JPH03187897A - Saccharide rate quality controller - Google Patents
Saccharide rate quality controllerInfo
- Publication number
- JPH03187897A JPH03187897A JP32600689A JP32600689A JPH03187897A JP H03187897 A JPH03187897 A JP H03187897A JP 32600689 A JP32600689 A JP 32600689A JP 32600689 A JP32600689 A JP 32600689A JP H03187897 A JPH03187897 A JP H03187897A
- Authority
- JP
- Japan
- Prior art keywords
- stock solution
- amount
- stock
- sugar content
- head
- 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
Links
- 150000001720 carbohydrates Chemical class 0.000 title abstract 5
- 239000011550 stock solution Substances 0.000 claims description 88
- 238000003908 quality control method Methods 0.000 claims description 6
- 238000006073 displacement reaction Methods 0.000 claims description 5
- 238000005259 measurement Methods 0.000 claims description 4
- 238000002347 injection Methods 0.000 description 10
- 239000007924 injection Substances 0.000 description 10
- 235000013361 beverage Nutrition 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 230000007423 decrease Effects 0.000 description 5
- 230000004913 activation Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 3
- 229930006000 Sucrose Natural products 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 239000005720 sucrose Substances 0.000 description 3
- 238000001514 detection method Methods 0.000 description 2
- 238000005429 filling process Methods 0.000 description 2
- 238000005303 weighing Methods 0.000 description 2
- 230000001133 acceleration Effects 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 235000019527 sweetened beverage Nutrition 0.000 description 1
Landscapes
- Filling Of Jars Or Cans And Processes For Cleaning And Sealing Jars (AREA)
Abstract
Description
(産業上の利用分野)
本発明は食品機械の充填機に通用される糖度品質管理装
置に関するものである。
(従来の技術)
容器に所定量の飲料を充填する充填機の充填方法には、
通常法の2通りがある。
(1)飲料を構成する炭酸水と高糖度の原液を所定の割
合で混合し、所定の糖度に合せた液を予めタンクに貯蔵
し、充填機はその混合液を規定量だけ容器に充填する。
(2)炭酸水と原液は別々のタンクに貯蔵され、最初の
充填過程では、容器に規定量の炭酸水が充填され、次の
充填過程では、規定量の原液が充填され、後工程で撹拌
されて容器に所定の糖度の飲料を充填する。なお、この
場合炭酸水と原液の充填順序が逆になることもある。
第2図は最初の充填工程で規定量の炭酸水を充填された
容器が搬送されて、次の充填工程で原液が充填される従
来装置の概略構成を示す。
第2図において原液タンクlには、高糖度の原液が貯蔵
されている。原液は投入バルブ2により計量カップ3に
補給される。計量カップ:3は支持台4で支えられ、支
持台4の変位星をロードセル5で検出して変位検出信号
が計量制御器6に入力されて、計量力ノブ3の風袋を含
めた全重量が計測される。また7は排出バルブで、計量
カップ3から原液を容器8に充填するものであり、投入
バルブ2、排出バルブ7の開閉制御は計量制御器6によ
り行われる。第2図の一点鎖線部分は、同時に充填する
容器数だけ装備されており、計量制御器6は投入バルブ
2、排出バルブ7の開閉信号ライン及びロードセル5の
検出信号ラインの多重化により、1台或は数台で全容器
の充填制御を行う。
第3図は計量制御器6の1つの容器に対する充填毎の制
御シーケンス図を示す。さて第3図に示す如く計量制御
236は、投入バルブ2に開指令を出力し、前回充填で
減った分の原液を旧量カンプ3に補充する。所定量の原
液が計量カップ3に補充されると、計量制御器6は投入
ノ\ルブ2に閉指令を出力する。−また計量制御器6は
、d量値が落ち着(までの時間経過後投入計量値を取得
し、次に排出バルブ7に開指令を出力する。所定量の原
液が注入管9を通って容器8に充填されると、計量制御
器6は排出)\ルブ7に閉指令を出力する。この計量制
御器6は計量値が落ち着くまでの時間経過後、U[出計
星値を取得する。
以上の制御シーケンスが容器の充填毎に繰り返されるが
、その同期信号は、容器の搬送ンーケンス制御システム
から入力される。計量制御器6は1台で多数の容器の充
填制御を行う。計量制御器6の投入量設定値、排出量設
定値は外部より入力される。
(発明が解決しようとする課題)
製品飲料の糖度を規定値に保つためには、容器内の規定
量の炭酸水に対して規定量の原液を投入する必要がある
。規定量の原液は、計量制御器6により計量されて投入
されるが、この時に次のような問題があった。
(1)計量制御器6は、排出バルブ7による原液排出量
が排出量設定値に達したときに、排出バルブ7に閉指令
を出すが、排出バルブ7の作動遅れ時間により、排出計
量値は排出量設定値より大きくなる。この差を落差量、
(−排出計量値−排出設定値)というが、この落差量は
製品飲料の糖度を規定値より大きくする原因になる。
(2)そしてこの落差量は次式で計算される。
落差量(g)=注入管内の原液重量速度(g/5ec)
×作動遅れ時間(s e c ) −−−
−−−(1)一般に排出バルブ7の作動遅れ時間は一定
であるが、計量カップ3の原液レヘルがほぼ一定とすれ
ば、注入管内の原液流速は、原液粘度により変化するの
で、原液の#I?!度及び温度により変化する。従って
原液の品種、温度により落差量は変化するので、このこ
とも製品飲料の糖度を変動させる原因になる。
以上述べたことから、容器に規定量の原液を充填するた
めには、次の2項のことが必要である。
(1)落差量を正確に予測すること。
(2)計量制御器6の排出量設定値を次式で定めること
。
排出量設定値−原液規定量−落差量 −(2)ここで原
液規定量とは、容器内の規定炭酸y’gに対して規定糖
度になるのに必要な原ン夜充填量である。
本発明は前記従来の課題を解決するために(足案された
ものである。
(課題を解決するための手段)
このため本発明は、原液を貯蔵する原ン夜タンクと、同
原液タンクの原液を計量力・ノブGこ)111充する投
入バルブと、同計量カップを保持する支持台と、同支持
台の変位量を検出するロート′セルと、前記計量カップ
からの原液を容器に充填する排出バルブと、前記ロード
セルから前記計量カップの風袋を含めた全重量の計測信
