particle size,
The specific gravity of the abrasive mud and the actual concentration of the large size metal particles in the circulating metal mud are determined. By comparing the specific gravity and concentration with the corresponding optimum specific gravity and concentration, the amount of metal particles to be replenished and the number of washings are determined. Preferably, the calculation of the specific gravity, concentration and replenishment amount is performed by a computer. In addition to controlling the number of washings, the computer also accurately controls the course of various driving operations and also the operation of the device for weighing the replenished metal particles from time to time.

【0012】本発明方法における特に好ましい実施例に
おいては、小さな粒径の固体分離物も収集され、研磨鉱
泥中の濃度を測定するためにその重量が測定される。そ
して小さな粒径の固体分離物はその全部または一部が排
出処分され、残りが再循環使用される。
In a particularly preferred embodiment of the method of the present invention, small particle size solid isolates are also collected and weighed to determine their concentration in the abrasive sludge. Then, all or part of the small-sized solid separated product is discharged and disposed of, and the rest is recycled.

【0013】特に研磨鉱泥循環システムから抽出された
所定体積の研磨鉱泥の分離沈澱は、鉛直に配した筒状の
水収容容器内で行うと好適である。
In particular, it is preferable that the separation and precipitation of a predetermined volume of the polishing ore extracted from the polishing ore circulation system be carried out in a vertically arranged cylindrical water container.

【0014】大きな粒径の固体分離物の重量の決定、場
合によってはこれに加えるに小さな粒径の固体分離物の
重量の決定は、前記固体分離物の一方又は他方を含む所
定体積の液体の重量を測ることによってなされると、好
都合である。
Determining the weight of the large particle size solids isolate, and optionally the weight of the small particle size solids isolate, is based on the determination of the volume of liquid containing one or the other of the solids isolates. It is expedient if done by weighing.

【0015】この方法の信頼性は、研磨混合物中の異な
る性質をもつ粒子(特に大径粒子と小径粒子)を分離す
る原理が、重量と大小の粒子間にみられる流動抵抗の差
とにのみ基いているという事実によって保証される。何
故なら、金属粒子の沈澱の速さは、粒子の直径に概ね比
例し、鉄の1/3.54の比重をもつみかげ石のダスト
は、沈澱の際にはるかに小さな直径の鉄粒子と同じ速さ
で沈澱するという現象が利用できるからである。従って
相当大きな粒径のみかげ石のダスト(例えば直径1m
m)さえも効果的に金属粒子から分離することができ
る。
The reliability of this method is that the principle of separating particles having different properties (especially large particles and small particles) in the polishing mixture is only due to the difference in weight and flow resistance between large and small particles. Guaranteed by the fact that it is based. Because the speed of precipitation of metal particles is roughly proportional to the diameter of the particles, the granite dust, which has a specific gravity of 1 / 3.54 of iron, has the same speed as iron particles of much smaller diameter during precipitation. This is because the phenomenon of precipitation can be used. Therefore, granite dust with a fairly large particle size (for example, a diameter of 1 m
Even m) can be effectively separated from the metal particles.

【0016】本発明の装置は、設定値より大きな粒径の
金属粒子を設定値より小さな粒径の金属粒子及びみかげ
石のダストから分離するための筒状の沈澱器を備えてい
る。
The apparatus of the present invention comprises a tubular precipitator for separating metal particles having a particle size larger than a set value from metal particles having a particle size smaller than the set value and granite dust.

【0017】この筒状の沈澱器は、洗浄液を満たすのに
適切なように形成され、また入口部分と排出口部分をも
ち、前者は循環中の研磨鉱泥を所定体積収集するための
第一容器と、後者は前記筒状の沈澱器の底に溜まった沈
澱物を収集するための第二容器と、それぞれ開閉可能な
通路を介して接続している。本発明はまた第一容器及び
第二容器に夫々付設され、夫々から排出される所定体積
の研磨鉱泥又は沈澱物の重量を夫々測る重量測定装置を
備えている。更に本発明は重量データから研磨鉱泥の比
重とその研磨鉱泥中の大きな粒径の固体分離物の濃度を
算出し、かつ操作手順のシーケンス制御、新規の金属粒
の補充及び洗浄回数の制御を行うコンピュータ制御手段
を備えている。
This cylindrical precipitator is appropriately formed to fill the cleaning liquid and has an inlet portion and an outlet portion. The former is the first for collecting a predetermined volume of circulating polishing sludge. The container and the latter are connected to the second container for collecting the sediment accumulated at the bottom of the cylindrical precipitator through the respective openable and closable passages. The present invention also includes a weight measuring device attached to each of the first container and the second container for measuring the weight of a predetermined volume of the polishing mud or sediment discharged from each container. Furthermore, the present invention calculates the specific gravity of the polishing sludge from the weight data and the concentration of the solid particles having a large particle size in the polishing sludge, and the sequence control of the operating procedure, the replenishment of new metal particles and the control of the number of washing It is provided with a computer control means for performing.

