JPH02107361A - Crushing degree control unit of grinding machine - Google Patents

Crushing degree control unit of grinding machine

Info

Publication number
JPH02107361A
JPH02107361A JP26221988A JP26221988A JPH02107361A JP H02107361 A JPH02107361 A JP H02107361A JP 26221988 A JP26221988 A JP 26221988A JP 26221988 A JP26221988 A JP 26221988A JP H02107361 A JPH02107361 A JP H02107361A
Authority
JP
Japan
Prior art keywords
degree
grinding
measuring device
crusher
particles
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.)
Granted
Application number
JP26221988A
Other languages
Japanese (ja)
Other versions
JP2710039B2 (en
Inventor
Toshihiko Satake
佐竹 利彦
Yukio Hosaka
幸男 保坂
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.)
Satake Engineering Co Ltd
Original Assignee
Satake Engineering Co 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 Satake Engineering Co Ltd filed Critical Satake Engineering Co Ltd
Priority to JP26221988A priority Critical patent/JP2710039B2/en
Publication of JPH02107361A publication Critical patent/JPH02107361A/en
Application granted granted Critical
Publication of JP2710039B2 publication Critical patent/JP2710039B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Crushing And Grinding (AREA)
  • Disintegrating Or Milling (AREA)

Abstract

PURPOSE:To always stably keep a predetermined grinding degree regardless of the difference in the various characteristics of a material to be ground by relationally providing a measuring device for judging a grinding degree to a grinding machine and controlling the rotational speed of a grinding roll on the basis of the output signal of the measuring device. CONSTITUTION:A pair of rolls 62, 63 between which the difference in the number of rotations is provided are installed in a freely rotatable manner in opposed relationship and a transmission 69 is provided on the side rotationally driving the rolls 62, 63 in connection with each other. For example, a measuring device 86 for judging a grinding degree by measuring the projection areas of ground pebbles is relationally provided to a grinding machine and the output signal of the measuring device 86 is transmitted to the transmission 69 through a control unit 89. As a result, a predetermined grinding degree can be always stably kept regardless of the difference in various characteristics of a material to be ground.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、小麦等の製粉に使用される粉砕機、特にロー
ル粉砕機に関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a crusher used for milling wheat, etc., and particularly to a roll crusher.

〔従来技術〕[Prior art]

小麦から小麦粉をつくる製粉作業において、小麦等の砕
料(砕くべき原料)を、ロール粉砕機に供給し粉砕する
が、−度に粉状にまで粉砕せず、ロール粉砕機を数台連
座式に並べ、さらにこれらを各種の選別装置と搬送装置
により機能的に組み合わせて、小麦粉等の砕成物(所要
の粒度まで砕いた製品)を得ている。
In the milling process of making flour from wheat, the flour (raw material to be crushed) such as wheat is fed to a roll crusher and crushed, but rather than being crushed into powder all at once, several roll crushers are used in series. These are then functionally combined using various sorting devices and conveying devices to obtain crushed products (products crushed to the required particle size) such as wheat flour.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

このように、複数の粉砕機1選別装置を効率よく運転し
て高品質の砕成物を量産するために、ロール粉砕機での
粉砕度の調節や、篩選別機等の選別装置における篩の構
成等に特段の注意を払う必要があった。ロール粉砕機に
よる粉砕では、特に一対のロールの間隙が粉砕度を左右
する大きな要因であり、その調節には多大の時間を要し
ていた。また供給される砕料の粒径・含水率等の諸特性
の差が粉砕度の差となって表れ、運転過程においても、
粉砕度が変化して前記ロールの間隙の点検・調節を必要
としていた。
In this way, in order to efficiently operate multiple crusher 1 sorting devices and mass-produce high-quality crushed products, it is necessary to adjust the degree of crushing in the roll crusher and to adjust the sieves in the sorting devices such as the sieve sorter. It was necessary to pay particular attention to the composition, etc. In pulverization using a roll pulverizer, the gap between a pair of rolls is a major factor that affects the degree of pulverization, and adjusting it requires a lot of time. In addition, differences in various characteristics such as particle size and moisture content of the supplied granules appear as differences in the degree of pulverization, and during the operation process,
The degree of grinding changed, requiring inspection and adjustment of the gap between the rolls.

本発明は、従来の問題点を解決するために、粉砕度を判
別し、粉砕度を左右する粉砕機ノロールの回転速度を自
動的に調節して、常に高品質の砕成物を儲産できる粉砕
機の粉砕調節装置を提供することを目的とする。
In order to solve the conventional problems, the present invention determines the degree of crushing and automatically adjusts the rotation speed of the crusher nozzle, which affects the degree of crushing, so that high-quality crushed products can always be produced profitably. The purpose of the present invention is to provide a grinding adjustment device for a grinder.