号を受けて前記投入バルブと排出バルブの開閉制御を行
う計量制御器とからなる充填機において、前記計量カッ
プ中の原液の糖度を検出する糖度検出器と、同計量カッ
プ中の原液の温度を検出する温度検出器と、前記糖度検
出器と温度検出器の出力を人力して落差量を出力する落
差量算出器と、同糖度検出器の出力を入力して原液規定
量の補正値を出力する原液規定に補正器と、前記計量制
御器からの原液規定量と前記原液規定量補正器からの出
力を加算して補正原液規定量を算出する加算器と、同加
算器の出力と前記落差(1(算出器の出力を人力して両
者の差(補正原液規定量−落差量)を排出量設定値とし
て前記計量制御器に出力する減算器とからなるもので、
これを課題解決のための手段とするものである。
(作用)
一般に甘味飲料の原液の動粘度特性とは、蔗糖水溶液の
動粘度で近似できる。第4図は蔗糖水溶液の動粘度特性
を表わす。なお、原液温度の上昇と共に、動粘度は下が
り、糖度の上界と共に粘度は上昇する。
また原液充填時の規定条件を次のように定める。
原液温度T:10’C
原液糖度B:57゜
注入管内径d:11m1II
充填重量速度W : 60g/sec
なお、説明の都合上、配管曲がりや排出バルブでの圧力
損失を含めた等傷内な長さし、で注入管長さを代表させ
、始めに前記条件より等傷長さR8を求める。
原液の動粘度νは
ν= 54 X 10−2cffl/sec原液の比重
量Tは
r = 1.273g/ad
管内流速Uは
u = W/ (−d2r ) = 49.60cm/
secレイノルズ数R,,は
なお、R8の大きさより注入管内の流れは層流と考えら
れ、圧力損失ΔPは次式で与えられる。
ここにf−摩擦係数
g−重力加速度
[は層流であるので、次式で与えられる。
(3) (4)式より次式が成立つ。
また排出バルブの作動遅れ時間Δ(Field of Industrial Application) The present invention relates to a sugar content quality control device commonly used in filling machines of food machinery. (Prior art) The filling method of a filling machine that fills a container with a predetermined amount of beverage includes:
There are two normal methods. (1) The carbonated water and high sugar content stock solution that make up the beverage are mixed at a predetermined ratio, the liquid adjusted to the predetermined sugar content is stored in a tank in advance, and the filling machine fills the specified amount of the mixed solution into the container. . (2) Carbonated water and stock solution are stored in separate tanks; in the first filling process, a specified amount of carbonated water is filled into the container, and in the next filling process, a specified amount of stock solution is filled into the container, which is then stirred in the subsequent process. The container is then filled with a beverage having a predetermined sugar content. In this case, the filling order of carbonated water and stock solution may be reversed. FIG. 2 shows a schematic configuration of a conventional apparatus in which a container filled with a specified amount of carbonated water is transported in the first filling step, and then filled with stock solution in the next filling step. In FIG. 2, a stock solution tank 1 stores a stock solution with a high sugar content. The stock solution is supplied to the measuring cup 3 by the input valve 2. The measuring cup 3 is supported by a support stand 4, the displacement star of the support stand 4 is detected by the load cell 5, the displacement detection signal is input to the weighing controller 6, and the total weight including the tare of the measuring force knob 3 is calculated. be measured. Reference numeral 7 denotes a discharge valve, which is used to fill the container 8 with the stock solution from the measuring cup 3. Opening and closing of the input valve 2 and the discharge valve 7 are controlled by the metering controller 6. The dot-dash line in FIG. 2 is equipped with the same number of containers as the number of containers to be filled at the same time, and one metering controller 6 is constructed by multiplexing the opening/closing signal lines of the input valve 2, the discharge valve 7, and the detection signal line of the load cell 5. Alternatively, several units can control the filling of all containers. FIG. 3 shows a control sequence diagram of the metering controller 6 for each filling of one container. Now, as shown in FIG. 3, the metering control 236 outputs an opening command to the input valve 2, and replenishes the old volume comp 3 with the stock solution that was reduced in the previous filling. When the measuring cup 3 is replenished with a predetermined amount of stock solution, the metering controller 6 outputs a close command to the input knob 