【0018】本発明のみかげ石等の石材の切断に用いる
研磨鉱泥の洗浄及び組成のコントロール方法とその装置
の特徴と利点は、添付図面を参照しながらなされる、模
範的ではあるが限定的ではない実施例についての以下の
説明で明らかにされる。
The features and advantages of the method for cleaning and controlling the composition of the polishing ore used for the cutting of stone materials such as granite according to the present invention, and the advantages thereof will be described with reference to the accompanying drawings, but are not limitative. It will be made clear in the following description of the non-exclusive examples.

【0019】[0019]

【実施例】図1において、鉛直フレーム1上には漏斗形
の第一容器2が設置され、その底部は自動弁3を介して
鉛直状態に配した筒状の沈澱器4の入口部分と通じてお
り、この沈澱器4の排出部分は自動弁5を介して中継タ
ンク6とつながっている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS In FIG. 1, a funnel-shaped first container 2 is installed on a vertical frame 1, and its bottom is connected via an automatic valve 3 to an inlet portion of a cylindrical precipitator 4 arranged vertically. The discharge portion of the precipitator 4 is connected to the relay tank 6 via the automatic valve 5.

【0020】中継タンク6は自動弁7を介して、漏斗形
の第二容器8と通じている。この第二容器8の底部は自
動弁9を介して、循環回路内の研磨鉱泥を収集する貯溜
部に連通する導管10と、排出物処理装置または泥処理
装置につながっている導管11とのいずれかに選択的に
接続するようになっている。第一容器2、第二容器8及
び中継タンク6は筒状の沈澱器4の鉛直軸線上に配置さ
れている。
The relay tank 6 is connected to a funnel-shaped second container 8 via an automatic valve 7. The bottom of this second container 8 is connected to a reservoir 10 for collecting the polishing ore in the circulation circuit via an automatic valve 9 and a conduit 11 connected to an emission treatment device or a sludge treatment device. It is designed to selectively connect to either one. The first container 2, the second container 8 and the relay tank 6 are arranged on the vertical axis of the cylindrical precipitator 4.

【0021】第一容器2は、研磨鉱泥の循環回路から延
びて来ていて、自動弁13によって通路が開閉される収
集パイプ12からの供給を受ける。第一容器2と第二容
器8はそれぞれロードセル14、15で重量測定される
ように配設されており、ロードセル14は第一容器2中
に収集された所定体積の研磨鉱泥の重量を測定するため
に用いられ、ロードセル15は第二容器8中に収集され
た沈澱物の重量を測定するために用いられる。
The first container 2 extends from the circulation circuit of the polishing ore and receives a supply from a collecting pipe 12 whose passage is opened and closed by an automatic valve 13. The first container 2 and the second container 8 are arranged so as to be weighed by the load cells 14 and 15, respectively, and the load cell 14 measures the weight of a predetermined volume of the abrasive sludge collected in the first container 2. The load cell 15 is used to weigh the precipitate collected in the second container 8.

【0022】本装置は洗浄液(特に水)の供給ライン1
6とつながっている。すなわち、第一容器2、沈澱器
4、中継タンク6、及び第二容器8がそれぞれ自動弁1
7、18、19、20を介して洗浄水供給ライン16に
つながっている。沈澱器4の底からある高さのところに
自動弁22を備えた導管21が接続されており、この導
管21によって粒径の小さな固体粒子を含む液体を排出
物処理装置や泥処理装置に放流できるようにしている。
This apparatus is provided with a cleaning liquid (particularly water) supply line 1
Connected to 6. That is, the first container 2, the precipitator 4, the relay tank 6, and the second container 8 are respectively provided with the automatic valve 1
The washing water supply line 16 is connected via 7, 18, 19, and 20. A conduit 21 having an automatic valve 22 is connected at a height from the bottom of the precipitator 4, and the conduit 21 discharges a liquid containing solid particles having a small particle size to an exhaust treatment device or a mud treatment device. I am able to do it.