C問題点を解決するための手段) 上記の目的を達成するために本発明は、回転数差を設け
た一対の[J−ルを対向回転自在に設け、前記一対のロ
ールを連動回転駆動する駆動側に変速装置を設けた粉砕
機において、粉砕度を判別する測定器を粉砕機に関連的
に付設しで、該器の出力信号を制御装置を介して前記変
速装置に連絡し、前記測定器は粒大選別機と重量計とか
らなるものと粉砕粒の投影面積測定で判別するものなど
により問題解決の手段とした。
Means for Solving Problem C) In order to achieve the above object, the present invention provides a pair of rolls with a difference in rotation speed so as to be rotatable opposite each other, and the pair of rolls are driven to rotate in conjunction with each other. In a pulverizer equipped with a transmission on the drive side, a measuring device for determining the degree of pulverization is attached to the pulverizer, and an output signal from the device is communicated to the transmission via a control device to perform the measurement. The problem was solved by using a device consisting of a particle size sorter and a weighing scale, and a device that discriminated by measuring the projected area of crushed particles.

〔作 用〕[For production]

測定器によって粉砕機による粉砕度を判別し、その出力
信号を制御装置へ送り、粉砕用ロールの変速装置を制御
して【コールの回転速度を調節し、常に所望の粉砕度が
青られるようにすることができる。
The degree of crushing by the crusher is determined by a measuring device, and the output signal is sent to the control device, which controls the speed change device of the crushing roll to adjust the rotational speed of the coal so that the desired degree of crushing is always achieved. can do.

〔実施例〕〔Example〕

本発明の実施例を図面第1図ないし第5図に基づいて説
明する。
Embodiments of the present invention will be described based on FIGS. 1 to 5 of the drawings.

第1図は小麦等の製粉の行程を示すもので、粉砕度を判
別する測定器が、粉砕した粒子を粒大選別J゛る粒大選
別機と重量計とからなる場合を示している。ここでは4
台の粉砕機(製粉機)1.2,3.4と3台の篩選別機
5,6.7をの主要構成機としている。
FIG. 1 shows the process of milling wheat, etc., and shows the case where the measuring device for determining the degree of grinding consists of a grain size sorter that sorts the crushed particles by grain size, and a weighing scale. here 4
The main components are three pulverizers (flour mills) 1.2 and 3.4 and three sieve sorters 5 and 6.7.

第1の粉砕機1は、サイクロン8に空気輸送にて連絡し
、サイクロン8はその下部にエア・ロック・バルブ9を
設けるとともに切換弁付バルブ10で粉砕粒子の一部を
粉砕度を判別する粒大選別機と重量計とからなる測定器
11へ適宜供給するように連絡し、さらに第1の篩選別
機5の供給口へ連絡する。篩選別機5は、本実施例では
粒大によって3段階に選別分離ひき、大粒子排出口12
.中粒子排出口13.小粒子排出口14を有し、大粒子
排出口12は粉砕機1の供給口へ、中粒子排出口13は
第2の粉砕機の供給口へ、小粒子排出口14は、サイク
ロン15へとそれぞれ連絡する。測定器11は、粒大選
別機を内蔵して2段階に選別分離して大粒子を第1の粉
砕機1の供給口へ、その他の粒子を2番目の粉砕機2の
供給ロヘ送給するように連絡する。
The first pulverizer 1 communicates with a cyclone 8 by pneumatic transport, and the cyclone 8 is provided with an air lock valve 9 at its lower part and uses a valve 10 with a switching valve to determine the degree of pulverization of some of the pulverized particles. A measuring device 11 consisting of a grain size sorter and a weighing scale is connected to the measuring device 11 for appropriate supply, and further to the supply port of the first sieve sorter 5. In this embodiment, the sieve sorter 5 separates the particles into three stages depending on the particle size, and has a large particle discharge port 12.
.. Medium particle outlet 13. It has a small particle outlet 14 , a large particle outlet 12 to the supply port of the pulverizer 1 , a medium particle outlet 13 to the supply port of the second pulverizer, and a small particle outlet 14 to the cyclone 15 . Please contact each. The measuring device 11 has a built-in particle size sorter and separates the particles into two stages, and sends large particles to the supply port of the first pulverizer 1 and other particles to the supply port of the second pulverizer 2. Please contact us as follows.

また第2の粉砕機2は、サイクロン15に空気輸送にて
連絡し、サイクロン15はその下部にエア・ロック・バ
ルブ16を設けるとともに切換弁付バルブ17で粉砕粒
子の一部を粉砕度を判別する測定器18へ適宜供給する
ように連絡し、さらに第2の篩選別機6の供給口I\連
絡する。篩選別el16は粒大によって3段階に選別分
離でき、大粒子排出口19.中粒子排出口20、小粒子
排出口21を右し、大粒子排出口19は第2の粉砕機2
の供給口へ、中粒子排出口20は第3の粉砕機3の供給
口へ、小粒子排出口21はサイクロン22へとそれぞれ
連絡する。
Further, the second crusher 2 is connected to a cyclone 15 by pneumatic transport, and the cyclone 15 is provided with an air lock valve 16 at its lower part, and uses a valve 17 with a switching valve to determine the degree of crushing of some of the crushed particles. The sieve sorter 6 is also contacted with the supply port I\ of the second sieve sorter 6. The sieve sorting element 16 can be separated into three stages depending on particle size, and there is a large particle discharge port 19. The medium particle outlet 20 and the small particle outlet 21 are on the right, and the large particle outlet 19 is on the right side of the second crusher 2.
The medium particle discharge port 20 communicates with the supply port of the third crusher 3, and the small particle discharge port 21 communicates with the cyclone 22.