2. -Also, the metering controller 6 acquires the input metering value after the time has elapsed until the amount d has settled down, and then outputs an opening command to the discharge valve 7. A predetermined amount of stock solution passes through the injection pipe 9 When the container 8 is filled, the metering controller 6 outputs a close command to the discharge valve 7. The metering controller 6 acquires the U [output star value] after a period of time has elapsed until the metering value has stabilized. The above control sequence is repeated every time a container is filled, and the synchronization signal is input from the container conveyance sequence control system. One metering controller 6 controls the filling of a large number of containers. The input amount set value and the discharge amount set value of the metering controller 6 are inputted from the outside. (Problems to be Solved by the Invention) In order to maintain the sugar content of a product beverage at a specified value, it is necessary to add a specified amount of stock solution to a specified amount of carbonated water in a container. A prescribed amount of the stock solution is metered and dispensed by the metering controller 6, but the following problem occurs at this time. (1) The metering controller 6 issues a close command to the discharge valve 7 when the amount of raw liquid discharged by the discharge valve 7 reaches the discharge amount setting value, but due to the operation delay time of the discharge valve 7, the discharge measurement value does not change. The emission amount will be greater than the set value. This difference is the head amount,
(−discharge measured value−discharge set value), but this head difference causes the sugar content of the product beverage to be higher than the specified value. (2) This amount of head difference is calculated using the following formula. Head amount (g) = Stock solution weight velocity in injection tube (g/5ec)
×Activation delay time (sec) ---
--- (1) In general, the activation delay time of the discharge valve 7 is constant, but if the level of the stock solution in the measuring cup 3 is approximately constant, the flow rate of the stock solution in the injection pipe changes depending on the viscosity of the stock solution, so the ## of the stock solution is I? ! Varies depending on degree and temperature. Therefore, since the amount of head changes depending on the type and temperature of the stock solution, this also causes fluctuations in the sugar content of the product beverage. From the above, in order to fill a container with a specified amount of stock solution, the following two items are necessary. (1) Accurately predict the amount of head. (2) Determine the discharge amount setting value of the metering controller 6 using the following formula. Discharge amount set value - Specified amount of stock solution - Head amount - (2) Here, the specified amount of stock solution is the amount of stock solution that is required to reach the specified sugar content with respect to the specified amount of carbonic acid y'g in the container. The present invention has been devised in order to solve the above-mentioned conventional problems. An injection valve for filling the stock solution with measuring force/knob G)111, a support stand for holding the measuring cup, a funnel' cell for detecting the displacement of the support stand, and a container filled with the stock liquid from the measuring cup. In the filling machine, the filling machine includes a discharge valve that controls the amount of water in the measuring cup, and a weighing controller that receives a measurement signal of the total weight including the tare of the