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JPS5911128B2 - Method for controlling the amount of glue added at a constant concentration - Google Patents
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JPS5911128B2 - Method for controlling the amount of glue added at a constant concentration - Google Patents

Method for controlling the amount of glue added at a constant concentration

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Publication number
JPS5911128B2
JPS5911128B2 JP51066727A JP6672776A JPS5911128B2 JP S5911128 B2 JPS5911128 B2 JP S5911128B2 JP 51066727 A JP51066727 A JP 51066727A JP 6672776 A JP6672776 A JP 6672776A JP S5911128 B2 JPS5911128 B2 JP S5911128B2
Authority
JP
Japan
Prior art keywords
sizing agent
flow rate
additive
temperature
transmission signal
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
Application number
JP51066727A
Other languages
Japanese (ja)
Other versions
JPS52149587A (en
Inventor
敬 谷所
克明 横田
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.)
Kanadevia Corp
Original Assignee
Hitachi Shipbuilding and 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 Hitachi Shipbuilding and Engineering Co Ltd filed Critical Hitachi Shipbuilding and Engineering Co Ltd
Priority to JP51066727A priority Critical patent/JPS5911128B2/en
Publication of JPS52149587A publication Critical patent/JPS52149587A/en
Publication of JPS5911128B2 publication Critical patent/JPS5911128B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 この発明は、例えば製紙工程において紙原料に10糊剤
を添加する際に実施される定濃度の糊剤の添加量制御方
法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for controlling the amount of a sizing agent added at a constant concentration, which is carried out, for example, when adding 10 sizing agents to paper raw materials in a paper manufacturing process.

従来、被添加物輸送管と、この管と合流すると共に途中
に流量制御弁を有する糊剤輸送管とを備えた糊剤添加装
置において、糊剤添加後の混合物15の粘度を一定に保
持するのに相当困難であつた。
Conventionally, the viscosity of the mixture 15 after addition of the sizing agent is maintained constant in a sizing agent addition device equipped with an additive material transporting pipe and a sizing agent transporting pipe that merges with this pipe and has a flow rate control valve in the middle. It was quite difficult.

その主な理由は、糊剤がたとえ一定濃度であつても温度
によつてその粘度が変わること、及び被添加物輸送管内
を流れる被添加物の流量が刻々と変化することにあつた
。加 この発明の目的は、上記の欠点を除去し、被添加
物の流量の変化及び同温度の変化を測定し、これに対応
して自動的に糊剤の流量を変化させて、糊剤添加後の混
合物の粘度を一定に保持することができる定濃度の糊剤
の添加量制御方法を提供し25ようるするにある。
The main reasons for this are that even if the sizing agent has a constant concentration, its viscosity changes depending on the temperature, and the flow rate of the additive flowing through the additive transport pipe changes from moment to moment. An object of the present invention is to eliminate the above-mentioned drawbacks, measure changes in the flow rate and temperature of the material to be added, automatically change the flow rate of the sizing agent accordingly, and add the sizing agent. It is an object of the present invention to provide a method for controlling the amount of a sizing agent added at a constant concentration by which the viscosity of a subsequent mixture can be kept constant.

この発明者らは、上記の目的を達成するために鋭意研究
を重ねた結果、下記の点を案出した。
As a result of extensive research to achieve the above object, the inventors devised the following points.

まず、一般に糊剤の粘度Mと糊剤の温度(を)との関係
は次式で示されることが知られている。30り=C2e
−aを・・・・・・・・・・・・・・・(I)但しC2
■糊剤の特性によつて定まる定数、a二糊剤の特性によ
つて定まる定数で、糊剤の粘度の自然対数と温度との関
係を グラフに直線として表わしたさいのそ 35の直線の傾きに負符号を付した値、 を:糊剤の温度。
First, it is generally known that the relationship between the viscosity M of the glue and the temperature of the glue is expressed by the following equation. 30ri=C2e
-a・・・・・・・・・・・・・・・(I) However, C2
■Constant determined by the properties of the glue, a2Constant determined by the properties of the glue. The value of the slope with a negative sign, is: the temperature of the glue.

