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JPS623054A - Manufacture and equipment for finished products from gravel and sand - Google Patents

Manufacture and equipment for finished products from gravel and sand

Info

Publication number
JPS623054A
JPS623054A JP14503486A JP14503486A JPS623054A JP S623054 A JPS623054 A JP S623054A JP 14503486 A JP14503486 A JP 14503486A JP 14503486 A JP14503486 A JP 14503486A JP S623054 A JPS623054 A JP S623054A
Authority
JP
Japan
Prior art keywords
evaluator
sample
finished product
components
target value
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
JP14503486A
Other languages
Japanese (ja)
Inventor
クラウス・ブレ
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.)
AUFUBERAITSUNGUSUMASHINEN MBH
Aufuberaitsungusumashinen Mbh & Co Kg g
Original Assignee
AUFUBERAITSUNGUSUMASHINEN MBH
Aufuberaitsungusumashinen Mbh & Co Kg g
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 AUFUBERAITSUNGUSUMASHINEN MBH, Aufuberaitsungusumashinen Mbh & Co Kg g filed Critical AUFUBERAITSUNGUSUMASHINEN MBH
Publication of JPS623054A publication Critical patent/JPS623054A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B28WORKING CEMENT, CLAY, OR STONE
    • B28CPREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
    • B28C7/00Controlling the operation of apparatus for producing mixtures of clay or cement with other substances; Supplying or proportioning the ingredients for mixing clay or cement with other substances; Discharging the mixture
    • B28C7/0007Pretreatment of the ingredients, e.g. by heating, sorting, grading, drying, disintegrating; Preventing generation of dust
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B13/00Control arrangements specially adapted for wet-separating apparatus or for dressing plant, using physical effects
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B9/00General arrangement of separating plant, e.g. flow sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B11/00Arrangement of accessories in apparatus for separating solids from solids using gas currents
    • B07B11/04Control arrangements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B9/00Combinations of apparatus for screening or sifting or for separating solids from solids using gas currents; General arrangement of plant, e.g. flow sheets
    • GPHYSICS
    • G05CONTROLLING; REGULATING
    • G05DSYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
    • G05D11/00Control of flow ratio
    • G05D11/02Controlling ratio of two or more flows of fluid or fluent material
    • G05D11/13Controlling ratio of two or more flows of fluid or fluent material characterised by the use of electric means
    • G05D11/135Controlling ratio of two or more flows of fluid or fluent material characterised by the use of electric means by sensing at least one property of the mixture

Landscapes

  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Engineering & Computer Science (AREA)
  • Automation & Control Theory (AREA)
  • Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Combined Means For Separation Of Solids (AREA)
  • Sampling And Sample Adjustment (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 この発明は、原料カー品を選別したのちに、試料1!を
取出し、その分析ののちに、目標値と比較する、原料製
品から砂利と砂の仕上ル製品を製造する方法、およびこ
れを遂行する装置に関する。
DETAILED DESCRIPTION OF THE INVENTION In this invention, after sorting raw car products, sample 1! The present invention relates to a method for producing finished products of gravel and sand from raw products, and an apparatus for carrying out the process, in which the results are analyzed and compared with target values.

例えば砂利および砂の↓う′l!!l原料製品が、種類
ムまたはBの砂のドイツ工業規格(D工N−Vorsc
hrift )に一致する粒子帯域構成で天然に見出さ
れることは、極めてまnである。この種類の砂f:a造
するため、例えば縦紐して送入される固体材料から不純
物を洗い落す装ff1(ドイツ連邦共和国特許# 、2
 s 4tコ9ダθ号明糾i)、砂ウオーム、上昇流分
級器、サイクロンなどのような、棹種、の砂選別器か存
する。この選別器は、一定の原料が供給される際に、砂
の品質に関して、手動で調節される。こjは、仕上シ製
品の試料を取出して、次いでこt′Lを、実験所で評価
することによって、達成される。この咋に、評価には、
長時間が必要であり、この時間のおいだ、装置は作動を
続け、場合によっては、不完全な製品が生じる。
For example, gravel and sand ↓U'l! ! l The raw material product meets the German Industrial Standard for type M or B sand (D-N-Vorsc).
It is extremely rare to be found in nature with particle zone configurations matching hrift). This type of sand f:a is used for washing off impurities from the solid material fed, for example, in vertical strings (Patent No. of the Federal Republic of Germany, Patent No. 2).
There are various types of sand sorters, such as sand worms, upflow classifiers, cyclones, etc. This screener is manually adjusted with respect to the quality of the sand when fed with a certain amount of raw material. This is accomplished by taking a sample of the finished product and then evaluating t'L in the laboratory. In this case, in the evaluation,
A long period of time is required, during which time the equipment continues to operate, possibly resulting in an incomplete product.