measuring cup from the load cell and controls the opening and closing of the input valve and the discharge valve. A sugar content detector that detects the sugar content of the stock solution, a temperature detector that detects the temperature of the stock solution in the same measuring cup, and a head amount calculator that manually outputs the amount of head difference by manually inputting the outputs of the sugar content detector and temperature detector. Then, input the output of the same sugar content detector and output the corrected value of the specified amount of stock solution with a corrector, and add the specified amount of stock solution from the metering controller and the output from the specified amount of stock solution corrector. an adder that calculates the corrected specified amount of stock solution, and an adder that calculates the output of the adder and the head difference (1) manually, and calculates the difference between the two (corrected specified amount of stock solution - head amount) as the discharge amount setting value. It consists of a subtracter that outputs to the metering controller.
This is a means to solve problems. (Function) In general, the kinematic viscosity characteristics of a sweetened beverage stock solution can be approximated by the kinematic viscosity of a sucrose aqueous solution. FIG. 4 shows the kinematic viscosity characteristics of a sucrose aqueous solution. Note that as the temperature of the stock solution increases, the kinematic viscosity decreases, and as the upper limit of the sugar content increases, the viscosity increases. In addition, the specified conditions for filling the stock solution are determined as follows. Stock solution temperature T: 10'C Stock solution sugar content B: 57° Injection pipe inner diameter d: 11m1II Filling weight speed W: 60g/sec For the sake of explanation, we have not included any damage in the pipe, including bends in the piping and pressure loss at the discharge valve. Let the length be representative of the length of the injection tube, and first find the equal flaw length R8 from the above conditions. The kinematic viscosity ν of the stock solution is ν = 54 x 10-2 cffl/sec The specific weight T of the stock solution is r = 1.273 g/ad The flow rate U in the pipe is u = W/ (-d2r) = 49.60 cm/
The flow in the injection pipe is considered to be laminar due to the size of R8, and the pressure loss ΔP is given by the following equation. Here, f-friction coefficient g-gravitational acceleration [is a laminar flow, so it is given by the following equation. (3) From equation (4), the following equation holds true. Also, the discharge valve operation delay time Δ
【を0.2秒とすると
、(+)式より′落差量ΔWは
ΔW=WXΔt=60X0.2=12g −−−
−−−(5)次に原液温度が15°Cに上昇したときの
落差量の変化を求める。
このときの原液動粘度νは、
シ=39.5X10−2cffl/sec比重量Tは
r =1.271g/cIl!である。
またこのときの注入管流速Uは、(3)(4)式より次
のように求められる。
落差量ΔWは
上式よりR8は
L e ”” 108.7cm
(5) (8)式より原液温度5°Cの上昇で、落差量
は4.4g増加することが分る。
次に原液糖度が2°減少した時の落差量の変化を求める
。
このときの原液動粘度νは
ν= 40 X 10− ”c艷/sec比重量γは
r =1.2623g/c−である。
またこの時の流速Uは(6)弐より求められる。
落差量ΔWは(7)式より求められる。
67.52X0.2=16.20g −−一
・−(9)(5)(9)式より分るように原液糖度2°
の低下で落差量は4.2g増加する。
また原液糖度が変化した場合は、原液規定量Sも変化す
る。原液の規定糖度B。での原液規定量をS。とすると
、原液糖度がΔBだけ変化した時の原液規定量の変化量
ΔSは次式で与えられる。
従ってこの時は、予め充填される原液の規定量もΔBだ
け増減させる必要がある。即ち、糖度の減少した時は原
液規定量がΔBだけ増加するので、原液はΔBだけ減ら
して充填する必要がある。
なお、以上の検討では、排出バルブ7の作動遅れ時間は
0.2秒としたが、実瞭には弁の作動時間による遅れや
弁操作部の遅れなどのため正確に予測することは難しい
が、(1)式を使うことにより作動遅れ時間Δtを推定
することができる。即ち、落差量ΔWは排出量実測値と
排出量設定値の差として算出される。
一方原液の温度と糖度が与えられると、原液の動粘度ν
と比重量γが定まるので、(6)式より注入管での流速
Uが推定される。また(1)式より排出バルブの作動遅
れ時間Δ【は次式より算出できる。
ΔW
Δt = −−−−
−−−−(If)γ−d”u
この作動遅れ時間Δtは原液の温度や糖度で殆ど変わら
ないので、以上述べたことから原液の温度と糖度が与え
られれば、次の手順で落差量を正確に予測し、更に排出
量設定値を求めて製品飲料の糖度の品質を管理できる。
(])原液の温度と糖度を入力する。