また一般に、紙原料等においては、糊剤添加後の混合物
の粘度を一定に保つためには、添加率(γ)を大きくす
れば粘度(7)は小さくてよく、一方粘度が大きくなれ
ば添加率(γ)は小さくてよく、したがつて添加率(γ
)と粘度Mは反比例する。
In addition, in general, for paper raw materials, etc., in order to keep the viscosity of the mixture constant after adding a sizing agent, the viscosity (7) can be lowered by increasing the addition rate (γ), whereas the viscosity (7) can be lowered by increasing the viscosity. The addition rate (γ) may be small, so the addition rate (γ
) and viscosity M are inversely proportional.

これを式で表わすと、つぎのようになる。但しV:糊剤
の粘度、 ●τ1 Fp:糊剤の流量 FM:被添加物の流量 上記(1),()式よりVとγとを消去すると、つぎの
()式が成立する。
This can be expressed as a formula as follows. However, V: viscosity of the sizing agent, ●τ1 Fp: flow rate of the sizing agent FM: flow rate of the additive When V and γ are eliminated from the above equations (1) and (), the following equation () holds true.

FP=KeaTFM・・・・・・・・・・・・()なお
、紙原料等の被添加物は糊剤に対して大容量であるので
、被添加物の温度1は糊剤の添加によつてもほとんど変
らず、したがつて糊剤の温度(t)は被添加物に添加さ
れた後に被添加物の温度1となるので、糊剤の温度(t
)に代えて被添加物の温度1が使用されている。
FP=KeaTFM・・・・・・・・・・・・() Note that since the additives such as paper raw materials have a large capacity relative to the size agent, the temperature 1 of the additives does not affect the addition of the size agent. Therefore, the temperature of the sizing agent (t) becomes the temperature 1 of the additive after being added to the additive, so the temperature of the sizing agent (t)
) is used instead of the temperature 1 of the additive.

上記()式によれば、糊剤の粘度Mを直接測定すること
なく、糊剤添加後の混合物の粘度を一定に保ちながら被
添加物の流量(FM)、同温度1及び糊剤の流量(Fp
)を種々に変更して実験的に数値(代)を求めることが
できる。
According to the above equation (), without directly measuring the viscosity M of the sizing agent, while keeping the viscosity of the mixture after adding the sizing agent constant, the flow rate (FM) of the additive, the same temperature 1, and the flow rate of the sizing agent can be calculated. (Fp
) can be experimentally determined by various changes.

そしてこのようにして、実験的に数値(代)を予め求め
たのち、こんどは実際に製品をつくる段階において被添
加物の流量(FM)と同温度1を測定して、これらの測
定値と予め実験的に求められた数値(代)とを逆に()
式に入れると、混合物の粘度を一定に保持し得る糊剤の
添加流量(Fp)を算出することができる。
In this way, after experimentally determining numerical values (substances) in advance, the flow rate (FM) of the additive and the same temperature 1 are measured at the stage of actually manufacturing the product, and these measured values and Reverse the numerical value (substitution) obtained experimentally in advance ()
By entering into the equation, it is possible to calculate the addition flow rate (Fp) of the sizing agent that can keep the viscosity of the mixture constant.

糊剤の実際の添加流量をこの算出された流量(Fp)に
自動的に制御することにより、糊剤添加後の混合物の粘
度を一定に保つことができ、これがこの発明の方法を構
成しているものである。この発明の方法を、以下図面を
参照しながら説明する。
By automatically controlling the actual addition flow rate of the sizing agent to this calculated flow rate (Fp), the viscosity of the mixture after adding the sizing agent can be kept constant, which constitutes the method of the present invention. It is something that exists. The method of this invention will be explained below with reference to the drawings.

図面において、1は被添加物輸送管、2,3はその途中
に設けられた流量計及び温度計で、それぞれ測定した値
をデジタル伝送信号に変換する変換器を備えている。
In the drawings, reference numeral 1 indicates an additive transport pipe, and 2 and 3 indicate a flow meter and a thermometer installed in the middle thereof, each of which is equipped with a converter for converting measured values into digital transmission signals.

5は被添加物輸送管1に合流する糊剤輸送管で、途中に
は流量制御弁6を備えている。
Reference numeral 5 denotes a paste transport pipe that joins the additive transport pipe 1, and is provided with a flow rate control valve 6 in the middle.

7は流量計2及び温度計3からの伝送信号を得て、上記
式を演算して、得られた伝送信号を流量制御弁6に送る
ようになされた計算機で、演算器8〜12を備えている
7 is a calculator configured to obtain transmission signals from the flowmeter 2 and thermometer 3, calculate the above equation, and send the obtained transmission signal to the flow rate control valve 6, and is equipped with calculation units 8 to 12. ing.