【0023】コンピュータのプロセッサ23は本発明装
置の操作手順を制御しており、命令信号を各種自動弁に
送ったり、ロードセル14、15からの重量データを受
け取ったりしている。自動弁13の開放により、収集パ
イプ12から第一容器2内へ研磨鉱泥が流入するが、そ
の流入時の液面の高さはレベルコントローラ24によっ
て制御されている。第一容器2内で液面が設定高さに達
したとき、その液面高さの値が読まれて、前記プロセッ
サ23に送られ、自動弁13は閉じる。そしてロードセ
ル14によって、第一容器2の内容物重量が測定され、
その測定値が前記プロセッサ23に送られ、ここで収集
された研磨鉱泥の比重が計算される。一方、自動弁18
の開放によって、沈澱器4内に水が流入し、この流入は
所定の高さに達っしたとレベルコントローラ25が判断
するまで続けられる。その間、自動弁5は開き、自動弁
7は閉じている。つづいて自動弁3の開放が命令され、
第一容器2内の研磨鉱泥を沈澱器4内の水の中へと落下
させ、そこで大きな粒径の金属粒子が小さな粒径の粒子
から分離され、中継タンク6内に収集される。自動弁3
の開放後、所定時間がたったとき、自動弁5が閉じら
れ、細かくて軽い粒子が中継タンク6内に流入するのを
防ぐ。
The processor 23 of the computer controls the operating procedure of the device of the present invention and sends command signals to various automatic valves and receives weight data from the load cells 14 and 15. When the automatic valve 13 is opened, the polishing mud flows from the collecting pipe 12 into the first container 2, and the height of the liquid surface at the time of the inflow is controlled by the level controller 24. When the liquid level reaches the set height in the first container 2, the value of the liquid level is read and sent to the processor 23, and the automatic valve 13 is closed. Then, the weight of the contents of the first container 2 is measured by the load cell 14,
The measured value is sent to the processor 23, and the specific gravity of the abrasive sludge collected here is calculated. On the other hand, the automatic valve 18
Is opened to allow water to flow into the precipitator 4, and this flow is continued until the level controller 25 determines that the predetermined height has been reached. Meanwhile, the automatic valve 5 is open and the automatic valve 7 is closed. Then, the opening of the automatic valve 3 was ordered,
The abrasive sludge in the first vessel 2 is dropped into the water in the settler 4, where the large particle size metal particles are separated from the small particle size particles and collected in the relay tank 6. Automatic valve 3
After a predetermined time has passed after the opening of the automatic valve 5, the automatic valve 5 is closed to prevent fine and light particles from flowing into the relay tank 6.

【0024】その後自動弁7が開放され、中継タンク6
内の金属粒子を第二容器8内に落下させる。そのおり第
二容器8内には自動弁20の開放により水が供給され、
この水の供給は液面が所定の高さに達っしたとレベルコ
ントローラ26が判断するまで続けられる。第二容器8
の内容物の重量はロードセル15によって計測され、そ
の値はプロセッサ23に送られ、研磨鉱泥リットルあた
りの大きな粒径の金属粒子の重量、すなわちその濃度
(g/1)が算出される。計測が終わると、自動弁9が
開放され、計量された金属粒子は導管10を通って循環
回路内の研磨鉱泥貯溜部に戻される。
After that, the automatic valve 7 is opened and the relay tank 6 is opened.
The metal particles therein are dropped into the second container 8. Water is supplied to the second container 8 by opening the automatic valve 20,
This water supply is continued until the level controller 26 determines that the liquid level has reached a predetermined height. Second container 8
The weight of the contents is measured by the load cell 15, the value is sent to the processor 23, and the weight of the metal particles having a large particle size per liter of the polishing ore, that is, its concentration (g / 1) is calculated. When the measurement is completed, the automatic valve 9 is opened, and the weighed metal particles are returned to the polishing ore storage section in the circulation circuit through the conduit 10.

【0025】中継タンク6と第二容器8の洗浄は自動弁
19、20を一時的に開放することにより行われる。そ
の間弁22もまた開放され、沈澱器4内の懸濁液が導管
21を介して放出され、同時に粒径の小さな金属粒子が
沈澱器4の底に集められる。
The cleaning of the relay tank 6 and the second container 8 is performed by temporarily opening the automatic valves 19 and 20. Meanwhile, the valve 22 is also opened, and the suspension in the precipitator 4 is discharged through the conduit 21, while at the same time, the small-sized metal particles are collected at the bottom of the precipitator 4.

【0026】そこで新たに自動弁5を開放し、粒径の小
さな金属粒子を中継タンク6に流入させ、次いで自動弁
7の開放により第二容器8に送る。ここで、粒径の小さ
な金属粒子は、粒径の大きな金属粒子の場合と同様の方
法によって、ロードセル15によってその重量を計測さ
れ、その測定値はプロセッサ23に送られる。そしてこ
こで研磨鉱泥中の小さな粒径の金属粒子の濃度が算出さ
れる。
Therefore, the automatic valve 5 is newly opened, metal particles having a small particle size are caused to flow into the relay tank 6, and then the automatic valve 7 is opened to send the particles to the second container 8. Here, the weight of the small-sized metal particles is measured by the load cell 15 by the same method as that of the large-sized metal particles, and the measured value is sent to the processor 23. Then, here, the concentration of small-sized metal particles in the polishing ore is calculated.