(2) (6)式より注入管での原液流速Uを算出す
る。
(3) (7)式より落差量を算出する。
(4)原液糖度が変化した場合は、原液規定量Sを00
式によって補正する。
(5) (2)式より排出量設定値を定める。
(実施例)
以下本発明を図面の実施例について説明すると、第5図
は本発明の実施例における糖度品質管理装置20と、第
2図の従来装置との関係を示し、第1図は前記糖度晶質
管理装置の詳細構成を示す。
糖度品質管理装置20は、計量カップ3の糖度と温度を
検出して入力し、計量制御装置6より原液規定量を入力
して計量制御装置6に排出量設定値を出力する。
第1図で計量カップ3の原液の糖度を糖度検出器10で
検出し、原液の温度を温度検出器11で検出する。糖度
検出器10の出力と温度検出器】1の出力は落差量算出
器12に入力され、落差量算出器12は原液の糖度と温
度より内蔵テーブルにより原液動粘度と比重量を定め、
(6)(7)式より落差量を求める。また糖度検出器1
0の出力は、原液規定量補正器13に入力され、00式
より原液規定量の補正値を算出する。
加算器14は、計量制御器6から人力される原液規定量
と、原液規定量補正器13の出力を加算して補正原液規
定量を算出する。減算器15は、加算器I4の出力と落
差量算出器I2の出力を入力し、(補正原液規定量−落
差量)即ち、排出バルブ7の排出量設定値を出力する。
また落差量算出器12は、原液の糖度及び温度が変化し
た時の落差量を算出する。補正器13は原液糖度が変化
した時の原液規定量の補正量を算出する。更に加算器1
4は、排出バルブ7が充填すべき原液規定量を算出する
。減算器15は原液の糖度及び温度が変わっても、製品
飲料の糖度を規定値に保持するために必要な排出バルブ
の排出量設定値を算出する。
(発明の効果)
以上詳細に説明した如く本発明は構成されているので、
原液の糖度及び温度が変化しても、落差量を正確に予測
して排出バルブの排出量設定値を正確に与えることによ
り、常に正しい排出量規定値を容器に充填でき、これに
より製品飲料の糖度を規定値に保つことができる。If [ is 0.2 seconds, then from formula (+), the head difference ΔW is ΔW=WXΔt=60X0.2=12g ---
--- (5) Next, find the change in head when the temperature of the stock solution rises to 15°C. At this time, the kinematic viscosity of the stock solution ν is: C = 39.5 x 10-2 cffl/sec, and the specific weight T is r = 1.271 g/cIl! It is. In addition, the injection tube flow velocity U at this time is determined from equations (3) and (4) as follows. From the above equation, the head amount ΔW is 108.7 cm for R8. (5) From the equation (8), it can be seen that the head amount increases by 4.4 g when the stock solution temperature increases by 5°C. Next, find the change in head when the sugar content of the stock solution decreases by 2°. At this time, the kinematic viscosity ν of the stock solution is ν = 40 x 10- ”c/sec, and the specific weight γ is r = 1.2623 g/c-. The flow velocity U at this time is obtained from (6) 2. Head The amount ΔW is obtained from the formula (7). 67.52X0.2=16.20g −−1・−(9)(5) As can be seen from the formula (9), the sugar content of the stock solution is 2°
The head amount increases by 4.2g due to the decrease in . Further, when the sugar content of the stock solution changes, the prescribed amount S of the stock solution also changes. Normal sugar content of stock solution B. The specified amount of stock solution is S. Then, when the sugar content of the stock solution changes by ΔB, the amount of change ΔS in the specified amount of stock solution is given by the following equation. Therefore, at this time, it is necessary to increase or decrease the specified amount of stock solution filled in advance by ΔB. That is, when the sugar content decreases, the specified amount of stock solution increases by ΔB, so it is necessary to reduce the stock solution by ΔB and fill it. In the above study, the activation delay time of the discharge valve 7 was assumed to be 0.2 seconds, but it is difficult to predict accurately due to the delay due to the valve activation time and the delay in the valve operating section. , (1) can be used to estimate the actuation delay time Δt. That is, the amount of head difference ΔW is calculated as the difference between the actual measured value of the discharge amount and the set value of the discharge amount. On the other hand, given the temperature and sugar content of the stock solution, the kinematic viscosity of the stock solution ν
Since the specific weight γ is determined, the flow velocity U in the injection pipe can be estimated from equation (6). Further, from equation (1), the discharge valve operation delay time Δ[ can be calculated from the following equation. ΔW Δt = −−−−
