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JPH0245494B2 - - Google Patents

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Publication number
JPH0245494B2
JPH0245494B2 JP59006924A JP692484A JPH0245494B2 JP H0245494 B2 JPH0245494 B2 JP H0245494B2 JP 59006924 A JP59006924 A JP 59006924A JP 692484 A JP692484 A JP 692484A JP H0245494 B2 JPH0245494 B2 JP H0245494B2
Authority
JP
Japan
Prior art keywords
grain
mixing
discharge
preliminary
conveyor
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP59006924A
Other languages
Japanese (ja)
Other versions
JPS60150823A (en
Inventor
Toshihiko Satake
Yukio Hosaka
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 JP59006924A priority Critical patent/JPS60150823A/en
Publication of JPS60150823A publication Critical patent/JPS60150823A/en
Publication of JPH0245494B2 publication Critical patent/JPH0245494B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/80Forming a predetermined ratio of the substances to be mixed
    • B01F35/83Forming a predetermined ratio of the substances to be mixed by controlling the ratio of two or more flows, e.g. using flow sensing or flow controlling devices
    • B01F35/832Flow control by weighing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/60Mixing solids with solids

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Adjustment And Processing Of Grains (AREA)
  • Accessories For Mixers (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、穀物、例えば白米等を所定の重量比
で混合する穀物混合装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a grain mixing device for mixing grains, such as polished rice, in a predetermined weight ratio.

〔従来技術〕[Prior art]

複数の混合予備タンクの吐出口に定量排出手段
を設け、各タンクから任意の混合比で穀物を排出
させる混合装置において、各タンクからコンベア
上に同時に排出を開始て、一定時間内に排出を完
了させて混合する場合、複数の混合予備タンクの
各吐出口は、コンベアの上面の上方に距離間隔を
おいて設けられているので、排出開始時と排出完
了時には必然的に混合斑を生じるものである。つ
まり、第3図に示すように、各タンクが一斉に排
出を開始した後、コンベア3の始端側のタンク
T1から排出された穀物が、前記コンベア終端側
のタンクT5の吐出口の下方に達する間の混合物
は、各タンクからの全ての穀物が合流していない
ので著しく不均一であり、さらに撹拌装置を必要
とする等の不具合を生じていた。
In a mixing device that is equipped with quantitative discharge means at the discharge ports of multiple preliminary mixing tanks and discharges grain from each tank at an arbitrary mixing ratio, discharge from each tank is started simultaneously onto a conveyor and the discharge is completed within a certain period of time. When mixing by mixing, the discharge ports of the plurality of preliminary mixing tanks are provided at intervals above the top surface of the conveyor, so uneven mixing inevitably occurs at the start and completion of discharge. be. In other words, as shown in Fig. 3, after all tanks start discharging at the same time,
While the grains discharged from T 1 reach the lower part of the outlet of tank T 5 at the end of the conveyor, the mixture is significantly non-uniform as not all the grains from each tank are combined, and the mixture is further stirred. This caused problems such as the need for additional equipment.

〔発明の目的〕[Purpose of the invention]

本発明は上記に鑑み、全ての穀物が終始均一に
合流して搬送されるとともに、各混合予備タンク
からの排出量を制御して一貫して所定の均一な混
合を行うことのできる混合装置を提供することを
目的とするものである。
In view of the above, the present invention provides a mixing device that is capable of uniformly merging and conveying all the grains from beginning to end, and that can consistently perform predetermined uniform mixing by controlling the discharge amount from each mixing reserve tank. The purpose is to provide

〔発明の構成〕[Structure of the invention]

本発明の穀物混合装置は、コンベア上方に並設
された複数の混合予備タンクと、前記各混合予備
タンクの吐出口に設けられた排出量可変排出バル
ブと、入力された穀物混合比により、前記排出量
可変排出バルブのそれぞれの回転数を算出し、設
定された重量混合比で前記混合予備タンクから穀
物を排出させる演算制御装置とからなり、前記排
出量可変排出バルブは、前記コンベアの搬送方向
に対して、順次時差をおいて作動開始するように
前記演算制御装置に連絡されたことを特徴とする
構成である。
The grain mixing device of the present invention includes a plurality of preliminary mixing tanks arranged in parallel above the conveyor, a variable discharge discharge valve provided at the discharge port of each of the preliminary mixing tanks, and a grain mixing ratio that is input. It is comprised of an arithmetic and control device that calculates the rotational speed of each of the variable discharge volume discharge valves and discharges the grain from the mixing reserve tank at a set weight mixing ratio, and the variable discharge volume discharge valves are configured to rotate in the direction of conveyance of the conveyor. This configuration is characterized in that the arithmetic and control unit is contacted to start operating at different time intervals.