【0027】この運転サイクルの最後において、自動弁
17、18、19、20が一時的に開放され、各容器や
各導管をすばやく洗浄する。そして洗浄水は導管11を
通って排出物処理装置へ送られる。
At the end of this operating cycle, the automatic valves 17, 18, 19, 20 are temporarily opened to quickly clean each container and each conduit. The wash water is then sent to the waste treatment device through the conduit 11.

【0028】このようにして測定された大きな粒径及び
小さな粒径の金属粒子の実際の濃度は、それぞえ予め記
憶されている最適値と比較され、この比較の結果に基い
て、プロセッサ23は循環中の研磨鉱泥へ補充する新規
の金属粒子の補充量を計量装置D(図示省略)に教え、
その補充を行わせる。また、小さな粒径の粒子は、導管
10を介して循環回路内の研磨鉱泥貯溜部に戻される
か、または導管11を介して循環回路から除去される。
The actual concentrations of the large and small metal particles thus measured are compared with prestored optimum values, respectively, and the processor 23 is based on the result of this comparison. Tells the metering device D (not shown) the amount of new metal particles to be added to the circulating polishing sludge,
Let them replenish it. Also, particles of small size are returned to the abrasive ore deposits in the circulation circuit via conduit 10 or removed from the circulation circuit via conduit 11.

【0029】図2は、本発明装置のひとつの簡単な変形
例を示したものである。この変形例は粒径の小さな金属
粒子の濃度を直接測ったり、それを再循環させることが
できないものである。この変形例においては、大きな粒
径の金属粒子は沈澱器4の底に集まり、排出導管21を
介して粒径の小さな金属粒子やみかげ石のダストを含む
懸濁液が沈澱器4の外へ排出された後、自動弁5の開放
により第二容器8内に直接流入させられ、すでに述べた
方法でその重量が測定される。大きな粒径の金属粒子の
好ましい分離は、研磨鉱泥の沈澱器4への流入タイミン
グと自動弁22の開放のタイミングの調整によって得ら
れる。
FIG. 2 shows one simple modification of the device of the present invention. In this modification, the concentration of small metal particles cannot be directly measured or recycled. In this variant, the large-sized metal particles collect at the bottom of the precipitator 4, and the suspension containing the small-sized metal particles and the granite dust is discharged to the outside of the precipitator 4 via the discharge conduit 21. After that, the automatic valve 5 is opened to flow directly into the second container 8 and its weight is measured by the method described above. The preferable separation of the large-sized metal particles is obtained by adjusting the timing of the flow of the polishing sludge into the precipitator 4 and the timing of opening the automatic valve 22.

【0030】本発明方法に用いた実施例では、筒状の沈
澱器4として、直径0.3m、高さ2.5mのものを採
用した。そして研磨鉱泥をその循環回路から40リット
ル分取り入れ、第一容器2内の重量をロードセル14を
用いて計測した結果、研磨鉱泥の比重は1,650g/
lであった。第二容器8内の重量を計測した結果、取り
入れた研磨鉱泥中に、粒径0.3mm以上とみなされる
大粒径の金属粒子は2,400g存在し、粒径0.3m
m以下とみなされる小粒径の金属粒子は4,000g存
在することが明らかとなった。従って循環研磨鉱泥中の
大きな方の粒径の金属粒子の濃度は60g/lであり、
これはみかげ石の切断において許容できる数値であっ
た。なお小さな方の粒径の金属粒子の濃度は100g/
lであった。大小の粒径の分離物を夫々分析した結果、
小さな方の粒径の粒子中に10%の大きな方の粒径の粒
子が混在し、大きな方の粒径の粒子中に10%の小さな
粒径の粒子が混在していることが明らかとなった。大き
な方の粒径の金属粒子中からみかげ石のダストが完全に
洗浄除去されていることを考えると、上記の90%の分
離率は好ましいものと考えられる。この分離率は、制御
プロセスの各種パラメータを最適なものにすることによ
り、更に改善され得る。
In the embodiment used in the method of the present invention, a cylindrical precipitator 4 having a diameter of 0.3 m and a height of 2.5 m was adopted. Then, 40 liters of the polishing mud was taken in from the circulation circuit, and the weight in the first container 2 was measured by using the load cell 14. As a result, the specific gravity of the polishing mud was 1,650 g /
It was l. As a result of measuring the weight in the second container 8, there were 2,400 g of large-sized metal particles considered to have a particle size of 0.3 mm or more in the introduced polishing ore, and the particle size was 0.3 m.
It was revealed that there were 4,000 g of small-sized metal particles considered to be m or less. Therefore, the concentration of the metal particles of the larger particle size in the circulating polishing ore is 60 g / l,
This was an acceptable number for granite cutting. The concentration of metal particles with a smaller particle size is 100 g /
It was l. As a result of analyzing each of the large and small particle size separations,
It became clear that 10% of the larger particle size particles were mixed in the smaller particle size particles, and 10% of the smaller particle size particles were mixed in the larger particle size particles. It was Considering that the granite dust is completely washed and removed from the metal particles having the larger particle diameter, the above-mentioned separation rate of 90% is considered to be preferable. This separation rate can be further improved by optimizing various parameters of the control process.

