JPS6086424A - Constant flow rate feeding method using loss-in-weight type feeder - Google Patents

Constant flow rate feeding method using loss-in-weight type feeder

Info

Publication number
JPS6086424A
JPS6086424A JP19455583A JP19455583A JPS6086424A JP S6086424 A JPS6086424 A JP S6086424A JP 19455583 A JP19455583 A JP 19455583A JP 19455583 A JP19455583 A JP 19455583A JP S6086424 A JPS6086424 A JP S6086424A
Authority
JP
Japan
Prior art keywords
feeder
flow rate
loss
raw material
discharging
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
JP19455583A
Other languages
Japanese (ja)
Inventor
Yujiro Kimura
木村 雄二郎
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP19455583A priority Critical patent/JPS6086424A/en
Publication of JPS6086424A publication Critical patent/JPS6086424A/en
Pending legal-status Critical Current

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  • Weight Measurement For Supplying Or Discharging Of Specified Amounts Of Material (AREA)
  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)

Abstract

PURPOSE:To improve the accuracy of feeding of a constant flow rate by using two loss-in-weight type feeders, and at the switching of discharging feeding prescribed starting materials to the feeder side in executing the discharging up to the switching. CONSTITUTION:Discharging is executed by using two loss-in-weight type feeders 1, 2 alternately, and at the switching of discharging the feeder 1 side in executing the discharging up to the switching fades out a flow rate Ft1 and the feeder 2 side starting the logging fades in a flow rate Ft2 to control respective flow rates so that (Ft1+Ft2) gets near an objective flow rate F0. Since the material is fed to the feeder 1 side in executing the discharging after the completion of fade-out, the flow rate is always controlled so as to get near the object flow rate F0 even in the feeding of the material when observed from the feeding side of the material, so that the accuracy of feeding of a constant flow rate can be improved.

Description

【発明の詳細な説明】 本発明はロスインウェイト式フィーダによる定流量供給
方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a constant flow rate supply method using a loss-in weight type feeder.

ロスインウェイト式フィーダは原料貯蔵量の単位時開の
減少重量から実際の切出し流JilFtを算出し、Ft
が目標流m Foに近づくようにフィーダ駆動モータの
運転が制御される。従来では一原料当り1台のロスイン
ウェイト式フィーダで切出しが実行されており、原料貯
蔵量が下限値に達すると原料補給に際して駆動モータを
過去の運転に基づく一定回転数で運転し、原料補給後に
計重値に基づく通常運転に戻して、原料補給中も途切れ
ることがないよう原料が切出されている。
The loss-in weight type feeder calculates the actual cut-out flow JilFt from the reduced weight per unit opening of the raw material storage amount, and calculates Ft
The operation of the feeder drive motor is controlled so that mFo approaches the target flow mFo. Conventionally, one loss-in-weight type feeder is used to feed each raw material, and when the raw material storage amount reaches the lower limit, the drive motor is operated at a constant rotation speed based on past operations to replenish the raw material. Afterwards, normal operation is resumed based on the weighed value, and the raw material is cut out without interruption even during raw material replenishment.

しかしこのような定流量供給方法では原料補給中も切出
しが途切れないものの、原料補給中は非制御状態である
ため、この間は目標流量FOに十分に近づけることは期
待できず、定流量供給の精度を低下させているのが現状
である。
However, with such a constant flow rate supply method, cutting is not interrupted even during raw material replenishment, but since it is in an uncontrolled state during raw material replenishment, it cannot be expected that the target flow rate FO will be sufficiently close to the target flow rate during this time, and the accuracy of constant flow rate supply may be affected. The current situation is that it is decreasing.

本発明は原料補給中の流量を目標流k Foに十分に近
づけることができるロスインウェイト式フィーダによる
定流量供給方法を提供することを目的とする。
An object of the present invention is to provide a constant flow rate supply method using a loss-in-weight type feeder that can bring the flow rate during raw material replenishment sufficiently close to the target flow kFo.

