JPH09271654A - Liquid mixing apparatus and method - Google Patents

Liquid mixing apparatus and method

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Publication number
JPH09271654A
JPH09271654A JP8085358A JP8535896A JPH09271654A JP H09271654 A JPH09271654 A JP H09271654A JP 8085358 A JP8085358 A JP 8085358A JP 8535896 A JP8535896 A JP 8535896A JP H09271654 A JPH09271654 A JP H09271654A
Authority
JP
Japan
Prior art keywords
transfer
flow rate
ratio
control valve
mixing
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
JP8085358A
Other languages
Japanese (ja)
Other versions
JP3976813B2 (en
Inventor
Masatsugu Yamaguchi
雅嗣 山口
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.)
Nittetsu Mining Co Ltd
Original Assignee
Nittetsu Mining 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 Nittetsu Mining Co Ltd filed Critical Nittetsu Mining Co Ltd
Priority to JP08535896A priority Critical patent/JP3976813B2/en
Publication of JPH09271654A publication Critical patent/JPH09271654A/en
Application granted granted Critical
Publication of JP3976813B2 publication Critical patent/JP3976813B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To continuously perform the mixing/transfer treatment of a plurality of liquids while making an apparatus compact and to prevent the fluctuations of a mixing ratio to perform mixing/transfer with high accuracy. SOLUTION: This liquid mixing apparatus 1 is equipped with an internal gear pump 10 having two suction ports 3, 4 and one emitting port 6 and equipped with a regulation valve 8 altering the open areas of the suction ports 3, 4 to make a transfer ratio alterable, the flow rate detection means 18, 19 respectively arranged on the side of the suction ports 3 and on the side of the emitting port 6 and a control means 21 regulating the regulation valve 8 based on the detection signals of the flow rate detection means 18, 19 to alter the transfer ratio of a plurality of liquids to requlate the transfer/mixing/ transfer ratio of a plurality of the liquids.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、食品工業、化学工
業、医農薬化粧品工業、石油化学工業等の諸産業におい
て、複数液を所望の比率で連続的に混合・移送する液混
合装置及び方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a liquid mixing apparatus and method for continuously mixing and transferring a plurality of liquids at a desired ratio in various industries such as the food industry, chemical industry, medical / agricultural cosmetics industry, petrochemical industry and the like. It is about.

【0002】[0002]

【従来の技術】従来より、複数液を混合・移送する液混
合装置としては、所定の比率で供給された一定量の液体
同士を撹拌・混合する撹拌タンクと、該撹拌タンクで処
理した混合液を次のプロセスに移送する移送用ポンプと
を組み合わせたバッチ処理式のもの、あるいは、供給さ
れた液体を撹拌・混合しながら圧送するラインミキサー
と、該ラインミキサーに混合すべき液体を所定の比率で
供給するための原料供給用ポンプとを組み合わせた連続
処理式のもの等が、種々使用されている。
2. Description of the Related Art Conventionally, as a liquid mixing device for mixing and transferring a plurality of liquids, a stirring tank for stirring and mixing a fixed amount of liquids supplied at a predetermined ratio, and a mixed liquid treated in the stirring tank. Of a batch processing type that is combined with a transfer pump that transfers the liquid to the next process, or a line mixer that pressure-feeds the supplied liquid while stirring and mixing the liquid, and a predetermined ratio of the liquid to be mixed in the line mixer. Various types of continuous treatment type and the like, which are combined with a raw material supply pump for supplying in the above are used.

【0003】しかし、前述の撹拌タンクを使用するバッ
チ処理式のものは、撹拌タンクの容量単位でしか処理が
できず、処理量を任意量に調整することができないとい
う不便があった。また、撹拌タンクに原料の供給中は、
混合・移送処理が中断するため、処理に時間がかかると
いう問題もあった。
However, the batch processing type using the agitation tank described above is inconvenient in that the processing can be performed only by the volume unit of the agitation tank, and the processing amount cannot be adjusted to an arbitrary amount. Also, while the raw material is being supplied to the stirring tank,
There is also a problem that the processing takes time because the mixing / transfer processing is interrupted.