−−−−(If)γ−d”u This operation delay time Δt hardly changes depending on the temperature and sugar content of the stock solution, so from the above, if the temperature and sugar content of the stock solution are given, the head difference can be calculated using the following procedure. It is possible to control the quality of the sugar content of the product beverage by accurately predicting the discharge amount and determining the discharge amount setting value. (]) Input the temperature and sugar content of the stock solution. (2) From equation (6), calculate the flow rate of the stock solution in the injection pipe. Calculate U. (3) Calculate the head amount from formula (7). (4) If the sugar content of the stock solution changes, set the specified amount of stock solution S to 00.
Correct by the formula. (5) Determine the emission amount setting value from equation (2). (Example) The present invention will be described below with reference to the embodiments shown in the drawings. FIG. 5 shows the relationship between the sugar content quality control device 20 in the embodiment of the present invention and the conventional device shown in FIG. 2, and FIG. The detailed configuration of the sugar content crystalline control device is shown. The sugar content quality control device 20 detects and inputs the sugar content and temperature of the measuring cup 3, inputs the prescribed amount of stock solution from the metering control device 6, and outputs a discharge amount set value to the metering control device 6. In FIG. 1, the sugar content of the stock solution in the measuring cup 3 is detected by a sugar content detector 10, and the temperature of the stock solution is detected by a temperature detector 11. [Output of sugar content detector 10 and temperature sensor] The output of 1 is input to the head calculator 12, which determines the kinematic viscosity and specific weight of the stock solution from the sugar content and temperature of the stock solution using a built-in table.
Find the amount of head from equations (6) and (7). Also, sugar content detector 1
The output of 0 is input to the stock solution specified amount corrector 13, and a correction value for the stock solution specified amount is calculated from the formula 00. The adder 14 adds the specified amount of undiluted solution manually input from the metering controller 6 and the output of the specified undiluted solution amount corrector 13 to calculate a corrected specified amount of undiluted solution. The subtracter 15 inputs the output of the adder I4 and the output of the head amount calculator I2, and outputs (corrected stock solution specified amount - head amount), that is, the discharge amount setting value of the discharge valve 7. Further, the head amount calculator 12 calculates the head amount when the sugar content and temperature of the stock solution change. The corrector 13 calculates a correction amount for the prescribed amount of the stock solution when the sugar content of the stock solution changes. Furthermore adder 1
4 calculates the specified amount of stock solution that the discharge valve 7 should be filled with. The subtractor 15 calculates the discharge amount setting value of the discharge valve necessary to maintain the sugar content of the product beverage at a specified value even if the sugar content and temperature of the stock solution change. (Effects of the Invention) Since the present invention is configured as explained in detail above,
Even if the sugar content and temperature of the stock solution change, by accurately predicting the head and giving the discharge valve setting value accurately, it is possible to always fill the container with the correct discharge volume specification value, which allows the product beverage to be Sugar content can be maintained at the specified value.