次いで、実験の結果に基づいて、選別器は手で新らたに
調節されるが、その場合に、調整は、作業者の経験に従
って達成される。さらに、実際上見出されるように、原
料の粒子帯域構成は常に揺動し、該尚するドイツ工業規
格に従う品質AおよびBの砂は、決して、常に経済的に
製造することはできない。しかしながら、例えは架橋の
ような多くの利用分野に対して、定まった砂の品質を一
定に保持することは、極めて重要である。さらrC1公
知の方法では、原料の収1−か望ましくないという欠点
が存する。
Based on the results of the experiment, the sorter is then manually adjusted anew, the adjustment being achieved according to the operator's experience. Furthermore, as is found in practice, the particle zone configuration of the raw material is constantly fluctuating and sands of quality A and B according to the German Industrial Standards in question can never always be produced economically. However, for many applications, such as crosslinking, it is extremely important to keep a certain sand quality constant. Furthermore, the known method has the disadvantage that the yield of raw materials is undesirable.

この発明の目的は、仕上シ製品の粒子帯域の変化を常圧
監視し、半白1・的Kまたは完全に自動的に、変化に対
処するようにした、方法および装置を提供することにあ
る。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a method and apparatus for atmospheric pressure monitoring of changes in the particle zone of a finished product and for reacting to changes either half-white or completely automatically. .

この発明によれば、この目的の達成のため、試料の取出
しのために、仕上シ製品から、部分量が抜出され、これ
が、多くの成分に分離され、こ扛が、目標値と現在値の
比較ののちに、仕上シ製品または回収成分に混入される
According to the invention, in order to achieve this objective, a partial quantity is extracted from the finished product for sample removal, which is separated into a number of components, and which is divided into a target value and a current value. After comparison, it is mixed into the finished product or recovered ingredients.

原料製品の選別器を有する、上述し7た方法を遂行する
ための、この発明による装置では、仕上シ製品の吐出部
に、試料取出し器が配置され、これに、&径の粒子成分
のための分離器が後続し、その際に、粒子成分のために
、測定器が配備され、この測定器が、データを評価器に
伝送し、この評価器が、粒子成分の混入を調節し、かつ
選別器または原料製品送入部のための調節部を作動し、
若しくはそのいずれかを達成する。
In the device according to the invention for carrying out the method as described above, which has a sorter for the raw product, a sample taker is arranged at the outlet of the finished product, in which a sample extractor is arranged for particle components of size &. A separator follows, with a measuring device being provided for the particulate component, which transmits the data to an evaluator, which adjusts the contamination of the particulate component, and actuating the regulator for the sorter or raw product inlet;
or achieve any of the above.

望ましい実施例によれば、個個の粒子成分が、分配切換
器を介して、吐出部および回収部に連結される。
According to a preferred embodiment, the individual particle components are connected via a distribution switch to the discharge section and the collection section.

ざらに、第1の粒子成分が吐出部に直接送入できること
が、望ましい。
In general, it is desirable that the first particle component can be delivered directly to the discharge section.

別の提案によれば、評価器が、一定のまたは調節可能の
目標値付与器を備える。
According to another proposal, the evaluator comprises a constant or adjustable setpoint value provider.

測定器における現在値と調節が一致する豊で、評価器が
、制御パルスを、ラインを介して調節部に送ることが、
ざらに望ましい。
When the current value in the measuring device and the adjustment match, the evaluator sends a control pulse to the regulator via the line.
Roughly desirable.

分配切換器を、評価器によって制御できるようにするこ
とが、さらに提案される。
It is further proposed that the distribution switch can be controlled by the evaluator.

評価器におけるプログラムまたは貯蔵部によって、仕上
ル製・品の吐出部が任意にしばしば繰返しできることは
、望ましい。
It is desirable that the output of the finished product can be repeated as often as desired, depending on the program or storage in the evaluator.

別の提案によれば、試料取出し器は、ばら材料のゲート
からなる。
According to another proposal, the sample extractor consists of a gate of bulk material.

この発明の別の提案によれば、分離器として、ふるい分
け機、上昇流分級器、風ふるい機などが設けられる。
According to another proposal of the invention, a sieve, an upflow classifier, a wind sieve, etc. are provided as the separator.