測定器18は、測定器11と同様に、粒大選別機を内蔵
して2段階に選別分離しで、大粒子を第2の粉砕機2の
供給口へ、その他の粒子を第3の粉砕機3の供給口へ送
給ザるように連絡り′る。
Like the measuring device 11, the measuring device 18 has a built-in particle size sorter and separates the large particles into two stages, sending large particles to the supply port of the second crusher 2 and sending other particles to the third crusher. Contact the supply port of machine 3 to send it.

次に第3の粉砕機3は、サイクロン23に空気輸送にて
連絡し、サイクロン23はその下部にエア・ロック・バ
ルブ24を設けるとともに切換弁付バルブ25で粉砕粒
子の一部を粉砕度を判別する測定器26へ適宜供給する
ように連絡し、さらに第3の篩選別機7の供給口へ連絡
する。篩選別機7は粒大によって3段階に選別分離でき
、大粒子排出口27.中粒子排出口28、小粒子排出口
29を有し、大粒子排出口27は第4の粉砕機4の供給
口へ、中粒子排出口28はサイクロン30へ、小粒子排
出口29はサイクロン31へとそれぞれ連絡する。そし
て第4の粉砕機は、サインクロン23に空気輸送にて連
絡する。
Next, the third crusher 3 communicates with the cyclone 23 by pneumatic transport, and the cyclone 23 is provided with an air lock valve 24 at its lower part, and uses a valve 25 with a switching valve to adjust the degree of crushing of some of the crushed particles. It is communicated to the measuring device 26 for discrimination so that it can be appropriately supplied, and further communicated to the supply port of the third sieve sorting machine 7. The sieve sorter 7 can sort and separate particles into three stages depending on particle size, and has a large particle discharge port 27. It has a medium particle discharge port 28 and a small particle discharge port 29, the large particle discharge port 27 is connected to the supply port of the fourth crusher 4, the medium particle discharge port 28 is connected to the cyclone 30, and the small particle discharge port 29 is connected to the cyclone 31. Please contact each of them. The fourth crusher communicates with the Sincron 23 by pneumatic transportation.

サイクロン8.15.23の排気は、ブロア32を介し
てサイクロン33へ連絡し、サイクロン22.31.3
0の排気もブロア34を介してサイク[]ン35へ連絡
し、サイクロン33゜35の排気はバッグフィルター3
6を経て外部へ放出する。サイクロン22.30.31
,33.35は共にその下部にエア・ロック・バルブ3
7.38.39.40.41を設け、砕成物貯留用の粉
体受タンク42.43.44の供給口へ連絡する。この
図中には、測定器11゜18.26が図示さているが、
特に粉砕度を判別する測定器が粒大選別機と重量計とか
らなる場合のもので、測定器が粉砕粒の投影面積測定で
粉砕度を判別するものである場合には、その部分の流れ
は測定用バイパス路となる。
The exhaust air of cyclone 8.15.23 is connected to cyclone 33 via blower 32, and
The exhaust air from cyclones 33 and 35 is also connected to the cyclone 35 via the blower 34, and the exhaust from the cyclones 33 and 35 is connected to the bag filter 3.
6 and then released to the outside. Cyclone 22.30.31
, 33.35 both have air lock valve 3 at the bottom.
7.38.39.40.41 is provided and connected to the supply port of powder receiving tank 42.43.44 for storing crushed material. In this figure, a measuring device 11°18.26 is shown,
In particular, if the measuring device for determining the degree of pulverization consists of a grain size sorter and a weight scale, and if the measuring device determines the degree of pulverization by measuring the projected area of the pulverized grains, the flow of that part is becomes a bypass path for measurement.

次に本実施例の粉砕機1〜4について、第2図に基づき
説明する。
Next, the crushers 1 to 4 of this embodiment will be explained based on FIG. 2.

第2図に示す粉砕機は対向回転自在に一対のロール62
.63を粉砕室内に設け、該ロールそれぞれに軸装した
歯車65.66により係合し、ある回転数差をもって連
動回転する一対の対向するロールを成し、更にロール駆
動用電動機67の駆動調車68に巻装したベルト76を
主軸用調車64に巻装することで一対のロール62.6
3は主電動機67で連動回転する。また前記駆動用電動
機67は変速装置69を有するもので、該変速装置は主
電動機67にインバータを装着したものや任意の可変速
電動機でもよい。その他駆動調車と主軸用調車64とベ
ルト76とによる変速をバリバイヤプーリによって構成
する等、任意に選択できるものである。
The crusher shown in FIG.
.. 63 is provided in the grinding chamber, and is engaged with gears 65 and 66 mounted on each of the rolls, forming a pair of opposing rolls that rotate in conjunction with a certain rotational speed difference, and a driving pulley of the roll driving electric motor 67. By winding the belt 76 wound around the main shaft pulley 64, a pair of rolls 62.6
3 is interlocked and rotated by a main electric motor 67. Further, the driving electric motor 67 has a transmission device 69, and the transmission device may be a main electric motor 67 equipped with an inverter or any variable speed electric motor. Other options may be selected, such as configuring the speed change using the driving pulley, the main shaft pulley 64, and the belt 76 using a vari-byer pulley.

本実施例においては、速度制御用電動機75により回転
速度を調節する可変速電動機を図示した。
In this embodiment, a variable speed electric motor whose rotational speed is adjusted by a speed control electric motor 75 is illustrated.