【0004】一方、ラインミキサーを利用する連続処理
式のものは、処理量を任意量に調整することができ、し
かも、混合・移送処理を中断することなく実行できると
いう長所があるが、ラインミキサー自体が液体相互を撹
拌・混合するために一定以上の長さ寸法を必要とするた
め、装置のコンパクト化が難しいという問題があった。
また、液体相互の混合比率が、原料をラインミキサーに
供給する各ポンプの吐出量によって設定されるため、混
合比率の微調整が難しいという問題もあった。
On the other hand, the continuous processing type utilizing a line mixer has an advantage that the processing amount can be adjusted to an arbitrary amount and the mixing / transfer processing can be executed without interruption. There is a problem that it is difficult to make the apparatus compact, because the liquid itself needs a certain length or more for stirring and mixing the liquids.
Further, since the mixing ratio of the liquids is set by the discharge amount of each pump that supplies the raw material to the line mixer, there is a problem that it is difficult to finely adjust the mixing ratio.

【0005】そこで、このような背景から、二つの吸込
口及び一つの吐出口を有すると共に、前記各吸込口の開
口面積を変更して移送比率を変更可能な調節弁を備えた
内接形歯車ポンプを使用した液混合装置が開発された。
この液混合装置は、前記内接形歯車ポンプの各吸込口
に、それぞれ、原料液体を貯留した原料タンクを接続し
たもので、前記内接形歯車ポンプを連続稼働することに
より連続的に混合・移送を行うことができ、ラインミキ
サーを使用した装置と比較してコンパクト化することが
できる。しかも、前記内接形歯車ポンプに供給される原
料液相互の混合比率は、該内接形歯車ポンプに装備され
た調節弁によって、調整することができる。
From this background, therefore, an internal gear having two suction ports and one discharge port and a control valve capable of changing the transfer ratio by changing the opening area of each suction port. A liquid mixing device using a pump was developed.
This liquid mixing device is one in which a raw material tank storing a raw material liquid is connected to each suction port of the internal gear pump, and the internal gear pump is continuously operated to continuously mix and mix. It can be transferred and can be made compact as compared with an apparatus using a line mixer. In addition, the mixing ratio of the raw material liquids supplied to the internal gear pump can be adjusted by the control valve equipped in the internal gear pump.

【0006】[0006]

【発明が解決しようとする課題】ところが、前述の内接
形歯車ポンプを使用した従来の液混合装置は、前記調節
弁が前記内接形歯車ポンプに外付けされた操作レバー等
によって手動操作されるもので、各原料タンクにおける
サクションヘッドや各原料液の粘度を考慮して所定の混
合比率が得られるように、運用前に、前記調節弁を操作
することによって内接形歯車ポンプへの各原料液の流入
量を調整している。しかし、前記調節弁が手動操作であ
るがため、例えば、運用中に、原料タンク中の液面変化
によるサクションヘッドの変動や温度等の影響による原
料液の粘度変化によって、内接形歯車ポンプの各吸込口
への原料液の流入比が変化し、それによって混合比率が
変動する場合には、混合比率が不安定になって、混合精
度の低下等の問題が生じる虞が有った。
However, in the conventional liquid mixing apparatus using the above-mentioned internal gear pump, the control valve is manually operated by an operation lever or the like externally attached to the internal gear pump. In order to obtain a predetermined mixing ratio in consideration of the viscosity of the suction head and each raw material liquid in each raw material tank, each of the internal gear pumps is operated by operating the control valve before operation. The inflow rate of the raw material liquid is adjusted. However, since the control valve is manually operated, for example, during operation, due to a change in the suction head due to a change in the liquid level in the raw material tank, a change in the viscosity of the raw material liquid due to the influence of temperature, etc. When the inflow ratio of the raw material liquid to each suction port changes and the mixing ratio fluctuates accordingly, the mixing ratio becomes unstable, and there is a possibility that problems such as deterioration of the mixing accuracy may occur.

【0007】そこで、本発明の目的は上記課題を解消す
ることにあり、複数液の混合・移送処理を連続的に実施
できると同時に装置のコンパクト化にも適し、しかも、
運用中に、原料液の混合比率や粘度に変動が生じた時に
は、調節弁の位置を自動調整して、混合比率を初期の適
性値に修正することができて、混合比率の変動を防止
し、高精度の混合・移送を行うことのできる液混合装置
及び方法を提供することである。
Therefore, an object of the present invention is to solve the above-mentioned problems, and it is possible to continuously carry out the mixing / transferring process of a plurality of liquids, and at the same time, it is suitable for downsizing of the apparatus.
If the mixing ratio or viscosity of the raw material liquid fluctuates during operation, the position of the control valve can be automatically adjusted to correct the mixing ratio to the initial appropriate value, preventing fluctuations in the mixing ratio. It is an object of the present invention to provide a liquid mixing apparatus and method capable of highly accurate mixing / transferring.