別の提案によれば、測定器がわん曲!全備え、その端部
が、入口および出口で動くことかできるように取付けら
れ、わん曲t・が、屈曲点で、秤量セルに導かれる。
According to another suggestion, the measuring device is crooked! The entire structure is movably mounted at its ends at the inlet and at the outlet, and the curvature t is guided into the weighing cell at the point of inflection.

この発明(Cよる方法および装置によれは、時間の空費
なしVC即座に、定常的にまたは一定の時間単位内で、
原料)品の粒子帯域の変位が、半自動的にまたは完全に
自動的に対処できる。制御および調節ユニットは、原料
製品の選別器に接続される。
According to the method and apparatus according to the present invention (C), VC can be performed immediately, regularly or within a certain time unit without wasting time.
The displacement of the particle zone of the raw material product can be dealt with semi-automatically or fully automatically. The control and regulation unit is connected to the raw product sorter.

以下、図面を参照しながら、この発明の実施例について
説明する。
Embodiments of the present invention will be described below with reference to the drawings.

この発明による方法および装置の構成を説明するため、
最初に、第7図を参照する。ここで、原料製品は、コン
ベヤベルト、ノコ・−トまたはポンプ送フ通路lダによ
って、選別器lに送入される。
To explain the structure of the method and apparatus according to the invention,
First, reference is made to FIG. Here, the raw product is fed to the sorter 1 by means of conveyor belts, saws or pump feed passages.

この選別器の実施例としては、例えは、洗浄ベッドを備
えた装置のような柚揖の可能な例が存する。
As an embodiment of this sorter, there are several possible examples, such as a device with a washing bed.

洗浄ベッドの場合には、その深さを変えることによって
、細かい砂の吐出量が制御できる8選別器/として、上
昇流分級器、砂ウオーム、サイクロンなどが利用できる
In the case of a washing bed, an upflow classifier, sand worm, cyclone, etc. can be used as the 8-sifter, which can control the discharge amount of fine sand by changing its depth.

仕上シ#品は、吐出部りにル出される。有害物および過
剰の細かい砂は、回収通路13を通って、低地に送られ
、または回収装機7に送られ、ここで、細かい砂が回収
できる。
The finished product is discharged to the discharge section. Harmful substances and excess fine sand are sent through the collection channel 13 to low-lying areas or to a collection machine 7, where the fine sand can be collected.

吐出部デでは、試料取出し器−によって、試料の取出し
が達成される。試料取出し器コは、例えは第9図に示さ
れるような、ばら材料のゲートによって構成できる。取
出された試料は、試料数出し器=から分離器3に達し、
ここで、試料は、少くとも一つの粒子成分に分別される
。ここで、11の粒子成分IOは、直接に仕上シ製品吐
出部デに送入でき、または別に吐出できる。第一粒子成
分//>よび第3粒予成分l−は、図示の実施例では、
分離器3から、微細粒子成分測定器ダおよび弘′にそれ
ぞれ導かれ、ここで、測定が達成される1粒子成分//
およびノコの吐出部は、過剰の微細製品の吐出部/3!
L、直接に輸送でき、または別に輸送できる1粒子成分
//およびノコの制御のため、各通路16および16′
の中に、分配切換器6および6′が配診され、これによ
っても、粒子成分け、吐出通路9における仕上シ製品に
混入できる。
At the discharge part D, the sample is removed by a sample remover. The sample extractor can be constituted by a gate of bulk material, for example as shown in FIG. The sample taken out reaches the separator 3 from the sample counter =,
Here, the sample is separated into at least one particle component. Here, the eleven particle components IO can be fed directly to the finishing product outlet D or can be discharged separately. The first grain component //> and the third grain precomponent l- are, in the illustrated embodiment,
From the separator 3, one particle component is led to the fine particle component analyzers Da and Hiro', respectively, where the measurement is accomplished.
And the discharge part of the saw is the discharge part of excess fine products / 3!
L, one particle component that can be transported directly or separately // and for the control of the saw, each channel 16 and 16'
Dispensing switches 6 and 6' are provided in the discharge channel 9, which also allow particulate components to be mixed into the finished product in the discharge channel 9.