70は粉砕機上部に設けた供給ホッパー 72は該ホッ
パー71の排出口に設けた繰出ロール、73は同じく制
御弁である。また粉砕室下部は空気輸送用の排出樋74
である。
70 is a supply hopper provided at the top of the crusher; 72 is a delivery roll provided at the outlet of the hopper 71; and 73 is a control valve. In addition, the lower part of the grinding chamber has a discharge gutter 74 for air transportation.
It is.

次に、粉砕度を判別する粒大選別機と重量計とからなる
測定器11,18.26について第3図を参照して説明
する。粉砕機1〜3の粉砕物排出口に連絡したサイクロ
ンの下部に設けたエア・ロック・バルブ9,16.24
下方に切換弁付バルブ10,17.25を設()、該切
換弁は電磁ソレノイド45で開閉駆動する。該バルブに
よって適宜粉砕された試料が供給される測定器11,1
8.26の供給筒46の下部に、臼−ドセル47を付設
しC秤量可能に構成した第1のタンク48を設けるとと
もに、該タンク48の排出口49には電磁ソレノイド5
0によって駆動さる開閉可能なシャッター51を設け、
排出口49の下方に篩網52を入換自在に重載して揺動
自在に設けた粒大選別機である篩選別礪53を設け、本
実施例ではl!i52を通過しない大粒子と通過するそ
の他の粒子とに2段階に選別分離し、Filim別機の
大粒子排出樋54は、ロードセル55を付設して秤量可
能に構成した第2のタンク56に連絡するとともに、そ
の他の粒子の排出樋57を次の粉砕機等の行程へ連絡す
る。前記タンク56の排出口58には電磁ソレノイド5
9により開閉可能に駆動されるシャッター60を設け、
該タンク56下部に排出樋61を設けて粉砕機等の行程
に連絡する。
Next, the measuring devices 11, 18, 26, which are composed of a grain size sorter and a weight scale for determining the degree of grinding, will be explained with reference to FIG. Air lock valve 9, 16.24 installed at the bottom of the cyclone connected to the crushed material outlet of crushers 1 to 3
A valve 10, 17.25 with a switching valve is provided below (), and the switching valve is driven to open and close by an electromagnetic solenoid 45. Measuring device 11, 1 to which a suitably crushed sample is supplied by the valve.
At the lower part of the supply cylinder 46 of 8.26, there is provided a first tank 48 which is equipped with a mortar cell 47 and is configured to be capable of C weighing.
A shutter 51 that can be opened and closed and driven by 0 is provided,
Below the discharge port 49, a sieve sorting bin 53 is provided, which is a grain size sorter in which a sieve screen 52 is stacked so as to be exchangeable and swingable. Large particles that do not pass through the i52 and other particles that do pass are sorted and separated in two stages, and a large particle discharge gutter 54 of the separate Filim machine is connected to a second tank 56 that is equipped with a load cell 55 and configured to be able to weigh. At the same time, the discharge gutter 57 for other particles is connected to the next process such as a crusher. An electromagnetic solenoid 5 is provided at the outlet 58 of the tank 56.
A shutter 60 that is driven to open and close by 9 is provided,
A discharge gutter 61 is provided at the bottom of the tank 56 to communicate with a process such as a crusher.

ここでまず粉砕度を判別する測定器が粒大選別機と重量
計とからなる場合のロール間隙調節の制御回路80につ
いて説明すると、第4図に示すように、供給タンク48
とタンク56によって重IW1.W2を秤量する秤量回
路81を演算回路82に連絡し、さらに基準値設定回路
83とともに比較制御回路84へ連絡する。比較制御回
路84は駆動回路85を介して、速度制御用電動機75
に連絡するとともに、タンク等のシャッターを駆動する
ソレノイド等へ連絡する。
First, the control circuit 80 for adjusting the roll gap when the measuring device for determining the degree of pulverization consists of a particle size sorter and a weight scale will be explained.As shown in FIG.
and heavy IW1. by tank 56. A weighing circuit 81 for weighing W2 is connected to an arithmetic circuit 82, and further connected to a comparison control circuit 84 together with a reference value setting circuit 83. The comparison control circuit 84 connects the speed control motor 75 via the drive circuit 85.
It also contacts the solenoid that drives the shutter of the tank, etc.

また粉砕度を判別する測定する測定器が粉砕粒の投影面
積測定で粉砕度を判断する場合について説明すると、第
5図の如く投影面積測定の画像信号を得るために、粉砕
機後の輸送途中にカメラ86を設ける。たとえば前記測
定器11の如く、切換弁付バルブ10よりバイパスを設
け、バイパス路壁にカメラ86を含む測定部を設ける。
In addition, to explain the case where the measuring device for determining the degree of crushing determines the degree of crushing by measuring the projected area of the crushed particles, as shown in Figure 5, in order to obtain an image signal for measuring the projected area, the A camera 86 is provided. For example, like the measuring device 11, a bypass is provided from the switching valve 10, and a measuring section including a camera 86 is provided on the wall of the bypass path.