【0031】上述の本発明の実施例においては、いずれ
も沈澱器4から放出される大きな粒径の金属粒子を含む
所定体積の液体の重量測定を行うようになっているが、
前記大きな粒径の金属粒子の重量測定は、水を機械的に
濾過し除去した後、直接行うことができることも明らか
である。また明らかなことに、第一容器2と第二容器8
の液面のコントロールは、測定器を使用することに代え
て、余剰流入液をオーバーフローさせることによっても
行うことができる。このオーバフロー法は前記容器2、
8についての重量測定の下で行われる。すなわち重量が
増えないようだと、それは余剰流入液がオーバフローし
始めたことを意味するので、液の供給を停止し、同時に
前記容器2、8についての最終重量を知ることができ
る。大小の粒径の固形分離物の重量も、ロードセルを使
用することに代えて、第二容器8内に堆積した粒子の高
さを読むことや、金属粒子の量に比例した磁場の強さの
変化を測定することによる間接的な方法によって測定す
ることができる。
In each of the above-described embodiments of the present invention, the weight of a predetermined volume of liquid containing metal particles having a large particle size, which is discharged from the precipitator 4, is weighed.
It is also clear that the weight measurement of the large particle size metal particles can be carried out directly after mechanically filtering out the water. It is also clear that the first container 2 and the second container 8
The liquid level can be controlled by overflowing the excess inflow liquid instead of using the measuring device. This overflow method uses the container 2,
8 under weight measurement. That is, if the weight does not seem to increase, it means that the excess inflow liquid has begun to overflow, so that the supply of the liquid can be stopped and at the same time the final weight of the containers 2, 8 can be known. Instead of using a load cell, reading the height of the particles deposited in the second container 8 and measuring the strength of the magnetic field proportional to the amount of metal particles are also used for the weights of the large and small particle size solids. It can be measured by an indirect method by measuring the change.

【0032】本発明のみかげ石等の石材の切断に用いる
研磨鉱泥の洗浄及び組成のコントロール方法とその装置
において、本発明自体の範囲を逸脱することがなけれ
ば、いかなる変形や修正も可能である。
In the method and apparatus for controlling the composition and cleaning of the polishing mud used for cutting stone materials such as granite of the present invention, any modification or modification can be made without departing from the scope of the present invention. .

【0033】[0033]

【発明の効果】本発明によれば、研磨鉱泥の比重の測
定、及び設定値より大きな粒径の金属粒子(場合によっ
てはこれに加えて設定値より小さな粒径の金属粒子)の
研磨鉱泥中の濃度の測定を可能にし、研磨鉱泥洗浄の自
動的なコントロールと、推測によらず実際の金属粒子の
消耗量にもとづき、どの種類のみかげ石等の石材に対し
ても最適な条件となる研磨鉱泥が得られるように新規の
金属粒子を自動的に補充できる、みかげ石等の石材の切
断に用いる研磨鉱泥の洗浄及び組成のコントロール方法
とその装置を提供することができる。
According to the present invention, the specific gravity of the polishing ore mud is measured, and the polishing ore of metal particles having a particle size larger than the set value (in addition to this, metal particles having a particle size smaller than the set value in some cases) is used. It enables the measurement of the concentration in mud, the automatic control of the polishing ore mud washing, and the actual consumption of metal particles without guessing, and the optimum conditions for stone materials such as granite. It is possible to provide a method and a device for controlling the cleaning and composition of the polishing mud used for cutting stone materials such as granite, which can automatically replenish new metal particles so as to obtain the following polishing mud.

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

【図1】本発明の実施例に用いられる装置の正面図であ
る。
FIG. 1 is a front view of an apparatus used in an embodiment of the present invention.