微細粒子測定器ケ、ダ′は、制御ライン17゜17’f
介して、評価器、y rc接続され、これはざらに、ラ
イン15を介して、調節部&に接続され、またラインi
g、ig’を介して、分配切換器6゜6′に接続される
。この際に、ライン/7./7’を通って到着する信号
は、調節可能の目標値と、定常的に比較される。目標値
から偏っている場合には、評価器5が、偏シに従って、
制御パルスを調節部gに与える。このパルスは、出発す
るパルスが確定された目標値と一致するまで、放出され
る。
The fine particle measuring device is connected to the control line 17°17'f.
via the evaluator, y rc is connected, which is roughly connected to the regulator & via line 15, and also to the line i
It is connected to the distribution switch 6°6' via g and ig'. At this time, line /7. The signal arriving through /7' is constantly compared with an adjustable target value. If it is biased from the target value, the evaluator 5, according to the bias,
A control pulse is applied to the regulator g. This pulse is emitted until the starting pulse corresponds to the established target value.

この隙に、分配切換器6.6′の同様な制御も達成され
る。
During this time, a similar control of the distribution switch 6.6' is also achieved.

、評価器5は、微細粒子成分測定器弘、ダ′において@
度を一定に保持するための、組成の指示を備えてもよく
、伽えなくてもよい、さらに、S柚の所望の仕上少製品
を製造するために、選択可能の貯蔵品が配備できる。ラ
イン15によって調節部Sに与えられる制御パルスによ
って、原料製品の選別器/が調節され、調節された微細
粒子成分の目標値が、微細粒子成分測定器t、q′にお
ける成分//、/−の微細粒子成分と一致したときに、
所望の仕上υ製品が生成される。これによって、成分/
/、/−の揺動が続く際に、 !liJ整も続行される
。調節部gによって、原料製品送入部/4tに作用を加
えることもでき、その際に、送入シュート、シャワー装
置、上昇水流および送入量が調節される0分配切換器6
に対しては、スライダ、絞シフラップ、分配シュート、
ピンチコックなどが利用される。
, the evaluator 5 is the fine particle component measuring instrument Hiro, Da'.
In addition, selectable stocks can be provided to produce a desired finished product of S yuzu, which may or may not have instructions of composition to maintain a constant strength. By means of the control pulses given to the regulating section S by the line 15, the raw product sorter / is adjusted, and the adjusted target value of the fine particle component is determined by the component //, /- in the fine particle component measuring devices t, q'. When it matches the fine particle component of
A desired finished υ product is produced. This allows the ingredients/
When /, /- oscillation continues, ! LiJ adjustment will also continue. The adjustment part g can also act on the raw product inlet part/4t, in which case the inlet chute, the shower device, the rising water flow and the inlet amount are adjusted by the 0-distribution switch 6.
For sliders, aperture flaps, distribution chutes,
A pinch cock etc. is used.

12図および第3図には、分離器3と測定器4、4′の
実施例が図示される。分離器3は、ふるい分け機からな
ることができ、これにおいて、取出される試料が、種種
の成分io、li、iコに分別される。そのため、ふる
い分け機は、ふるい板l?を有し、こねは、種也の粒子
成分を得るため、長手軸線および横軸線で分割される。
12 and 3 illustrate embodiments of the separator 3 and the measuring devices 4, 4'. The separator 3 can consist of a sieving machine, in which the sample taken is separated into different components io, li, i. Therefore, the sieving machine has a sieve plate l? The dough is divided along the longitudinal and transverse axes to obtain the grain components of the seeds.

分離のため、特に第3図に示されるように、隔壁二〇が
設けられる。ふるい分け桜はまた、多くのふるい板を有
するふるいによって、形成することもできる。漏斗、2
/の底の近くの細かい砂と水の混合物は、わん曲管=2
の中に達する。これの端部は、入口23および出ロコダ
で動くことができるように取付けられる。わん曲管ココ
は、屈曲点コSで、秤量セルコロに保持される。これは
、作用する負荷を、容積流における重量の変化に基づい
て、対応の電気信号に変換し、これが、評価器Sに付与
される。容積は、入口=3における交換可能の入れ子部
分全備えたノズルによって、または出ロコ弘におけるス
ライダによって、正確に訓読できる。このような秤量セ
ルの代シに、超洞定セル、放射線密度測定器などが設け
られてもよい。第3図に示されるように、多くの成分l
/、/−に対して、多くのわん曲管2=が、並列配θさ
れる。
For separation, a partition 20 is provided, as shown in particular in FIG. Screening cherry can also be formed by a sieve having many sieve plates. funnel, 2
The mixture of fine sand and water near the bottom of the curved pipe = 2
reach inside. The ends of this are movably mounted at the inlet 23 and outlet locoders. The curved tube is held at the bending point S by the weighing cell roller. This converts the applied load, based on the change in weight in the volumetric flow, into a corresponding electrical signal, which is applied to the estimator S. The volume can be accurately read by a nozzle with replaceable telescopic parts at the inlet = 3 or by a slider at the exit loco. Instead of such a weighing cell, an ultrasonic cell, a radiation density measuring device, etc. may be provided. As shown in Figure 3, many components l
Many curved pipes 2= are arranged in parallel θ with respect to / and /−.