〔作 用〕 これにより、各混合予備タンク内の穀物は、穀
物混合比に応じた回転数で駆動する排出量可変排
出バルブによつて一定時間、前記混合比に応じた
流量で排出を行うのであるが、前記排出バルブは
コンベアの搬送方向に対して、順次時差をおいて
作動を開始し、終始全ての穀物が重なり合つた状
態で搬送されることになる。
[Function] As a result, the grains in each preliminary mixing tank are discharged for a certain period of time at a flow rate according to the mixing ratio by the variable discharge valve which is driven at a rotation speed according to the grain mixing ratio. However, the discharge valves start operating at different times with respect to the conveyance direction of the conveyor, and all the grains are conveyed in an overlapping state from beginning to end.

また、容積重測定機を設けた場合は、各穀物の
容積重と排出バルブの1回転当たりの排出容量と
から、穀物の容積重の違いに応じてより正確な重
量比で排出することができる。
Additionally, if a volumetric weight measuring device is installed, it is possible to discharge grains at a more accurate weight ratio based on the volumetric weight of each grain and the discharge volume per revolution of the discharge valve, depending on the difference in grain volumetric weight. .

〔実施例〕〔Example〕

以下、本発明の穀物混合装置の好適な実施例に
ついて、図面を参照しながら説明する。
Hereinafter, preferred embodiments of the grain mixing device of the present invention will be described with reference to the drawings.

第1図は、本発明の穀物混合装置の一実施例を
示す概略図である。1は、混合予備タンクT1
T5に張り込む各穀物の容積重を計測する容積重
測定機である。2,4は揚穀機、3はコンベア、
B1〜B5は、混合予備タンクT1〜T5の吐出口に設
けられた、各タンクからの穀物排出量を制御でき
る排出量可変排出バルブ、例えばパルスモータで
作動する堅型ロータリーバルブである。5は、容
積重測定機1と排出量可変排出バルブB1〜B5
連絡された、マイクロプロセツサ等からなる演算
制御装置、6は表示器、7はプリンタ、8は、所
望の穀物混合比を入力するキーボードである。
FIG. 1 is a schematic diagram showing an embodiment of the grain mixing device of the present invention. 1 is the mixing reserve tank T 1 ~
This is a volumetric weight measuring machine that measures the volumetric weight of each grain loaded into T5 . 2 and 4 are grain lifting machines, 3 is a conveyor,
B1 to B5 are variable discharge valves that can control the amount of grain discharged from each tank, which are installed at the discharge ports of the preliminary mixing tanks T1 to T5 , such as solid rotary valves operated by a pulse motor. be. 5 is an arithmetic control unit consisting of a microprocessor, etc., which is connected to the volumetric weight measuring device 1 and variable discharge volume discharge valves B 1 to B 5 ; 6 is a display; 7 is a printer; 8 is a desired grain mixture. This is a keyboard for inputting ratios.

次に、前記実施例における作用について述べ
る。
Next, the operation of the above embodiment will be described.

容積重測定機1を通して、各異品質の穀物の単
位体積当たりの重量である容積重が測定された穀
物は、揚穀機2を介して、各穀物毎に混合予備タ
ンクT1〜T5に張り込まれるとともに、前記容積
重測定機1で計測された各穀物の容積重は、各穀
物毎に演算制御装置5の記憶部に記憶される。
The grains whose volumetric weight, which is the weight per unit volume of each grain of different quality, has been measured through the volumetric weight measuring machine 1 are sent to mixing reserve tanks T 1 to T 5 for each grain via the grain lifting machine 2. The volumetric weight of each grain measured by the volumetric weight measuring device 1 while being loaded is stored in the storage section of the arithmetic and control unit 5 for each grain.