【0008】[0008]

【課題を解決するための手段】本発明の上記目的は、二
つの吸込口及び一つの吐出口を有すると共に、前記各吸
込口の開口面積を変更して移送比率を変更可能な調節弁
を備えた内接形歯車ポンプと、前記各吸込口側及び前記
吐出口側の少なくとも二箇所に配設された流量検知手段
と、前記流量検知手段の検知信号に基づいて前記調節弁
を調節し、複数液の移送比率を変更する制御手段とを備
え、複数液の移送・混合・移送比率の調節を行う液混合
装置により達成される。
The above object of the present invention is to provide a control valve having two suction ports and one discharge port and capable of changing the transfer ratio by changing the opening area of each suction port. Internal gear pump, a flow rate detecting means disposed at at least two positions on each of the suction port side and the discharge port side, and the control valve is adjusted based on a detection signal of the flow rate detecting means, This is achieved by a liquid mixing apparatus that includes a control unit that changes the liquid transfer ratio and that controls the transfer / mixing / transfer ratio of a plurality of liquids.

【0009】また、本発明の上記目的は、二つの吸込口
及び一つの吐出口を有すると共に、前記各吸込口の開口
面積を変更して移送比率を変更可能な調節弁を備えた内
接形歯車ポンプと、前記吐出口側に配設された粘度検出
手段と、前記粘度検出手段の検知信号に基づいて前記調
節弁を調節し、複数液の移送比率を変更する制御手段と
を備え、複数液の移送・混合・移送比率の調節を行う液
混合装置によっても達成することができる。
Further, the above object of the present invention is to provide an inscribed type having two suction ports and one discharge port and having a control valve capable of changing the transfer ratio by changing the opening area of each suction port. A gear pump, a viscosity detecting means disposed on the discharge port side, and a control means for adjusting the adjusting valve based on a detection signal of the viscosity detecting means and changing a transfer ratio of a plurality of liquids, This can also be achieved by a liquid mixing device that performs liquid transfer / mixing / adjustment of the transfer ratio.

【0010】さらに、本発明の上記目的は、二つの吸込
口及び一つの吐出口を有すると共に、前記各吸込口の開
口面積を変更して移送比率を変更可能な調節弁を備えた
内接形歯車ポンプにより、複数液の移送・混合・移送比
率の調節を行う液混合方法において、前記各吸込口側及
び前記吐出口側の少なくとも二箇所に配設された流量検
知手段の検知信号に基づいて前記調節弁を調節し、複数
液の移送比率の調節を行うことを特徴とする液混合方法
により達成される。
Further, the above-mentioned object of the present invention is an inscribed type having two suction ports and one discharge port, and equipped with a control valve capable of changing the transfer ratio by changing the opening area of each suction port. In a liquid mixing method of transferring, mixing, and adjusting a transfer ratio of a plurality of liquids by a gear pump, based on a detection signal of a flow rate detection unit arranged at least at two positions on each of the suction port side and the discharge port side. This is achieved by a liquid mixing method characterized by adjusting the control valve to adjust the transfer ratio of a plurality of liquids.

【0011】そして、本発明の上記目的は、二つの吸込
口及び一つの吐出口を有すると共に、前記各吸込口の開
口面積を変更して移送比率を変更可能な調節弁を備えた
内接形歯車ポンプにより、複数液の移送・混合・移送比
率の調節を行う液混合方法において、前記吐出口側に配
設された粘度検出手段の検知信号に基づいて前記調節弁
を調節し、所定粘度の混合液を得ることを特徴とする液
混合方法によっても達成することができる。
The above object of the present invention is an inscribed type having two suction ports and one discharge port, and equipped with a control valve capable of changing the transfer ratio by changing the opening area of each suction port. In a liquid mixing method in which a plurality of liquids are transferred, mixed, and the transfer ratio is adjusted by a gear pump, the control valve is adjusted based on a detection signal of a viscosity detection unit arranged on the discharge port side to adjust a predetermined viscosity. This can also be achieved by a liquid mixing method characterized by obtaining a mixed liquid.

【0012】本発明の上記構成によれば、内接形歯車ポ
ンプを利用する方式により該内接形歯車ポンプを連続稼
働させることで、複数液の混合・移送処理を連続的に実
施でき、前記内接形歯車ポンプの稼働を制御すること
で、処理量を任意量に調整することができる。
According to the above configuration of the present invention, by continuously operating the internal gear pump by the system utilizing the internal gear pump, it is possible to continuously carry out the mixing / transferring process of a plurality of liquids. By controlling the operation of the internal gear pump, the processing amount can be adjusted to an arbitrary amount.