このカメラ86で輸送中の粉砕粒をとらえることにより
、粉砕粒を画素数として処理し、投影面積に変換して、
あらかじめ決められた値と比較するものである。比較の
結果、あらかじめ決められた値と粉砕度が異なる場合、
駆動回路89に信号を発して速度制御用電動様75に連
絡するとともにタンク等のシャッターを駆動するソレノ
イド等へ連絡する。
By capturing the crushed grains being transported with this camera 86, the crushed grains are processed as the number of pixels, converted to a projected area,
It is compared with a predetermined value. As a result of comparison, if the grinding degree differs from the predetermined value,
A signal is issued to the drive circuit 89, which communicates with the speed control electric motor 75 and also communicates with a solenoid or the like that drives a shutter of a tank or the like.

上記実施例の作用について説明する。第1図に示すフロ
ー図に基づき説明すると、小麦等の砕料をまず第1の粉
砕機1に供給して粉砕し、その粉砕粒子を空気輸送にし
てサイクロン8へ送給し、エア・[コック・バルブ9.
切換弁イ・」バルブ10を経て、粒大選別をする篩選別
機5へ供給する。該選別機では篩目の異なる篩網を複数
段重載して、その篩網を揺動することによって大中小の
各粒子に選別・分離し、大粒子排出口12.中粒子排出
口13.小粒子排出口14へそれぞれ排出する。ここで
大粒子は第1の粉砕11の供給ホッパーへ還元し、中粒
子は第2の粉砕機2の供給ホッパーへ送給し、小粒子は
サイクロン15へ送給する。
The operation of the above embodiment will be explained. To explain based on the flowchart shown in FIG. 1, crushed materials such as wheat are first supplied to the first crusher 1 and crushed, and the crushed particles are pneumatically transported and sent to the cyclone 8. Cock valve9.
It is supplied to a sieve sorter 5 which sorts grains by size through a switching valve 10. In this sorter, a plurality of sieve screens with different sieve meshes are piled up in multiple stages, and by shaking the sieve screens, the particles are sorted and separated into large, medium and small particles, and the large particle discharge port 12. Medium particle outlet 13. The particles are discharged to the small particle discharge port 14, respectively. Here, large particles are reduced to the feed hopper of the first grinder 11, medium particles are fed to the feed hopper of the second grinder 2, and small particles are fed to the cyclone 15.

さらに第2の粉砕機に供給され粉砕された粉砕粒子はサ
イクロン15へ送給されエア・ロック・バルブ16.切
換弁付バルブ17を経て、第2の篩選別!fi6へ送給
する。第2の篩選別機6においても大中小の各粒子に選
別分離し、大粒子排出口19.中粒子排出口20.小粒
子排出口21へそれぞれ排出する。ここで大粒子は第2
の粉砕機の供給ホッパーへ還元し、中粒子は第3の粉砕
機の供給ホッパーへ送給し、小粒子はサイクロン22へ
送給して、気流選別してエア・ロック・バルブ37を経
て砕成物としてタンク42に貯留する。
Further, the crushed particles supplied to the second crusher are sent to the cyclone 15, and the air lock valve 16. After passing through the switching valve 17, the second sieve sorting begins! Send to fi6. The second sieve sorter 6 also sorts and separates particles into large, medium and small particles, and the large particle discharge port 19. Medium particle outlet 20. The particles are discharged to the small particle discharge port 21, respectively. Here, the large particle is the second
The medium particles are sent to the feed hopper of the third grinder, and the small particles are sent to the cyclone 22 where they are air-separated and crushed via the air lock valve 37. It is stored in the tank 42 as a product.

また第3の粉砕機3に供給され粉砕された粉砕粒子は、
Iナイフロン23へ送給され、エア・ロック・バルブ2
4.切換弁付バルブ25を経て第3の篩選別機7へ送給
ゴる。第3の篩選別機7においても大中小の各粒子に選
別・分離し、大粒子排出口27.中粒子排出口28.小
粒子排出口29へそれぞれ排出する。ここで大粒子は第
4の粉砕機4の供給ホッパーへ送給し、中粒子はサイク
ロン30へ送給し気流選別してエア・ロック・バルブ3
8を経て、砕成物としてタンク44に貯留する。小粒子
はサイクロン31へ送給し、気流選別してエア・ロック
・バルブ39を経て、砕成物としてタンク43に貯留す
る。サイクロン8,15.23の排気をサイクロン33
へ送給すると共に、サイクロン22゜30.31の排気
もサイクロン35へ送給し、空気選別してエア・ロック
・バルブ40.4iを経て、砕成物としてタンク43に
貯留する。
Moreover, the crushed particles supplied to the third crusher 3 and crushed are
I-kniferon 23 and air lock valve 2
4. It is fed to the third sieve sorter 7 via a switching valve 25. The third sieve sorter 7 also sorts and separates particles into large, medium and small particles, and the large particle discharge port 27. Medium particle outlet 28. The particles are discharged to the small particle discharge port 29, respectively. Here, the large particles are sent to the supply hopper of the fourth crusher 4, and the medium particles are sent to the cyclone 30, where they are separated by airflow and then put into the air lock valve 3.
8 and stored in a tank 44 as a crushed material. The small particles are sent to the cyclone 31, separated by airflow, passed through the air lock valve 39, and stored in the tank 43 as crushed material. Cyclone 8, 15.23 exhaust to cyclone 33
At the same time, the exhaust gas from the cyclones 22, 30, and 31 is also sent to the cyclone 35, where it is air-separated, passes through an air lock valve 40.4i, and is stored in a tank 43 as crushed material.