本犯明のロスインウェイト式フィーダによる定流星供給
方法は、第1のフィーダ側の原料貯蔵量が下限値に達す
るまでは第1のフィーダ単独で目標流量F。に近づくよ
うに定流量切出しを実゛行し、第1のフィーダ側の原料
貯M社が下限値に達すると第1のフィーダ流量をフェー
ドアウトすると共に第2のフィーダの流量をフェードイ
ンしてこの時の第1.第2のフィーダの時々の流量をそ
れぞれFtl * Ft2とした場合に(Ft、+Ft
2)が前記目標流量F。
In the constant meteor supply method using a loss-in-weight feeder according to the present invention, the first feeder alone maintains the target flow rate F until the raw material storage amount on the first feeder side reaches the lower limit. When the raw material storage M on the first feeder side reaches the lower limit value, the flow rate of the first feeder is faded out and the flow rate of the second feeder is faded in. Time 1. If the occasional flow rate of the second feeder is Ftl * Ft2, then (Ft, +Ft
2) is the target flow rate F.

に近づくよう制御し、第1のフィーダの前記フェードア
ウト完了後に第1のフィーダ側に原料を補給して、第1
のフィーダへの原料補給の際には第2のフィーダによる
原料切出しを実行することを特徴とする。
After the fade-out of the first feeder is completed, the raw material is supplied to the first feeder side, and the first
The second feeder is used to cut out the raw material when replenishing the raw material to the second feeder.

以下、本発明の具体的な実施例を第1図〜第8図に基づ
いて説明する。
Hereinafter, specific embodiments of the present invention will be described based on FIGS. 1 to 8.

第1図は1つの原料を定流星供給するために使用される
ロスインウェイト式フィーダの機械部分の構成を示す。
FIG. 1 shows the configuration of the mechanical parts of a loss-in-weight type feeder used for constant meteoric feeding of one raw material.

Q) (2)は第1.第2のロスインウェイト式フィー
ダ〔以下、第1.第2のフィーダと称す〕、(3) (
4)はそれぞれ第1.第2のフィーダ(1)(2)への
原料補給に際して[d閉される第1.第2の原料補給バ
ルブ、(5) (6)は第1.第2のフィーダ(1)(
2〕を支持する第1.第2の荷重変換装置、(7) (
8)は第1.第2のフィーダ(1) (2)を駆動する
第1.第2の駆動モータである。
Q) (2) is the first. Second loss-in weight type feeder [hereinafter referred to as the first loss-in weight type feeder] (referred to as the second feeder)], (3) (
4) are respectively 1st. When replenishing raw materials to the second feeders (1) and (2), the first feeder [d] is closed. The second raw material replenishment valve (5) (6) is the first raw material replenishment valve. Second feeder (1) (
2]. Second load conversion device, (7) (
8) is the first. The first feeder that drives the second feeder (1) (2). This is the second drive motor.

運転開始に際して第1.第2のフィーダ(1) (2)
のホッパ(9) (IIには原料が充填されている。先
ず、第1の荷重変換装置(5)の計λ値W1に基づいて
第1のフィーダ(1)が運転され、第2図の区間Aのよ
うに第1のフィーダ(1)の流量〔第2図(a)〕は目
目標流量oに近づき、第2のフィーダ(2)の流量〔第
2図(b)〕は流量「零」の状態で運転される。この区
刑Aにおいて計重値W11第2のフィーダ(2)側の第
2の荷重変換装置(6)の計重値W2は、それぞれ第2
図(d) (e)のように計重値Wlは単位時間当りほ
ぼF。で減少し、計重値W2は上限値W2H一定のまま
で変化しない。
First, when starting operation. Second feeder (1) (2)
Hopper (9) (II is filled with raw material. First, the first feeder (1) is operated based on the total λ value W1 of the first load converter (5), and the As in section A, the flow rate of the first feeder (1) [Fig. 2 (a)] approaches the target flow rate o, and the flow rate of the second feeder (2) [Fig. 2 (b)] approaches the flow rate ' In this ward A, the weighed value W11 and the weighed value W2 of the second load converter (6) on the second feeder (2) side are respectively the second
As shown in Figures (d) and (e), the weighed value Wl is approximately F per unit time. The weight value W2 remains constant at the upper limit value W2H and does not change.