第弘図には、試料取出し器−の実施例が示され、これは
、はら材料のゲートとして構成される。これにおいて、
ハウジングコクの中で、隔呈車輪コgが駆動される。こ
のような取出し器によって、常に一定の量が、仕上夛製
品の流れりから取出しできる。
In Figure 1 an embodiment of the sample extractor is shown, which is constructed as a gate of bulk material. In this,
A partition wheel g is driven inside the housing. With such a take-off device, a constant quantity can always be taken out of the finished product stream.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、この発明による装置のブロック線図である。 ツコ図は、分離器および測定器の実施例の正面図である
。第3図は、肴!2図の装置の91断面図ある。第を図
は、試料取出し器の実施例の断面図である。 図面において、lは選別器、コは試料取出し器、Jは分
離器、ダとダ′は測定器、Sは評価器、6と6′は分配
切換器、りは回収装置、gは調節部を示す。 手続補正書(方式) 昭和61年 7月23日
FIG. 1 is a block diagram of a device according to the invention. The diagram is a front view of an embodiment of the separator and meter. Figure 3 is a side dish! 91 is a sectional view of the device of FIG. 2. Figure 5 is a cross-sectional view of an embodiment of the sample extractor. In the drawing, l is a sorter, C is a sample taker, J is a separator, Da and Da' are measuring devices, S is an evaluator, 6 and 6' are distribution switching devices, ri is a collection device, and g is a control unit. shows. Procedural amendment (method) July 23, 1986

Claims (1)