【0013】そして、運用中に、原料タンク中の液面変
化によるサクションヘッドの変動や温度等の影響による
原料液の粘度変化によって、内接形歯車ポンプの各吸込
口への原料液の流入比が変化した場合には、それらサク
ションヘッドの変動や原料液の粘度変化に基づく原料液
の流入比の変化の発生が直ちに流量検知手段または粘度
検出手段によって検知される。そして、これら検知手段
の検知信号に基づいて内接形歯車ポンプの調節弁を操作
する制御手段が、元の適性な混合比率を維持すべく前記
調節弁の位置を自動調整する。
During operation, due to fluctuations in the suction head due to changes in the liquid level in the raw material tank and changes in the viscosity of the raw material liquid due to the effects of temperature, etc., the ratio of the inflow ratio of the raw material liquid to each suction port of the internal gear pump is increased. Is changed, the occurrence of a change in the suction head or a change in the inflow ratio of the raw material liquid due to a change in the viscosity of the raw material liquid is immediately detected by the flow rate detecting means or the viscosity detecting means. Then, the control means for operating the control valve of the internal gear pump based on the detection signals of these detection means automatically adjusts the position of the control valve so as to maintain the original proper mixing ratio.

【0014】[0014]

【発明の実施の形態】以下、図示実施形態により、本発
明を説明する。図1は、本発明に係る液混合装置の一実
施形態における概略構成を示したものである。本実施形
態の液混合装置1は、図示のように、二つの吸込口3,
4及び一つの吐出口6を有した内接形歯車ポンプ10
と、原料液体12,13を貯留して前記内接形歯車ポン
プ10の各吸込口3,4に接続されて各吸込口3,4に
原料液体12,13を供給する二つの原料タンク15,
16と、前記吸込口3側及び前記吐出口6側の二箇所に
配設された流量検知手段18,19と、前記流量検知手
段18,19の検知信号に基づいて前記内接形歯車ポン
プ10の調節弁8の位置を調節して前記吸込口3,4か
らの液流入率(即ち、移送比率)を変更する制御手段2
1とを備えており、前記吸込口3,4に供給された原料
液の移送・混合・移送比率の調節を行う。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below with reference to the illustrated embodiments. FIG. 1 shows a schematic configuration of an embodiment of a liquid mixing apparatus according to the present invention. The liquid mixing apparatus 1 of the present embodiment has two suction ports 3 as shown in the drawing.
Internal gear pump 10 having four and one discharge port 6
And two raw material tanks 15 for storing the raw material liquids 12 and 13 and being connected to the suction ports 3 and 4 of the internal gear pump 10 to supply the raw material liquids 12 and 13 to the suction ports 3 and 4,
16, flow rate detecting means 18 and 19 disposed at two positions on the suction port 3 side and the discharge port 6 side, and the internal gear pump 10 based on the detection signals of the flow rate detecting means 18 and 19. The control means 2 for adjusting the position of the control valve 8 of the above and changing the liquid inflow rate (that is, the transfer rate) from the suction ports 3 and 4.
1 for adjusting the transfer / mixing / transfer ratio of the raw material liquids supplied to the suction ports 3 and 4.

【0015】ここで、前記内接形歯車ポンプ10は、前
記吸込口3,4及び吐出口6を有したポンプケーシング
23と、リング状に装備される歯25a間に原料液が挿
通可能なスリット25bが形成されて前記ポンプケーシ
ング23内に回転自在に支持された外転ギヤ25と、こ
の外転ギヤ25の内側で偏心した位置で外転ギヤ25に
噛合するピニオンギヤ27と、前記ポンプケーシング2
3に固定装備されて前記ピニオンギヤ27を前記外転ギ
ヤ25に対して偏心した位置に保つ断面三日月状の支持
板29と、前記外転ギヤ25の外周に沿って移動可能に
装備されて吸込口3,4の開口面積S1 ,S2 を変更す
ることで移送比率を変更可能な調節弁8と、前記ピニオ
ンギヤ27を回転駆動するモータ(図示略)とを備えた
構成をなしており、前記ピニオンギヤ27の回転に伴っ
て前記ピニオンギヤ27と外転ギヤ25との噛み合い量
が変化することを利用して、吸込口3,4に供給された
各原料液体12,13の吸引、撹拌・混合、移送を行
う。
Here, the internal gear pump 10 has a slit in which the raw material liquid can be inserted between the pump casing 23 having the suction ports 3 and 4 and the discharge port 6 and the tooth 25a provided in a ring shape. 25b is formed and is rotatably supported in the pump casing 23; an outer rotation gear 25;
3, a support plate 29 having a crescent-shaped cross section, which is fixedly mounted on the outer ring gear 25 to keep the pinion gear 27 in an eccentric position with respect to the outer ring gear 25, and is movably mounted along the outer periphery of the outer ring gear 25. A control valve 8 whose transfer ratio can be changed by changing the opening areas S 1 and S 2 of 3 and 4 and a motor (not shown) for rotationally driving the pinion gear 27 are provided. Utilizing the fact that the meshing amount of the pinion gear 27 and the outer gear 25 changes with the rotation of the pinion gear 27, the raw material liquids 12 and 13 supplied to the suction ports 3 and 4 are sucked, stirred and mixed, Transfer.