上記のような糊剤添加装置を使用して、まず(I[)式
を満足する数値(代)を糊剤添加後の混合物の粘度を一
定に保ちながら、糊剤の流量(Fp)、被添加物の流量
(FM)及び被添加物の温度1を変化させて実験的に求
める。
Using the above-mentioned sizing agent addition device, first, the flow rate (Fp) of the sizing agent and the amount of the sizing agent are determined while keeping the viscosity of the mixture after adding the sizing agent constant. It is determined experimentally by changing the flow rate (FM) of the additive and the temperature 1 of the additive.

上記実験において得られた数値(代)を計算機7の演算
器11に記憶させておく、また演算器8に定数(a)を
記憶させておく。
The numerical values (alternatives) obtained in the above experiment are stored in the arithmetic unit 11 of the calculator 7, and the constant (a) is stored in the arithmetic unit 8.

上記の準備ののち、実際に被添加物を輸送管1内に流し
、輸送管5より糊剤を添加することになるが、糊剤の添
加量は次のようにして自動的に制御される。すなわち、
まず流量計2によつて被添加物の流量(FM)が測定さ
れる。測定された値は流量計2によつてデジタル伝送信
号に変換され演算器10に送り込まれる。一方温度計3
によつて被添加物の温度CI′)が測定され、測定され
た値は温度計3によつてデジタル伝送信号に変換され演
算器8に送り込まれる。温度(1)を表わす伝送信号は
演算器8において定数(a)を表わす伝送信号と掛け合
わされて、(AT)を表わす伝送信号に変換される。該
(AT)を表わす伝送信号は演算器9に送り込まれ、そ
こで(EaT)を表わす伝送信号に変換されて演算器1
0に送られ、そこで流量(FM)を表わす伝送信号と掛
け合わされて、(EaT−FM)を表わす伝送信号に変
換される。該(EaT−FM)を表わす伝送信号は演算
器11に送り込まれ、そこで数値(代)を表わす伝送信
号と掛け合わされ、流量(Fp)を表わす伝送信号に変
換される。該流量(Fp)を表わす伝送信号は、演算器
12に送り込まれ、そこで該伝送信号に対応する制御弁
6の開度を表わす伝送信号に変換される。該伝送信号は
制御弁6に送り込まれ、制御弁6の開度を調節する。こ
のようにして糊剤の添加量(FM)が自動制御されるも
のである。この発明の方法によれば、被添加物の流量の
変化及び同温度の変化を測定し、これに対応して、自動
的に糊剤の流量を変化させて、糊剤の添加量を自動制御
することにより、糊剤添加後の混合物の粘度を一定に保
持することができるという効果を奏する。
After the above preparations, the material to be added is actually poured into the transport pipe 1, and the sizing agent is added from the transport pipe 5. The amount of sizing agent added is automatically controlled as follows. . That is,
First, the flow meter 2 measures the flow rate (FM) of the additive. The measured value is converted into a digital transmission signal by the flowmeter 2 and sent to the computing unit 10. On the other hand, thermometer 3
The temperature CI') of the additive is measured, and the measured value is converted into a digital transmission signal by the thermometer 3 and sent to the computing unit 8. The transmission signal representing the temperature (1) is multiplied by the transmission signal representing the constant (a) in the arithmetic unit 8 and converted into the transmission signal representing (AT). The transmission signal representing (AT) is sent to the arithmetic unit 9, where it is converted into a transmission signal representing (EaT) and sent to the arithmetic unit 1.
0, where it is multiplied by a transmission signal representing flow rate (FM) and converted into a transmission signal representing (EaT-FM). The transmission signal representing the (EaT-FM) is sent to the arithmetic unit 11, where it is multiplied by a transmission signal representing a numerical value (substitute) and converted into a transmission signal representing the flow rate (Fp). The transmission signal representing the flow rate (Fp) is sent to the computing unit 12, where it is converted into a transmission signal representing the opening degree of the control valve 6 corresponding to the transmission signal. The transmission signal is sent to the control valve 6 to adjust the opening degree of the control valve 6. In this way, the amount of sizing agent added (FM) is automatically controlled. According to the method of this invention, changes in the flow rate and temperature of the additive are measured, and the flow rate of the sizing agent is automatically changed accordingly, thereby automatically controlling the amount of sizing agent added. By doing so, it is possible to maintain a constant viscosity of the mixture after adding the sizing agent.