そして、第1のフィーダ(1)による単独の切出しを実
行してホッパ(9)の原料貯蔵量が下限値WILに達し
たことを検出すると、区間Bのように第1のフィーダ(
1)の流星が次第に減少して第2のフィーダ(2)の流
星は次第に増加するように制御され′る。なお、ここで
区間Bにおける第1.第2のフィーダ(1) (2)の
時々の流量をFtl、Ft2とすると、第1.第2のフ
ィーダ(1) (2)のフェードアウト、フェードイン
は(Ft1+Ft2) = Fo に近づくよう制御さ
れており、第2図(C)に示すように総合供給社は区間
Bも区間Aと同様にF。に近づけることができる。
Then, when it is detected that the raw material storage amount in the hopper (9) has reached the lower limit value WIL by performing individual cutting by the first feeder (1), as in section B, the first feeder (
The meteors at the second feeder (2) are controlled so that they gradually decrease and the meteors at the second feeder (2) gradually increase. Note that here, the first. If the occasional flow rates of the second feeders (1) and (2) are Ftl and Ft2, then the first. The fade-out and fade-in of the second feeders (1) and (2) are controlled so that they approach (Ft1+Ft2) = Fo, and as shown in Figure 2 (C), the general supply company has maintained that section B is the same as section A. To F. can be approached.

このようにして区間Bを実行してフェードアウトとフェ
ードインが完了すると、区間Aにおける第1のフィーダ
(1)のように@2のフィーダ(2)は計重値W2に基
づいて目標流量F0に近づ(よう制御され、区間Cにお
いては第2のフィーダ(2)の単独の原料切出しが実行
される。なお、原料貯蔵量が下限値に達した第1のフィ
ーダ(1)への原料補給は、フェードアウトが完了した
後の区間Cにおいて原料補給バルブ(3)に囲放侶号G
1を送って開始され、計重値W1が上限値WIHに達し
た時に原料補給が終−了する。
When the fade-out and fade-in are completed by executing section B in this way, the feeder @2 (2), like the first feeder (1) in section A, reaches the target flow rate F0 based on the weighed value W2. In section C, the second feeder (2) performs independent raw material cutting. In addition, the raw material supply to the first feeder (1) whose raw material storage amount has reached the lower limit value is performed. In section C after the fade-out is completed, the Ihojogo G is connected to the raw material replenishment valve (3).
1 and ends when the weighed value W1 reaches the upper limit value WIH.

第8図は第2図(a) (b)の制御を実行する制御装
監の原理を示す。Ql)(2)は計重値W1* W2の
変化からそれぞれ実際の流量Ft1.Ft2を算出する
流量算出部、の)は目標流量Foと実際の扼九Ft、と
を比較して流量誤差を算出する比較部、0<は回転数決
定手段で、比較部Q4で算出された流量誤差を零に近づ
けるに必要な駆動モータ(7)の回転数を決定してその
回転数に応じたレベルの直流電圧Ev1を出力する。(
ト)は前記直流電圧Kv+ を一定の速度で次第に零に
近づけるフェードアウト手段で、区間Aにおいては入力
された直流電圧EVIをそのまま出力し、下限検出部Q
QがW1=WIL を検出するとフェードアウトを開始
するよう構成されている。αηはフェードアウト手段(
IIを介した直流電圧EVIに応じて駆動モータ(7)
への厖力制御を実行する電力可変制御部である。第2の
フィーダ(2)側にも比較部(2)2回転数決定手段鵠
、電力可変制御部Qηと同様の比較部(至)。
FIG. 8 shows the principle of a control system that executes the control shown in FIGS. 2(a) and 2(b). Ql) (2) is the actual flow rate Ft1. The flow rate calculation unit that calculates Ft2 is a comparison unit that calculates a flow rate error by comparing the target flow rate Fo and the actual Ft, and 0< is a rotation speed determination means that is calculated by the comparison unit Q4. The number of rotations of the drive motor (7) required to bring the flow rate error close to zero is determined, and the DC voltage Ev1 is output at a level corresponding to the number of rotations. (
G) is a fade-out means that gradually approaches zero at a constant speed, and in section A, outputs the input DC voltage EVI as it is, and lower limit detection section Q
When Q detects W1=WIL, it is configured to start fading out. αη is the fade-out means (
Drive motor (7) according to the DC voltage EVI via II
This is a power variable control unit that executes power control to the Also on the second feeder (2) side, there is a comparison section (2) similar to the rotation speed determining means and the power variable control section Qη.

回転数決定手段(11,電力可変制御部−が設ζ)られ
ており、比較部(至)はg鼻部(2)で算出された(F
ll−F(1)と流量Ftz とを比較して区間Bの駆
動モータ(8)のフェードイン制御を実行している。
A rotation speed determining means (11, power variable control section - is installed), and a comparison section (to) is calculated by the g nose section (2) (F
Fade-in control of the drive motor (8) in section B is performed by comparing ll-F (1) with the flow rate Ftz.