粉砕度を判別する測定器が粒大選別機と重帛計とからな
る場合のロールの回転速度の調節について述べると、例
えば粉砕機1において、その供給ホッパーに供給された
小麦等の砕料が対のロール62.63の対向回転する間
隙を通過する際に粉砕され、サイクロン8に空気輸送さ
れるが、切換弁付バルブ10の操作で、その粉砕粒子の
一部を試料として測定器11へ導入し、該器11内では
、まずその試料を第1のタンク48に貯留し、ロードセ
ル47で重ff1lA/+を秤量した後、該タンク48
下部のシャッター51を開放し、篩選別機53に送給し
て粒大選別をし、ある所定の篩目の選別篩網52を通過
する物と通過しない物とに分離し、ここでは通過しなか
った試料を第2のタンク56に供給して貯留し、O−ド
セル55で重ff1W2を秤量する。ここで第4図に示
す制御回路を説明すると、WlとW2の比W2/W+を
比較制御回路84内で、演算すると共に基準値設定回路
83から出力される基準値と比較し、W 2 / W 
+の比が大きければ粉砕度が低くロールの回転速度が速
いことを意味するから、比較制御回路84から駆動回路
85へ信号を発して速度制御用電動別75へ電動機67
の回転を低くするように駆動信号を与え粉砕度を高め、
またW 2 / W +の比が基準値と比較して小さけ
れば、粉砕度が高すぎ0−ルの回転速度が遅いことを意
味するから、該電動機75を逆回転させて電動機67の
回転を高くし、粉砕度を低めることによって常に所定の
粉砕度で、粉砕機の運転を安定的に維持できるものであ
る。この場合、粒大選別機と重量計とを使用することに
よって粉砕度を直接的に判別しており、製粉の行程を示
すフロー図〈第1図)にも図示したように、各粉砕機に
供給される砕料の聞が変化したり、また次の篩選別機か
ら還元される砕料が存在しても対応できるものである。
Regarding the adjustment of the rotational speed of the rolls when the measuring device for determining the degree of crushing consists of a grain size sorter and a weight meter, for example, in the crusher 1, when the crushed material such as wheat supplied to the supply hopper is They are crushed as they pass through the gap between the pair of rolls 62 and 63 that rotate oppositely, and are pneumatically transported to the cyclone 8. By operating the switching valve 10, some of the crushed particles are sent as a sample to the measuring device 11. In the vessel 11, the sample is first stored in the first tank 48, and after weighing the weight ff1lA/+ with the load cell 47, the sample is stored in the first tank 48.
The shutter 51 at the bottom is opened, and the particles are fed to a sieve sorter 53 to be sorted by grain size and separated into those that pass through the sorting sieve 52 with a certain sieve size and those that do not. The remaining sample is supplied to the second tank 56 and stored therein, and the weight ff1W2 is weighed using the O-docel 55. Now, to explain the control circuit shown in FIG. 4, the ratio W2/W+ of Wl and W2 is calculated in the comparison control circuit 84 and compared with the reference value output from the reference value setting circuit 83, and W 2 /W+ is calculated. W
If the + ratio is large, it means that the degree of grinding is low and the rotational speed of the roll is high. Therefore, a signal is sent from the comparison control circuit 84 to the drive circuit 85 and the electric motor 67 is sent to the electric motor 67 for speed control.
A drive signal is given to lower the rotation of the machine to increase the degree of grinding.
Moreover, if the ratio of W 2 / W + is small compared to the reference value, it means that the degree of grinding is too high and the rotation speed of the 0-wheel is slow. By increasing the grinding degree and lowering the grinding degree, stable operation of the crusher can be maintained at a predetermined grinding degree at all times. In this case, the degree of pulverization is directly determined by using a particle size sorter and a weight scale, and as shown in the flow diagram (Figure 1) showing the milling process, each pulverizer is It is possible to cope with changes in the amount of crushed material to be supplied, or even if there is crushed material returned from the next sieve sorter.

また粉砕度を判定する測定器が、投影面積測定で粉砕度
を判定する場合について述べると、バイパス路に設けた
カメラ86を含む測定部から得られた信号はA/D、D
/Aコンバーター87で一粒ごと、にその投影面積の画
素数として解析され、画素数=πr2の式からCPtJ
88により一粒の粒径に換算する。CPU88にはあら
かじめ粉砕度を設定して、前記換算した粒径の粒度分布
と設定した粉砕度を比較し、粒度分布の頂点が設定値よ
り大きければ粉砕度が低く、ロールの回転速度が速いこ
とを意味するからCPU88から駆動回路89へ信号を
発して速度制御用電動機75へ電動機67の回転を低く
するように駆動信号を与え、逆に粒度分布の頂点が設定
値より小さければ粉砕度が高く、ロールの回転速度が遅
いことを意味するからCPU88から信号を発し電動機
67の回転を高くするように駆動回路89より駆動信号
を与えて、常に所定の粉砕度で粉砕機の運転を安定的に
維持できるものである。
Regarding the case where the measuring instrument for determining the degree of crushing determines the degree of crushing by measuring the projected area, the signal obtained from the measuring section including the camera 86 installed in the bypass path is
/A converter 87 analyzes each grain as the number of pixels of its projected area, and from the formula of number of pixels = πr2, CPtJ
88 to convert to the particle size of one grain. The degree of grinding is set in advance in the CPU 88, and the particle size distribution of the converted particle size is compared with the set degree of grinding. If the top of the particle size distribution is larger than the set value, the degree of grinding is low and the rotation speed of the roll is high. This means that the CPU 88 issues a signal to the drive circuit 89 and gives a drive signal to the speed control motor 75 to lower the rotation of the motor 67. Conversely, if the peak of the particle size distribution is smaller than the set value, the degree of grinding is high. Since this means that the rotational speed of the rolls is slow, a signal is generated from the CPU 88 and a drive signal is given from the drive circuit 89 to increase the rotation of the electric motor 67, thereby stably operating the crusher at a predetermined degree of crushing. It is something that can be maintained.