【図2】本発明の他の実施例に用いられる装置の正面図
である。
FIG. 2 is a front view of an apparatus used in another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

2 第一容器 4 沈澱器 6 中継タンク 8 第二容器 14、15 ロードセル 16 洗浄液供給ライン 21 導管 24、26 レベルコントローラ 2 First container 4 Precipitator 6 relay tank 8 second container 14,15 load cell 16 Cleaning liquid supply line 21 conduit 24, 26 level controller

Claims (12)

【特許請求の範囲】[Claims] 【請求項1】 設定値より大きな粒径の金属粒子と小さ
な粒径の金属粒子を石材のダストと共に含む研磨鉱泥を
洗浄しかつその組成をコントロールする方法において、
所定体積の研磨鉱泥の重量を測定する工程と、前記所定
体積の研磨鉱泥を液体中に沈澱させて、設定値より大き
な粒径の金属粒子を収集する工程と、収集された前記金
属粒子の重量を測定する工程と、前記研磨鉱泥の重量デ
ータと前記大きな粒径の金属粒子の重量データから前記
研磨鉱泥中の大きな粒径の金属粒子の濃度と研磨鉱泥の
比重を計算する工程と、大きな粒径の金属粒子を再循環
させる工程と、大きな粒径の金属粒子の濃度データと研
磨鉱泥の比重データにもとづき、新規の金属粒子の補充
と研磨鉱泥中の研磨粒子の洗浄を制御する工程とを備え
たことを特徴とするみかげ石等の石材の切断に用いる研
磨鉱泥の洗浄及び組成のコントロール方法。
1. A method for cleaning and controlling the composition of an abrasive sludge containing metal particles having a particle size larger than a set value and metal particles having a particle size smaller than a set value together with stone dust.
A step of measuring the weight of a predetermined volume of the polishing sludge, a step of precipitating the predetermined volume of the polishing slurry in a liquid, and collecting metal particles having a particle size larger than a set value; and the collected metal particles. And a step of measuring the weight of the polishing ore and the weight data of the polishing ore and the weight data of the metal particles of the large size, to calculate the concentration of the metal particles of the large size in the polishing and the specific gravity of the polishing ore. Based on the process, the step of recycling large-sized metal particles, the concentration data of large-sized metal particles and the specific gravity data of the polishing mud, the supplement of new metal particles and the polishing particles in the polishing mud A method of controlling the composition and cleaning of polishing mud used for cutting stone materials such as granite, which comprises a step of controlling cleaning.
【請求項2】 設定値より小さな粒径の金属粒子が分離
収集され、その重量が計測され、これによって循環して
いる研磨鉱泥内の小さな粒径の金属粒子の濃度を推し量
り、小さな粒径の金属粒子をその内の0から100%の
間のいずれかの量を再循環させる工程を付加的に備えた
ことを特徴とする請求項1記載のみかげ石等の石材の切
断に用いる研磨鉱泥の洗浄及び組成のコントロール方
法。
2. Metal particles having a particle size smaller than a set value are separated and collected, and the weight thereof is measured, whereby the concentration of the metal particles having a small particle size in the circulating polishing sludge is estimated to obtain a small particle. The polishing ore used for cutting stone materials such as granite as claimed in claim 1, further comprising a step of recycling any amount of the metal particles having a diameter of 0 to 100%. Method for cleaning mud and controlling composition.
【請求項3】 所定体積の研磨鉱泥が水収容の筒状容器
に供給されることを特徴とする請求項1、又は2記載の
みかげ石等の石材の切断に用いる研磨鉱泥の洗浄及び組
成のコントロール方法。
3. The cleaning and composition of the polishing mud used for cutting stone materials such as granite as claimed in claim 1 or 2, wherein a predetermined volume of the polishing mud is supplied to a cylindrical container containing water. Control method.
【請求項4】 大きな粒径の金属粒子及び収集がなされ
る場合における小さな粒径の金属粒子は水と共に収集さ
れ、水を含んだ所定体積のものの重量が計測されること
を特徴とする請求項1、2又は3記載のみかげ石等の石
材の切断に用いる研磨鉱泥の洗浄及び組成のコントロー
ル方法。
4. The metal particles having a large particle diameter and the metal particles having a small particle diameter when the metal particles are collected are collected together with water, and a predetermined volume containing water is weighed. 1. A method for cleaning abrasive mineral mud used for cutting stone materials such as granite or the like according to 1, 2, or 3, and controlling the composition.
【請求項5】 大きな粒径の金属粒子及び収集がなされ
る場合における小さな粒径の金属粒子は、懸濁液中の水
が濾過排出された後に、その重量が計測されることを特
徴とする請求項1、2又は3記載のみかげ石等の石材の
切断に用いる研磨鉱泥の洗浄及び組成のコントロール方
法。
5. The large particle size metal particles and the small particle size metal particles when collected are characterized in that the water in the suspension is weighed after being filtered out. A method for cleaning and controlling the composition of a polishing mud used for cutting stone materials such as granite, according to claim 1, 2 or 3.
【請求項6】 設定値より大きな粒径の金属粒子と小さ
な金属粒子を石材のダストと共に含む研磨鉱泥を洗浄し
かつその組成をコントロールする装置において、大きな
粒径の金属粒子を小さな粒径の金属粒子及び石材のダス
トから分離するための筒状の沈澱器4を有し、この沈澱
器4は洗浄液が収容できると共に、その入口部分が循環
回路中の研磨鉱泥を所定体積取入れるための第一容器2
と接続通路の開閉が可能なように接続され、その排出部
分が沈澱器4の底に溜まった沈澱物を受入れて収集する
ための第二容器8と接続通路の開閉が可能なように接続
されるように構成され、かつ第一容器2に付設されて前
記所定体積の研磨鉱泥の重量を測定する重量測定手段1
4を備えると共に、第二容器8に付設されて第二容器8
に収集された沈澱物の重量を測定する重量測定手段15
を備え、更に前記重量データから前記研磨鉱泥の比重
と、研磨鉱泥中の大きな粒径の金属粒子の濃度を計算す
ると共に、一連の操作手続と新規の金属粒子の補充と、
洗浄回数とを制御するデータ処理手段23を備えたこと
を特徴とするみかげ石等の石材の切断に用いる研磨鉱泥
の洗浄及び組成のコントロール装置。