上記実施例ではilのフィーダ(1)の原料補給の場合
について説明したが、区間Cを実行して第2のフィーダ
(2)の原料貯蔵量が下限値W2Lに達した場合には、
第2のフィーダ(2月こよる切出し量をフェードアウト
して第1のフィーダ(1)の切出し社をフェードインし
て、第2のフィーダ(2)のフェードアウト完了後に第
2のフィーダ(2)への原料補給が実行される。このよ
うに第1.第2のフィーダ(1)(2)でフェードアウ
トとフェードインを交互に実行するに必要な具体的な制
御装置は、区間A、Bは第8図構成で駆動モータ(7)
 (8)を制御し、流量算出部αυに計重値W2を人力
して流量算出部(2)に計重値W1を人力し、電力可変
制御部(Iηで駆動モータ(8)を制御して電力可変制
御部−で駆動モータ(7)を制御するように、以下、同
様に入れ換えることによって容易に実現できる。
In the above embodiment, the case of replenishing raw material to the feeder (1) of il was explained, but when the raw material storage amount of the second feeder (2) reaches the lower limit value W2L by executing section C,
Fade out the amount of cut from the second feeder (February), fade in the cut amount of the first feeder (1), and then switch to the second feeder (2) after completing the fade out of the second feeder (2). The specific control device required to alternately perform fade-out and fade-in in the first and second feeders (1) and (2) is as follows: Drive motor (7) with 8 diagram configuration
(8), manually inputs the weight value W2 to the flow rate calculation unit αυ, inputs the weight value W1 to the flow rate calculation unit (2), and controls the drive motor (8) with the power variable control unit (Iη). This can be easily realized by replacing the drive motor (7) with the power variable control section in the same manner.

また、上記各実施例では一方のフェードアウトに追従し
て他方p流電をフェードインさせたが、これは区11B
において@2のフィーダ(2)の切出し流量Ft2一定
の傾きでフェードインさせて第1のフィーダ(1)の切
出し流In FtlをFt2に追従してフェードアウト
するように構成しても同様の効果が得られる。
Furthermore, in each of the above embodiments, the fade-out of one side was followed by the fade-in of the other p current;
The same effect can be obtained by configuring that the cut-out flow rate Ft2 of the feeder (2) @2 is faded in at a constant slope, and the cut-out flow In Ftl of the first feeder (1) is faded out following Ft2. can get.

以上説明のように本発明の定fAL量供給方法によると
、二台のロスインウェイト式フィーダを用意して交互に
切出しを実行すると共にその切換え時点においてはそれ
まで切出しを実行していたフィーダ側は1+i+ m 
Ftl をフェードアウトし、次に切出しを9:」始す
るフィーダ側では流m Ft2 をフェードインして(
Ft、十Ft2)が目標流量F。に近づくように制御し
、フェードアウト完了後にそれまで切出しを実行してい
たフィーダ側に原料を補給するため、原料が供給される
側から見れば原料補給中であっても目Ki m m F
。に近つくように常に制御かかけられでおり、長ル」間
にわたって常職高精度の定流九倶給を期待できるもので
ある。
As explained above, according to the constant fAL amount supply method of the present invention, two loss-in weight type feeders are prepared and cutting is performed alternately, and at the time of switching, the feeder that has been performing cutting until then is is 1+i+m
Ftl is faded out, and then cutting is started at 9. On the feeder side, flow m Ft2 is faded in (
Ft, 10Ft2) is the target flow rate F. After fade-out is completed, the raw material is supplied to the feeder side that had been performing cutting until then, so that from the perspective of the side where the raw material is supplied, even when the raw material is being replenished, the
. It is constantly controlled so that it approaches the same, and you can expect constant flow with high precision for long periods of time.