〔発明の効果〕〔Effect of the invention〕

本発明の粉砕機の粉砕調節装置は、粉砕度を判別する測
定器を粉砕機に関連的に付設して、この測定器の出力信
号によって粉砕ロールの回転速度を調節して、砕料の諸
特性の差異などにかかわらず、所定の粉砕度を常に安定
的に維持することができるものである。また製粉のため
に使用される粉砕機では、段階的に粉砕度を定めて粉砕
を行うため、各粉砕機においてより正確な粉砕度の管理
が要求されるが、この装置によれば複数の粉砕機を適切
に操作運転することが容易にでき、常に高品質の砕成物
を効率的に量産できるものである。
The crushing adjustment device for a crusher according to the present invention includes a measuring device for determining the degree of crushing attached to the crushing machine, and the rotational speed of the crushing roll is adjusted based on the output signal of this measuring device, thereby controlling the various properties of the crushed material. Regardless of differences in characteristics, a predetermined degree of grinding can always be stably maintained. In addition, in the crushers used for flour milling, the degree of crushing is determined in stages and the degree of crushing is determined in stages, so each crusher requires more accurate control of the degree of crushing. It is easy to operate the machine appropriately, and it is possible to efficiently mass-produce high-quality crushed material at all times.

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

第1図は本発明の一実施例を示す製粉の行程のフロー図
、第2図は粉砕機の側断面図、第3図は粉砕度を判別す
る測定器の一実施例を示し、第4図はその制御回路図、
第5図は別実施例の粉砕度を判定する測定器及び回路図
である。 1・・・粉砕機、2・・・粉砕機、3・・・粉砕機、4
・・・粉砕機、5・・・篩選別機、6・・・篩選別機、
7・・・篩選別機、8・・・サイクロン、9・・・エア
・ロック・バルブ、10・・・バルブ、11・・・測定
器、12・・・大粒子排出口、13・・・中粒子排出口
、14・・・小粒子排出口、15・・・サイクロン、1
6・・・エア・ロック・バルブ、17・・・バルブ、1
8・・・測定器、19・・・大粒子排出口、20・・・
中粒子排出口、21・・・小粒子排出口、22・・・ナ
イクOン、23・・・サイクロン、24・・・エア・ロ
ック・バルブ、25・・・バルブ、26・・・測定器、
27・・・大粒子排出口、28・・・中粒子排出口、2
9・・・小粒子排出口、30・・・サイクロン、32・
・・ブロア、33・・・サイクロン、34・・・ブロア
、35・・・サイクロン、36・・・バッグフィルター
、37・・・エア・ロック・バルブ、38・・・エア・
ロック・バルブ、39・・・エア・ロック・バルブ、4
0・・・エア・ロック・バルブ、41・・・エア・ロッ
ク・バルブ、42・・・タンク、43・・・タンク、4
4・・・タンク、45・・・ソレノイド、46・・・供
給筒、47・・・ロードセル、48・・・供給タンク、
49・・・排出口、50・・・ソレノイド、51・・・
シャッター、52、部組、53・・・篩選別機、54・
・・大粒子排出樋、55・・・ロードセル、56・・・
タンク、57・・・排出樋、58・・・排出口、59・
・・ソレノイド、60・・・シャッター61・・・排出
樋、62・・・ロール、63・・・ロール、64・・・
主軸用調車、65・・・主軸用歯車、66・・・副軸用
歯車、67・・・主電動機、68・・・駆動調車、69
・・・変速装置、70・・・供給ホッパー、71・・・
機枠、72・・・繰出ロール、73・・・制御弁、74
・・・排出樋、75・・・速度制御用電動機、76・・
・ベルト、80・・・制御回路、81・・・秤量回路、
82・・・演算回路、83・・・基準値設定回路、83
・・・比絞制御回路、85・・・駆動回路、86・・・
CCDカメラ、87・・・A/D、D/Aコンバーター
 88・・・CPU、89・・・駆動回路。
FIG. 1 is a flowchart of the milling process showing one embodiment of the present invention, FIG. 2 is a side sectional view of a crusher, FIG. 3 is an embodiment of a measuring device for determining the degree of grinding, and FIG. The figure is the control circuit diagram,
FIG. 5 is a measuring device and a circuit diagram for determining the degree of grinding according to another embodiment. 1...Crusher, 2...Crusher, 3...Crusher, 4
... crusher, 5... sieve sorter, 6... sieve sorter,
7... Sieve sorter, 8... Cyclone, 9... Air lock valve, 10... Valve, 11... Measuring device, 12... Large particle discharge port, 13... Medium particle outlet, 14...Small particle outlet, 15...Cyclone, 1
6...Air lock valve, 17...Valve, 1
8... Measuring device, 19... Large particle outlet, 20...
Medium particle discharge port, 21...Small particle discharge port, 22...Nike ON, 23...Cyclone, 24...Air lock valve, 25...Valve, 26...Measuring instrument ,
27...Large particle outlet, 28...Medium particle outlet, 2
9...Small particle outlet, 30...Cyclone, 32.
...Blower, 33...Cyclone, 34...Blower, 35...Cyclone, 36...Bag filter, 37...Air lock valve, 38...Air...
Lock valve, 39...Air lock valve, 4
0... Air lock valve, 41... Air lock valve, 42... Tank, 43... Tank, 4
4... Tank, 45... Solenoid, 46... Supply tube, 47... Load cell, 48... Supply tank,
49...Discharge port, 50...Solenoid, 51...
Shutter, 52, subassembly, 53... sieve sorting machine, 54.
...Large particle discharge gutter, 55...Load cell, 56...
Tank, 57... Discharge gutter, 58... Discharge port, 59.
...Solenoid, 60...Shutter 61...Discharge gutter, 62...Roll, 63...Roll, 64...
Main shaft pulley, 65 Main shaft gear, 66 Subshaft gear, 67 Main motor, 68 Drive pulley, 69
...Transmission device, 70... Supply hopper, 71...
Machine frame, 72... Feeding roll, 73... Control valve, 74
...Discharge gutter, 75...Speed control motor, 76...
・Belt, 80...control circuit, 81...weighing circuit,
82... Arithmetic circuit, 83... Reference value setting circuit, 83
... Specific diaphragm control circuit, 85... Drive circuit, 86...
CCD camera, 87...A/D, D/A converter 88...CPU, 89...drive circuit.