かくして、混合予備タンクT1〜T5には、それ
ぞれ異品質の穀物が張り込まれ、演算制御装置5
には、各混合予備タンクT1〜T5に張り込まれた
穀物の容積重が記憶されている。次に、これら各
異品質の穀物を混合するために、所望の混合比と
総重量とをキーボード8から入力すると、演算制
御装置5は、記憶した各穀物の容積重から各混合
予備タンクT1〜T5の排出バルブB1〜B5の回転数
を算出する。すなわち、総重量をW0、各混合予
備タンクT1〜 T5の混合重量比を、例えば混合予備タンク T1:T2:T3:T4:T5=1:2:3:4:5と
を指定したとすると、各混合予備タンクT1〜T5
からのそれぞれの排出重量W1〜W5は、 W1= W0/15、 W5=2W0/15 W3=3W0/15、 W4=4W0/15 W5=5W0/15 ……(1) となる。そして、排出量可変バルブB1〜B5の1
回転当たりの排出容量をVとし、各混合予備タン
クT1〜T5に張り込まれ、演算制御装置5の記憶
部に記憶された各穀物の容積重をそれぞれw1
w5とすると、各排出バルブC1〜C5の回転数n1
n5は、次のようになる。
In this way, grains of different quality are filled in the preliminary mixing tanks T 1 to T 5 respectively, and the arithmetic and control unit 5
, the volumetric weight of the grains loaded into each of the preliminary mixing tanks T 1 to T 5 is stored. Next, in order to mix these grains of different quality, when a desired mixing ratio and total weight are input from the keyboard 8, the arithmetic and control unit 5 selects each mixing reserve tank T 1 from the stored volumetric weight of each grain. ~ Calculate the rotation speed of the discharge valves B 1 ~ B 5 of T 5 . That is, the total weight is W 0 , and the mixing weight ratio of each preliminary mixing tank T 1 to T 5 is, for example, mixing preliminary tanks T 1 :T 2 :T 3 :T 4 :T 5 =1:2:3:4: 5, each mixing reserve tank T 1 to T 5
The respective discharge weights W 1 to W 5 from W 1 = W 0 /15, W 5 = 2W 0 /15 W 3 = 3W 0 /15, W 4 = 4W 0 / 15 W 5 = 5W 0 /15 ...(1) becomes. And 1 of variable discharge valves B 1 to B 5
Let the discharge capacity per revolution be V, and the volumetric weight of each grain filled in each of the preliminary mixing tanks T 1 to T 5 and stored in the storage section of the arithmetic and control unit 5 are respectively w 1 to
When w is 5 , the rotation speed of each discharge valve C 1 to C 5 is n 1 to
n 5 becomes as follows.

n1= W0/(V・w1) = W0/(15・V・w1) n2= W1/(V・w2) =2W0/(15・V・w2) n3= W3/(V・w3) =3W0/(15・V・w3) n4= W4・(V・w4) =4W0/(15・V・w4) n5= W5/(V・w5) =5W0/(15・V・w5) ……(2) 演算制御装置5では、上記(2)式の演算を行い、
各排出バルブB1〜B5を回転させるモータを駆動
させ、演算された総回転数n1〜n5だけ、前記各排
出バルブを回転させるのであるが、前記各排出バ
ルブB1〜B5は、また、演算制御装置5によつて、
順次一定時間経過後駆動を開始するよう制御され
る。つまり混合予備タンクT1の排出口に設けら
れた排出量可変排出バルブB1から排出された穀
物が(第2図参照)、排出量可変排出バルブB2
直下に達した時、該バルブB2が排出を開始し、
同様に、前記穀物がコンベア3の進行とともに、
排出バルブB3,B4,B5のそれぞれの直下に達し
た時、前記バルブB3,B4,B5が順次遅延して排
出を開始するように、演算制御装置5は、前記各
排出量可変排出バルブB1〜B5間のそれぞれの距
離とコンベア3の速度とから、前記バルブB1
B5の作動時間差を算出するよう構成されており、
前記各バルブB1〜B5は、前記作動時間差を介し
て作動を開始し、それぞれ同一時間、上記(2)式で
算出された回転数だこ回転する。
n 1 = W 0 / (V・w 1 ) = W 0 / (15・V・w 1 ) n 2 = W 1 / (V・w 2 ) = 2W 0 / (15・V・w 2 ) n 3 = W 3 / (V・w 3 ) = 3W 0 / (15・V・w 3 ) n 4 = W 4・(V・w 4 ) = 4W 0 / (15・V・w 4 ) n 5 = W 5 / (V・w 5 ) = 5W 0 / (15・V・w 5 ) ...(2) The arithmetic and control unit 5 calculates the above equation (2),
The motor that rotates each of the discharge valves B 1 to B 5 is driven to rotate each of the discharge valves by the calculated total number of rotations n 1 to n 5 . , Also, by the arithmetic and control unit 5,
Control is performed to start driving after a certain period of time has passed. In other words, when the grain discharged from the variable discharge volume discharge valve B1 provided at the discharge port of the mixing reserve tank T1 (see Fig. 2) reaches the position immediately below the variable discharge volume discharge valve B2 , said valve B 2 starts draining,
Similarly, as the grain progresses on the conveyor 3,
The arithmetic and control unit 5 controls the discharge valves B 3 , B 4 , and B 5 so that when the discharge valves B 3 , B 4 , and B 5 reach the position immediately below each discharge valve, the valves B 3 , B 4 , and B 5 sequentially delay and start discharging. From the respective distances between the variable volume discharge valves B 1 to B 5 and the speed of the conveyor 3, the valves B 1 to B 5 are
B 5 is configured to calculate the operating time difference,
Each of the valves B 1 to B 5 starts operating with the difference in operating time, and rotates for the same period of time at the number of revolutions calculated by the above equation (2).