【特許請求の範囲】 1、原料製品を選別したのちに、試料を取出し、その分
析ののちに、目標値と比較する、原料製品から砂利と砂
の仕上り製品を製造する方法において、試料の取出しの
ために、仕上り製品から、部分量を抜出し、これを多く
の成分に分離し、これを、目標値と現在値の比較ののち
に、仕上り製品または回収成分に混入することを特徴と
する方法。 2、原料製品を選別したのちに、試料を取出し、その分
析ののちに、目標値と比較する、原料製品から砂利と砂
の仕上り製品を製造する装置において、原料製品の選別
群(1)を有し、仕上り製品の吐出部(9)に、試料取
出し器(2)を配置し、これに、種種の粒子成分(10
、11、12)のための分離器(3)を後続させ、その
際に、粒子成分(10、11、12)のために、測定器
(4、4′)を配備し、この測定器から、データを評価
器(5)に伝送し、この評価器によつて、粒子成分(1
0、11、12)の、仕上り製品または回収成分への混
入を調節し、かつ選別器(1)または原料製品の送入部
(14)のための調節部(8)を作動し、若しくはその
いずれかを達成することを特徴とする装置。 3、個個の粒子成分(11、12)が、分配切換器(6
、6′)を介して、吐出部(9)および回収部(13)
に送入できる、特許請求の範囲第2項に記載の装置。 4、第1の粒子成分(10)が、吐出部(9)に直接送
入できる、特許請求の範囲第2項または第3項に記載の
装置。 5、評価器(5)に、一定のまたは調節可能の目標値付
与器が設けられる、特許請求の範囲第2項から第4項の
いずれか1項に記載の装置。 6、測定器(4、4′)における現在値と目標値の一致
が達成されるまで、評価器(5)が、ライン(15)を
介して、制御パルスを調節部(8)に送る、特許請求の
範囲第2項から第5項のいずれか1項に記載の装置。 7、分配切換器(6、6′)が、評価器(5)によつて
制御できる、特許請求の範囲第2項から第6項のいずれ
か1項に記載の装置。 8、評価器(5)におけるプログラムまたは貯蔵部によ
つて、仕上り製品の吐出部(9)が、任意にしばしば繰
返しできる、特許請求の範囲第2項から第7項のいずれ
か1項に記載の装置。 9、試料取出し器(2)がばら材料のゲートからなる、
特許請求の範囲第2項から第8項のいずれか1項に記載
の装置。 10、分離器(3)が、ふるい分け機、上昇流分級器、
風ふるい機などからなる、特許請求の範囲第2項から第
9項のいずれか1項に記載の装置。 11、測定器(4、4′)がわん曲管(22)を備え、
その端部が、入口(23)および出口(24)で可動に
取付けられ、屈曲点(25)で、わん曲管が秤量セル(
26)に接続される、特許請求の範囲第2項から第10
項のいずれか1項に記載の装置。
[Scope of Claims] 1. In a method for producing finished products of gravel and sand from raw materials, the method includes taking out a sample after sorting raw materials, analyzing the sample, and comparing it with a target value. A method characterized by extracting a partial amount from the finished product, separating it into many components, and mixing these into the finished product or recovered components after comparing the target value and the current value. . 2. After sorting the raw products, take out the sample, analyze it, and compare it with the target value. A sample extractor (2) is arranged in the finished product discharge section (9), and various particle components (10
, 11, 12), a measuring device (4, 4') is provided for the particle components (10, 11, 12), from which , the data is transmitted to the evaluator (5), and the evaluator calculates the particle component (1
0, 11, 12) into the finished product or the recovered components and actuates the regulating part (8) for the separator (1) or the feed part (14) for the raw product; A device characterized in that it accomplishes any of the following: 3. The individual particle components (11, 12) are transferred to the distribution switch (6).
, 6'), the discharge section (9) and the collection section (13).
2. A device according to claim 2, which can be delivered to. 4. Device according to claim 2 or 3, in which the first particle component (10) can be fed directly into the outlet (9). 5. Device according to one of claims 2 to 4, characterized in that the evaluator (5) is provided with a constant or adjustable setpoint value applicator. 6. the evaluator (5) sends control pulses to the regulator (8) via the line (15) until an agreement between the current value and the target value in the measuring device (4, 4') is achieved; An apparatus according to any one of claims 2 to 5. 7. Device according to any one of claims 2 to 6, in which the distribution switch (6, 6') can be controlled by an evaluator (5). 8. According to any one of claims 2 to 7, by means of a program or a storage in the evaluator (5), the discharge of the finished product (9) can be repeated as often as desired. equipment. 9. The sample extractor (2) consists of a gate of bulk material;
An apparatus according to any one of claims 2 to 8. 10, the separator (3) is a sieving machine, an upflow classifier,
Apparatus according to any one of claims 2 to 9, comprising a wind sieve or the like. 11. The measuring device (4, 4') is equipped with a curved tube (22),
Its ends are movably mounted at the inlet (23) and outlet (24), and at the bending point (25) the curved tube is attached to the weighing cell (
Claims 2 to 10 connected to 26)
Apparatus according to any one of paragraphs.
JP14503486A 1985-06-22 1986-06-23 Manufacture and equipment for finished products from gravel and sand Pending JPS623054A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19853522478 DE3522478A1 (en) 1985-06-22 1985-06-22 Process and apparatus for producing a gravel/sand finished product
DE3522478.9 1985-06-22

Publications (1)

Publication Number Publication Date
JPS623054A true JPS623054A (en) 1987-01-09

Family

ID=6273986

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14503486A Pending JPS623054A (en) 1985-06-22 1986-06-23 Manufacture and equipment for finished products from gravel and sand

Country Status (3)

Country Link
JP (1) JPS623054A (en)
AU (1) AU5886086A (en)
DE (1) DE3522478A1 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL1005413C1 (en) * 1997-03-03 1998-09-07 Promin B V Method for composing granular mixtures with predetermined specifications, starting from granular starting material.
US7893378B2 (en) 2004-08-10 2011-02-22 Mss, Inc. Materials recovery facility process optimization via unit operation feedback
DE102005004273A1 (en) * 2005-01-28 2006-08-03 Anatec As Measuring device for determining the dusting behavior of disperse systems
DE102016108104A1 (en) * 2016-05-02 2017-11-02 Thomas Wöhrl Method for determining the relative proportion of fractions of bulk material in a mixture, consisting of fractions of different fractions, in order to achieve a given total mixing ratio with regard to the particle sizes of the bulk material
CN118092363A (en) * 2024-04-22 2024-05-28 宁德时代新能源科技股份有限公司 Control method and device of production system, computer equipment and product

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ZA82525B (en) * 1981-02-09 1982-12-29 Wilkinson Rubber Linatex Ltd Blending of fluid materials
US4483357A (en) * 1983-02-22 1984-11-20 Globe-Union Inc. Method for two stage in-line acid mixing

Also Published As

Publication number Publication date
AU5886086A (en) 1986-12-24
DE3522478A1 (en) 1987-01-02

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