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

口面は本究明の定流量供給方法の具体的な実施例を示し
、第1図は機械部分の構成図、第2図(a)〜(e)は
供給実行中の第1図の要部波形図、第8図は制都装はの
基本構成図である。 (1) (2)・・・第1.叱2のロスインウェイト式
フィーダ、(5) (6)−・・第1.第2の荷重反換
装置、(7) (8)・・・第′ 1.第2の駆動モー
タ、(9) 60 ”・・ホッパ、a$m−・・比較部
、α401・・・回転数決定手段、(へ)・・・ヅエー
ドアウト手段、(Iす・・・下限検出部、θη0ト・・
電力可変制御部、C21J・・・減算部、Fo・・・目
標流社代理人森本義弘 第1図 第2図
The front side shows a specific example of the constant flow supply method of this research, Fig. 1 is a configuration diagram of the mechanical part, and Figs. 2 (a) to (e) show the main parts of Fig. 1 during supply execution. The waveform diagram and FIG. 8 are the basic configuration diagrams of the metropolitan equipment. (1) (2)...First. Loss-in weight type feeder of No. 2, (5) (6) --- 1st. Second load reversing device, (7) (8)...'1. 2nd drive motor, (9) 60"...hopper, a$m-...comparison section, α401...rotation speed determining means, (to)...due-out means, (Isu...lower limit detection part, θη0t...
Power variable control section, C21J... Subtraction section, Fo... Target flow company agent Yoshihiro Morimoto Figure 1 Figure 2

Claims (1)

【特許請求の範囲】[Claims] 1、第1のフィーダ側の原料貯蔵量が下限値に達するま
では第1のフィーダ単独で目標流ji Fo〜に近づく
ように定流量切出しを実行し、第1のフィーダ側の原料
貯蔵量が下限値に達すると第1のフィーダ流量をフェー
ドアウトすると共に第2のフィーダのThh量をフェー
ドインしてこの時の第1.第2のフィーダの時々の流量
をそれぞれ)’tl+Ft2 とした場合に(Ft、 
+ Ft、)が前記目標流fn Foに近づくよう制卸
し、第1のフィーダの前記フェードアウト完了後に第1
のフィーダ側に原料を補給するロスインウェイト式フィ
ーダによる定流量供給方法。
1. Until the raw material storage amount on the first feeder side reaches the lower limit, the first feeder alone performs constant flow cutting so as to approach the target flow ji Fo~, and the raw material storage amount on the first feeder side When the lower limit is reached, the flow rate of the first feeder is faded out, and the Thh amount of the second feeder is faded in, so that the flow rate of the first feeder at this time is faded out. If the occasional flow rate of the second feeder is respectively)'tl+Ft2, then (Ft,
+ Ft,) is controlled so that it approaches the target flow fn Fo, and after the fade-out of the first feeder is completed, the first feeder
A constant flow supply method using a loss-in weight type feeder that replenishes raw materials to the feeder side.
JP19455583A 1983-10-18 1983-10-18 Constant flow rate feeding method using loss-in-weight type feeder Pending JPS6086424A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19455583A JPS6086424A (en) 1983-10-18 1983-10-18 Constant flow rate feeding method using loss-in-weight type feeder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19455583A JPS6086424A (en) 1983-10-18 1983-10-18 Constant flow rate feeding method using loss-in-weight type feeder

Publications (1)

Publication Number Publication Date
JPS6086424A true JPS6086424A (en) 1985-05-16

Family

ID=16326473

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19455583A Pending JPS6086424A (en) 1983-10-18 1983-10-18 Constant flow rate feeding method using loss-in-weight type feeder

Country Status (1)

Country Link
JP (1) JPS6086424A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998042786A3 (en) * 1997-03-24 1999-03-04 Cabot Corp Chemical mixing or reacting zone with controlled fluid through-flow
JP2015178658A (en) * 2014-03-19 2015-10-08 Jfeスチール株式会社 Method of continuously feeding auxiliary feedstock in revolving furnace auxiliary feedstock feeding equipment

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57108717A (en) * 1980-12-26 1982-07-06 Nisshin Flour Milling Co Ltd Continuous type flowmeter and constant volume supply device for liquid

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57108717A (en) * 1980-12-26 1982-07-06 Nisshin Flour Milling Co Ltd Continuous type flowmeter and constant volume supply device for liquid

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998042786A3 (en) * 1997-03-24 1999-03-04 Cabot Corp Chemical mixing or reacting zone with controlled fluid through-flow
US6399029B1 (en) 1997-03-24 2002-06-04 Cabot Corporation Chemical processing using a dual feeder system, a sample port assembly, and a fluid flow control system
JP2015178658A (en) * 2014-03-19 2015-10-08 Jfeスチール株式会社 Method of continuously feeding auxiliary feedstock in revolving furnace auxiliary feedstock feeding equipment

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