いま、各混合予備タンクT1〜T5吐出口のそれ
ぞれの間隔を全てlとし、コンベア3の速さをs
とすると、排出バルブB1の排出開始から、排出
バルブB1〜B5の作動時間差は、それぞれB2
l/s、B3…2・l/s、B4…3・l/s、B5
…4・l/sとなる。
Now, the intervals between the discharge ports of each preliminary mixing tank T 1 to T 5 are all 1, and the speed of the conveyor 3 is s.
Then, the difference in operating time of discharge valves B 1 to B 5 from the start of discharge of discharge valve B 1 is B 2 ...
l/s, B 3 …2・l/s, B 4 …3・l/s, B 5
...4.l/s.

そして、排出終了時には、排出開始時と同一の
時差を介して、排出量可変排出バルブB1から順
次B5へと排出を終了するので、混合予備タンク
T1〜T5から排出される穀物全てが、最後まで重
なり合つて合流され、コンベア3によつて同時に
搬送が終了し、揚穀機4を介して次行程に移送さ
れる。
Then, at the end of discharge, the discharge is completed sequentially from variable discharge valve B 1 to B 5 through the same time difference as at the start of discharge, so that the reserve mixing tank
All of the grains discharged from T 1 to T 5 are overlapped and merged until the end, and conveyance is completed at the same time by the conveyor 3, and transferred to the next process via the grain lifting machine 4.

〔発明の効果〕〔Effect of the invention〕

以上のように、本発明の穀物混合装置による
と、混合穀物の総重量と所望の重量混合を入力す
るだけで、複数の混合予備タンクから終始均一な
重量混合比の穀物が排出されるのはもちろんのこ
と、各混合予備タンクからの排出開始に順次時差
を設け、排出される穀物が全て合流しながらコン
ベアで搬送されるので、混合予備タンクからの排
出開始時及び終了時における混合斑を解消し、均
一な品質で穀物の混合が行える。そのため、穀物
の計数管理がより容易となり、また、各タンクか
らの穀物の排出だけで略混合が達成されるから、
混合のための特別な撹拌装置を必要としない。
As described above, according to the grain mixing device of the present invention, by simply inputting the total weight of mixed grains and the desired weight mixture, grains with a uniform weight mixing ratio from beginning to end can be discharged from the plurality of preliminary mixing tanks. Of course, there is a time difference in the start of discharging from each preliminary mixing tank, and all the discharged grains are conveyed by the conveyor while merging together, eliminating uneven mixing at the start and end of discharging from the preliminary mixing tank. This allows grains to be mixed with uniform quality. This makes grain counting management easier, and mixing can be achieved simply by discharging grain from each tank.
Does not require special stirring equipment for mixing.

また、容積重測定機を設けた場合は、各穀物の
容積重と排出バルブの1回転当たりの排出容量と
から、穀物の容積重の違いに応じてより正確な重
量比で排出でき、終始一貫して均一な混合が行え
る。
In addition, if a volumetric weight measuring device is installed, it is possible to discharge at a more accurate weight ratio according to the difference in volumetric weight of each grain based on the volumetric weight of each grain and the discharge volume per revolution of the discharge valve, and it is possible to discharge the grain at a more accurate weight ratio from beginning to end. to ensure uniform mixing.