第1図は本発明の実施例を示す糖度品質管理装置のフロ
ーシート、第2図は従来の充填機のフローシート、第3
図は充填機の充填シーケンス図、第4図は蔗糖水溶液の
動粘度特性線図、第5図は本発明の糖度品質管理装置と
従来の充填機との関係を示すフローシートである。
図の主要部分の説明
1−原液タンク 2−投入ハルブ
特
3−計量カップ
5・−・ロードセル
7−排出バルブ
1〇−糖度検出器
12−一落差量検出器
14−加算器
許
出
願
人
支持台
計量制御器
容器
温度検出器
原液規定量補正器
減算器
三菱重工業株式会社
第2図
JPJj図
1、原、i夜、タンク
第3図
第5図Figure 1 is a flow sheet for a sugar content quality control device showing an embodiment of the present invention, Figure 2 is a flow sheet for a conventional filling machine, and Figure 3 is a flow sheet for a conventional filling machine.
The figure is a filling sequence diagram of a filling machine, FIG. 4 is a kinematic viscosity characteristic diagram of a sucrose aqueous solution, and FIG. 5 is a flow sheet showing the relationship between the sugar content quality control device of the present invention and a conventional filling machine. Explanation of the main parts of the diagram 1 - Stock solution tank 2 - Input valve 3 - Measuring cup 5 - Load cell 7 - Discharge valve 10 - Sugar content detector 12 - Head difference detector 14 - Adder support stand Metering controller Container temperature sensor Stock solution specified amount corrector Subtractor Mitsubishi Heavy Industries, Ltd. Figure 2 JPJj Figure 1, original, i night, tank Figure 3 Figure 5
Claims (1)
量カップに補充する投入バルブと、同計量カップを保持
する支持台と、同支持台の変位量を検出するロードセル
と、前記計量カップからの原液を容器に充填する排出バ
ルブと、前記ロードセルから前記計量カップの風袋を含
めた全重量の計測信号を受けて前記投入バルブと排出バ
ルブの開閉制御を行う計量制御器とからなる充填機にお
いて、前記計量カップ中の原液の糖度を検出する糖度検
出器と、同計量カップ中の原液の温度を検出する温度検
出器と、前記糖度検出器と温度検出器の出力を入力して
落差量を出力する落差量算出器と、同糖度検出器の出力
を入力して原液規定量の補正値を出力する原液規定量補
正器と、前記計量制御器からの原液規定量と前記原液規
定量補正器からの出力を加算して補正原液規定量を算出
する加算器と、同加算器の出力と前記落差量算出器の出
力を入力して両者の差(補正原液規定量−落差量)を排
出量設定値として前記計量制御器に出力する減算器とか
らなることを特徴とする糖度品質管理装置。A stock solution tank for storing the stock solution, a charging valve for replenishing the stock solution from the stock solution tank into a measuring cup, a support stand for holding the measurement cup, a load cell for detecting the displacement of the support stand, and a load cell for detecting the displacement of the support stand; A filling machine comprising a discharge valve for filling a container with a stock solution, and a metering controller that receives a measurement signal of the total weight of the measuring cup including a tare from the load cell and controls the opening and closing of the input valve and the discharge valve, A sugar content detector that detects the sugar content of the stock solution in the measuring cup, a temperature detector that detects the temperature of the stock solution in the measuring cup, and the output of the sugar content detector and temperature sensor are inputted to output the amount of head difference. a head amount calculator that inputs the output of the sugar content detector and outputs a correction value for the specified amount of stock solution; An adder that calculates the corrected specified amount of stock solution by adding the outputs of , and an adder that inputs the output of the adder and the output of the head amount calculator and sets the discharge amount by the difference between the two (corrected specified amount of stock solution - head amount) A sugar content quality control device comprising: a subtractor that outputs a value to the metering controller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP32600689A JPH03187897A (en) | 1989-12-18 | 1989-12-18 | Saccharide rate quality controller |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP32600689A JPH03187897A (en) | 1989-12-18 | 1989-12-18 | Saccharide rate quality controller |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH03187897A true JPH03187897A (en) | 1991-08-15 |
Family
ID=18183043
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP32600689A Pending JPH03187897A (en) | 1989-12-18 | 1989-12-18 | Saccharide rate quality controller |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03187897A (en) |
-
1989
- 1989-12-18 JP JP32600689A patent/JPH03187897A/en active Pending
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