Claims (3)

【特許請求の範囲】[Claims] (1)、回転数差を設けた一対のロールを対向回転自在
に設け、前記一対のロールを連動回転駆動する駆動側に
変速装置を設けた粉砕機において、粉砕度を判別する測
定器を粉砕機に関連的に付設して、該測定器の出力信号
を制御装置を介して前記変速装置に連絡したことを特徴
とする粉砕機の粉砕度調節装置。
(1) In a crusher equipped with a pair of rolls that rotate at different rotation speeds and are rotatable in opposition to each other, and a transmission device is installed on the drive side to drive the pair of rolls in conjunction with each other, a measuring device for determining the degree of crushing is used. A grinding degree adjusting device for a grinding machine, characterized in that the grinding degree adjusting device is attached to the grinding machine and communicates an output signal of the measuring device to the transmission device via a control device.
(2)、測定器は粉砕した粒子を粒大選別して粉砕度を
判別する粒大選別機と重量計とからなる請求項(1)記
載の粉砕機の粉砕度調節装置。
(2) The grinding degree adjusting device for a grinding machine according to claim (1), wherein the measuring device comprises a grain size sorter and a weighing scale for sorting the crushed particles by size to determine the degree of crushing.
(3)、測定器が粉砕粒の投影面積測定で粉砕度を判別
するものである請求項(1)記載の粉砕機の粉砕度調節
装置。
(3) The grinding degree adjusting device for a crusher according to claim (1), wherein the measuring device determines the grinding degree by measuring the projected area of the crushed grains.
JP26221988A 1988-10-17 1988-10-17 Grinding degree control device for crusher Expired - Fee Related JP2710039B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26221988A JP2710039B2 (en) 1988-10-17 1988-10-17 Grinding degree control device for crusher

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26221988A JP2710039B2 (en) 1988-10-17 1988-10-17 Grinding degree control device for crusher

Publications (2)

Publication Number Publication Date
JPH02107361A true JPH02107361A (en) 1990-04-19
JP2710039B2 JP2710039B2 (en) 1998-02-10

Family

ID=17372734

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26221988A Expired - Fee Related JP2710039B2 (en) 1988-10-17 1988-10-17 Grinding degree control device for crusher

Country Status (1)

Country Link
JP (1) JP2710039B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20030014088A (en) * 2001-08-09 2003-02-15 가부시끼가이샤 니뽄 코우코꾸 An apparatus for displaying goods
WO2023171765A1 (en) * 2022-03-11 2023-09-14 Jfeスチール株式会社 Coal grinding method, method of manufacturing coal for coke, and coal grinding apparatus

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101678625B1 (en) 2008-07-02 2016-11-23 뷔흘러 에이지 Apparatus and method for producing flour and/or semolina

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20030014088A (en) * 2001-08-09 2003-02-15 가부시끼가이샤 니뽄 코우코꾸 An apparatus for displaying goods
WO2023171765A1 (en) * 2022-03-11 2023-09-14 Jfeスチール株式会社 Coal grinding method, method of manufacturing coal for coke, and coal grinding apparatus

Also Published As

Publication number Publication date
JP2710039B2 (en) 1998-02-10

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