6. An apparatus for cleaning and controlling the composition of a polishing ore containing metal particles having a particle size larger than a set value and metal particles having a particle size smaller than a set value together with stone dust, and a metal particle having a large particle size having a small particle size It has a cylindrical precipitator 4 for separating it from metal particles and stone dust, and this precipitator 4 can contain a cleaning liquid, and its inlet portion is for taking in a predetermined volume of polishing mud in the circulation circuit. First container 2
And the connection passage so that the connection passage can be opened and closed, and the discharge portion is connected so that the second passage 8 for receiving and collecting the sediment accumulated at the bottom of the precipitator 4 and the connection passage can be opened and closed. And a weight measuring unit 1 attached to the first container 2 for measuring the weight of the above-mentioned predetermined volume of the polishing sludge.
4 and is attached to the second container 8 to provide the second container 8
Weight measuring means 15 for measuring the weight of the precipitate collected in
Further comprising calculating the specific gravity of the polishing ore from the weight data, and the concentration of large-sized metal particles in the polishing ore, a series of operating procedures and supplementation of new metal particles,
A control device for cleaning and composition of abrasive ore used for cutting stone materials such as granite, characterized by comprising a data processing means 23 for controlling the number of times of cleaning.
【請求項7】 沈澱器4はその底部に一時的に上部から
分断される部分6を有することを特徴とする請求項6記
載のみかげ石等の石材の切断に用いる研磨鉱泥の洗浄及
び組成のコントロール装置。
7. The precipitator 4 has a portion 6 at the bottom thereof which is temporarily cut off from the top, and the cleaning and composition of the polishing ore mud used for cutting stone materials such as granite. Control device.
【請求項8】 第二容器8はふたつの異なる交互に選択
可能な排出導管10、11を有し、一方は循環回路中の
研磨鉱泥収集部に接続し、他方は排出物処理装置または
泥処理装置に接続していることを特徴とする請求項6、
又は7記載のみかげ石等の石材の切断に用いる研磨鉱泥
の洗浄及び組成のコントロール装置。
8. The second container 8 has two different and alternately selectable discharge conduits 10, 11, one connected to the abrasive sludge collector in the circulation circuit and the other to an exhaust treatment device or mud. 7. A processing device connected to a processing device.
Or a device for cleaning and composition of abrasive ore used for cutting stone materials such as granite as described in 7.
【請求項9】 沈澱器4の底からある高さのところに開
閉可能な排出導管21が設けられていることを特徴とす
る請求項6、7、又は8記載のみかげ石等の石材の切断
に用いる研磨鉱泥の洗浄及び組成のコントロール装置。
9. The method for cutting stone material such as granite according to claim 6, 7 or 8, wherein a discharge conduit 21 that can be opened and closed is provided at a height from the bottom of the settler 4. Equipment for cleaning and composition of polishing ore used.
【請求項10】 第一容器2、第二容器8、沈澱器4及
び沈澱器の底部分断部分6は夫々洗浄液供給ネットワー
ク16に開閉可能な通路を介して接続されていることを
特徴とする請求項6、7、8、又は9記載のみかげ石等
の石材の切断に用いる研磨鉱泥の洗浄及び組成のコント
ロール装置。
10. The first container 2, the second container 8, the precipitator 4 and the bottom partial disconnection part 6 of the precipitator are respectively connected to a cleaning liquid supply network 16 via an openable / closable passage. Item 6. A device for cleaning abrasive composition and controlling composition, which is used for cutting stone materials such as granite, according to 6, 7, 8 or 9.
【請求項11】 筒状の沈澱器4は鉛直軸線上に設けら
れており、第一容器2、第二容器8は前記鉛直軸線上に
配設されていることを特徴とする請求項6、7、8、9
又は10記載のみかげ石等の石材の切断に用いる研磨鉱
泥の洗浄及び組成のコントロール装置。
11. The cylindrical precipitator 4 is provided on a vertical axis, and the first container 2 and the second container 8 are provided on the vertical axis. 7, 8, 9
Or a control device for cleaning and composition of abrasive ore used for cutting stone materials such as granite.
【請求項12】 第一容器2及び第二容器8はレベルコ
ントローラ24、26によって液面の制御がなされてい
ることを特徴とする請求項6、7、8、9、10又は1
1記載のみかげ石等の石材の切断に用いる研磨鉱泥の洗
浄及び組成のコントロール装置。
12. The liquid level of the first container 2 and the second container 8 is controlled by level controllers 24, 26, and the liquid level is controlled in any one of claims 6, 7, 8, 9, 10 or 1.
1. A control device for cleaning and composition of abrasive ore used for cutting stone materials such as granite.
JP3032846A 1990-02-28 1991-02-27 Cleaning of polishing mineral sludge for use in cutting stone such as granite and method and device for control of its composition Pending JPH05412A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IT9326A IT1238882B (en) 1990-02-28 1990-02-28 PROCEDURE FOR THE WASHING AND CHECKING OF THE COMPOSITION OF ABRASIVE TURBIDES USED IN THE CUTTING OF GRANITES AND SIMILAR STONES AND RELATED EQUIPMENT.
IT9326A/90 1990-02-28