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

図面はこの発明の実施に使用される装置の系統図である
。 1・・・・・・被添加物輸送管、5・・・・・・糊剤輸
送管、6・・・・・・流量制御弁、7・・・・・・計算
機。
The drawing is a system diagram of the equipment used to carry out the invention. DESCRIPTION OF SYMBOLS 1... Additive transport pipe, 5... Paste transport pipe, 6... Flow rate control valve, 7... Calculator.

Claims (1)

【特許請求の範囲】 1 被添加物輸送管1と、この管1と合流すると共に途
中に流量制御弁6を有する糊剤輸送管5とを備えた糊剤
添加装置において、定濃度の糊剤を被添加物に添加する
に当り、まず、Fp=Ke^a^TF_M 但しFp:糊剤の流量、 a:糊剤の特性によつて定まる定数で、 糊剤の粘度の自然対数と温度との関 係をグラフに直線として表わしたさ いのその直線の傾きに負符号を付し た値、 T:被添加物の温度、 F_M:被添加物の流量、 上記式を満足する数値(K)を、糊剤添加後の混合物の
粘度を一定に保ちながら、糊剤の流量(Fp)、被添加
物の流量(F_M)及び被添加物の温度(T)を変化さ
せて予め実験的に求めておき、上記準備ののち、被添加
物の流量(F_M)と同温度(T)とを自動的に測定し
、測定によつて得られた値を伝送信号に変換して計算機
7に入れ、その計算機7によつて前記式を演算させて糊
剤の流量(Fp)を伝送信号として得、その伝送信号に
よつて流量制御弁6の開度を調節して糊剤の流量(Fp
)を調節して糊剤の添加量を制御することを特徴とする
定濃度の糊剤の添加量制御方法。
[Scope of Claims] 1. In a sizing agent addition device equipped with a material transporting pipe 1 and a sizing agent transporting pipe 5 that merges with this pipe 1 and has a flow rate control valve 6 in the middle, a sizing agent of a constant concentration is used. When adding to the additive, first, Fp = Ke^a^TF_M, where Fp: flow rate of the sizing agent, a: a constant determined by the properties of the sizing agent, and the natural logarithm of the viscosity of the sizing agent and the temperature. When the relationship is expressed as a straight line on a graph, the value of the slope of the straight line with a negative sign, T: temperature of the additive, F_M: flow rate of the additive, the value (K) that satisfies the above formula, While keeping the viscosity of the mixture after addition of the sizing agent constant, the flow rate of the sizing agent (Fp), the flow rate of the added material (F_M), and the temperature of the added material (T) are experimentally determined in advance. After the above preparation, the flow rate (F_M) and temperature (T) of the additive are automatically measured, and the values obtained by the measurement are converted into a transmission signal and input into the computer 7, and the computer 7 calculates the above formula to obtain the flow rate (Fp) of the glue as a transmission signal, and adjusts the opening degree of the flow rate control valve 6 based on the transmission signal to obtain the flow rate (Fp) of the glue.
) A method for controlling the amount of a sizing agent added at a constant concentration, the method comprising controlling the amount of sizing agent added by adjusting the amount of sizing agent added.
JP51066727A 1976-06-07 1976-06-07 Method for controlling the amount of glue added at a constant concentration Expired JPS5911128B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP51066727A JPS5911128B2 (en) 1976-06-07 1976-06-07 Method for controlling the amount of glue added at a constant concentration

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP51066727A JPS5911128B2 (en) 1976-06-07 1976-06-07 Method for controlling the amount of glue added at a constant concentration

Publications (2)

Publication Number Publication Date
JPS52149587A JPS52149587A (en) 1977-12-12
JPS5911128B2 true JPS5911128B2 (en) 1984-03-13

Family

ID=13324205

Family Applications (1)

Application Number Title Priority Date Filing Date
JP51066727A Expired JPS5911128B2 (en) 1976-06-07 1976-06-07 Method for controlling the amount of glue added at a constant concentration

Country Status (1)

Country Link
JP (1) JPS5911128B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5919366B2 (en) * 1978-03-27 1984-05-04 富士金属工作株式会社 flow control device
JPS5919365B2 (en) * 1978-03-27 1984-05-04 富士金属工作株式会社 flow control device

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4517520Y1 (en) * 1969-12-17 1970-07-17

Also Published As

Publication number Publication date
JPS52149587A (en) 1977-12-12

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