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

第1図は、本発明の穀物混合装置の一実施例を
示す概略図、第2図は、本実施例における穀物混
合装置を使用して穀物混合を行うときの説明図、
第3図は、従来の穀物混合装置を用いて混合を行
うときの説明図である。 1…容積重測定機、2,4…揚穀機、3…コン
ベア、5…演算制御装置、6…表示器、7…プリ
ンタ、8…キーボード、T1〜T5…混合予備タン
ク、B1〜B5…排出量可変排出バルブ。
FIG. 1 is a schematic diagram showing one embodiment of the grain mixing device of the present invention, and FIG. 2 is an explanatory diagram when grain mixing is performed using the grain mixing device of the present embodiment.
FIG. 3 is an explanatory diagram when mixing is performed using a conventional grain mixing device. 1... Volumetric weight measuring machine, 2, 4... Grain lifting machine, 3... Conveyor, 5... Arithmetic control unit, 6... Display, 7... Printer, 8... Keyboard, T 1 to T 5 ... Mixing reserve tank, B 1 ~B 5 ...Variable discharge valve.

Claims (1)

【特許請求の範囲】 1 コンベア上方に並設された複数の混合予備タ
ンクと、前記各混合予備タンクの吐出口に設けら
れた排出量可変排出バルブと、入力された穀物混
合比により前記排出量可変排出バルブのそれぞれ
の回転数を算出し、設定された重量混合比で前記
混合予備タンクから穀物を排出させる演算制御装
置と、からなり、前記排出量可変排出バルブは、
前記コンベアの搬送方向に対して、順次時差をお
いて作動開始するように前記演算制御装置に連絡
されたことを特徴とする穀物混合装置。 2 上記各排出量可変排出バルブの回転数は穀物
混合比と容積重とによつて算出すべく、混合穀物
毎の容積重を測定する容積重測定機を備えてなる
請求項1記載の穀物混合装置。
[Scope of Claims] 1. A plurality of preliminary mixing tanks arranged in parallel above the conveyor, a discharge variable discharge valve provided at the discharge port of each preliminary mixing tank, and a variable discharge amount according to the input grain mixing ratio. and an arithmetic and control device that calculates the rotational speed of each variable discharge valve and discharges the grain from the mixing preliminary tank at a set weight mixing ratio, the variable discharge amount discharge valve comprising:
The grain mixing device is characterized in that the grain mixing device is connected to the arithmetic and control device so as to start operating at a sequential time difference with respect to the conveyance direction of the conveyor. 2. The grain mixture according to claim 1, further comprising a volumetric weight measuring device for measuring the volumetric weight of each mixed grain so that the rotational speed of each of the variable discharge valves is calculated based on the grain mixing ratio and volumetric weight. Device.
JP59006924A 1984-01-17 1984-01-17 grain mixing equipment Granted JPS60150823A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59006924A JPS60150823A (en) 1984-01-17 1984-01-17 grain mixing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59006924A JPS60150823A (en) 1984-01-17 1984-01-17 grain mixing equipment

Publications (2)

Publication Number Publication Date
JPS60150823A JPS60150823A (en) 1985-08-08
JPH0245494B2 true JPH0245494B2 (en) 1990-10-09

Family

ID=11651790

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59006924A Granted JPS60150823A (en) 1984-01-17 1984-01-17 grain mixing equipment

Country Status (1)

Country Link
JP (1) JPS60150823A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0240230A (en) * 1988-07-27 1990-02-09 Satake Eng Co Ltd Grain mixer
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JPH06198156A (en) * 1993-01-06 1994-07-19 Nagasaki Pref Gov Atomizing and laminating mixer
UA75375C2 (en) * 2000-10-12 2006-04-17 Boehringer Ingelheim Pharma Method for producing powdery preparations for inhaling
US8905266B2 (en) * 2004-06-23 2014-12-09 Ecolab Inc. Method for multiple dosage of liquid products, dosing apparatus and dosing system
US8277745B2 (en) 2007-05-02 2012-10-02 Ecolab Inc. Interchangeable load cell assemblies
US7694589B2 (en) 2007-12-12 2010-04-13 Ecolab Inc. Low and empty product detection using load cell and load cell bracket
US9102509B2 (en) 2009-09-25 2015-08-11 Ecolab Inc. Make-up dispense in a mass based dispensing system

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5124080A (en) * 1974-08-21 1976-02-26 Goshina Sangyo Kinzokusaihenno atsushukuseikeisochi

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JPS60150823A (en) 1985-08-08

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