Publications (1)

Publication Number Publication Date
JPH05412A true JPH05412A (en) 1993-01-08

Family

ID=11128487

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3032846A Pending JPH05412A (en) 1990-02-28 1991-02-27 Cleaning of polishing mineral sludge for use in cutting stone such as granite and method and device for control of its composition

Country Status (7)

Country Link
EP (1) EP0445085B1 (en)
JP (1) JPH05412A (en)
BR (1) BR9100797A (en)
DE (1) DE69118571T2 (en)
ES (1) ES2088478T3 (en)
IT (1) IT1238882B (en)
PT (1) PT96906B (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2140353B1 (en) * 1998-07-23 2000-08-16 Gomez Luis Castro METHOD OF SAWING GRANITES.
ES2199064B1 (en) * 2002-07-01 2005-06-01 Luis Castro Gomez SAWING STONES WITHOUT ACUTE NOISE.
ITVI20030113A1 (en) * 2003-06-10 2004-12-11 Marmi Zenatelli Sas PROCEDURE FOR THE CORRECTION TREATMENT OF THE
ES2246168B1 (en) * 2004-07-27 2007-03-16 Luis Castro Gomez IMPROVED GRANITE SAW.
IT1394117B1 (en) * 2009-05-14 2012-05-25 Valentinotti CONTINUOUS CONTROLLED PALLETING / SANDBLASTING AND RELATIVE METHOD
IT1397126B1 (en) * 2009-10-13 2013-01-04 Fil Tec S R L SYSTEM AND METHOD FOR FILTERING THE WASTE WATER DERIVING FROM THE CUTTING OF BLOCKS AND POLISHING OF MARBLES, GRANITES AND SIMILARS.
WO2012126883A1 (en) * 2011-03-18 2012-09-27 Meyer Burger Ag Cutting fluid cleaning arrangement for a wire saw, wire saw arrangements and use of the wire saw arrangement
DE102016223190B3 (en) * 2016-10-04 2017-10-19 Eisenwerk Würth GmbH Method and device for determining an operating state of a blasting machine

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2994314A (en) * 1958-08-22 1961-08-01 Ty Sa Man Machine Company Stone cutting apparatus
FR1263257A (en) * 1960-04-21 1961-06-09 Saint Gobain Glass polishing improvement
IT1191597B (en) * 1986-03-14 1988-03-23 Luca Toncelli DEVICE FOR THE AUTOMATIC CONTROL OF THE DENSITY AND VISCOSITY OF THE ABRASIVE MIXTURE AND OF THE QUANTITY OF METAL GRAIN USED IN THE SEGMENT OF GRANITES OR HARD STONES
DE8910186U1 (en) * 1989-08-12 1989-12-07 Scheible Versorgungsanlagen

Also Published As

Publication number Publication date
PT96906B (en) 1998-09-30
DE69118571T2 (en) 1996-11-28
IT9009326A1 (en) 1991-08-28
ES2088478T3 (en) 1996-08-16
EP0445085A2 (en) 1991-09-04
EP0445085B1 (en) 1996-04-10
EP0445085A3 (en) 1992-10-07
IT9009326A0 (en) 1990-02-28
IT1238882B (en) 1993-09-04
BR9100797A (en) 1991-11-05
DE69118571D1 (en) 1996-05-15
PT96906A (en) 1993-01-29

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