【0016】前記原料タンク15内の原料液体12を吸
込口3に導く管路31には、前記流量検知手段18より
も上流側に位置して、開閉弁33が装備されている。ま
た、前記原料タンク16内の原料液体13を吸込口4に
導く管路35にも、該管路35を開閉する開閉弁36が
装備されている。そして、前記吐出口6に接続される混
合液排出管路37には、前記流量検知手段19と、前記
混合液排出管路37を開閉する開閉弁38が装備されて
いる。この混合液排出管路37は、混合液に対して次の
プロセス処理を実施する次プロセス装置39に接続され
ている。
A pipeline 31 for guiding the raw material liquid 12 in the raw material tank 15 to the suction port 3 is equipped with an opening / closing valve 33 located upstream of the flow rate detecting means 18. Further, the pipeline 35 that guides the raw material liquid 13 in the raw material tank 16 to the suction port 4 is also equipped with an opening / closing valve 36 that opens and closes the pipeline 35. The mixed liquid discharge conduit 37 connected to the discharge port 6 is equipped with the flow rate detecting means 19 and an opening / closing valve 38 for opening and closing the mixed liquid discharge conduit 37. The mixed liquid discharge conduit 37 is connected to a next process device 39 that performs the next process treatment on the mixed liquid.

【0017】前記流量検知手段18,19は、本実施形
態の場合は、いずれも、各管路における流量を非接触で
検出して前記制御手段21に出力する電磁流量計である
が、流量が液圧に比例することを利用すれば、流量計の
代りに圧力計を使用するようにしてもよい。
In the case of this embodiment, the flow rate detecting means 18 and 19 are both electromagnetic flow meters which detect the flow rate in each pipe line in a non-contact manner and output it to the control means 21. A pressure gauge may be used instead of the flow meter if it is proportional to the hydraulic pressure.

【0018】前記制御手段21は、モータやソレノイド
等をアクチュエータとして使って、前記調節弁8を無段
階に移動調整すると共に、前記ピニオンギヤ27の回転
数を制御する。また、この制御手段21は、図示略の入
力手段(制御手段21に接続されているキーボードな
ど)からの指示で、前記調節弁8の位置を任意位置に初
期設定することができる。そして、内接形歯車ポンプ1
0が稼働されると、その初期に前記流量検知手段18,
19における検出値を記憶し、以後の運用中は、前記流
量検知手段18,19における検出値が一定値(一定範
囲)に維持されるように、前記流量検知手段18,19
の検知信号に基づいて、前記調節弁8の位置を自動調節
すると同時に、前記外転ギヤ25の回転数を制御する。
The control means 21 uses a motor, a solenoid, or the like as an actuator to move and adjust the control valve 8 steplessly, and controls the rotation speed of the pinion gear 27. Further, the control means 21 can initialize the position of the control valve 8 to an arbitrary position by an instruction from an input means (not shown) such as a keyboard connected to the control means 21. And the internal gear pump 1
When 0 is operated, the flow rate detecting means 18,
The detected value in 19 is stored, and during the subsequent operation, the detected value in the flow detecting means 18 and 19 is maintained at a constant value (constant range) so that the flow detecting means 18 and 19 are maintained.
The position of the control valve 8 is automatically adjusted on the basis of the detection signal of 1. and the rotation speed of the outer rotation gear 25 is controlled.

【0019】具体的には、前記制御手段21は、図2に
示す如く、調節弁8の位置および外転ギヤ25の回転を
調整する。前記内接形歯車ポンプ10の稼働前に、原料
液体12,13の流量A,B(初期設定値)と、前記吐
出口6における流量Q(初期設定値)とを記憶する(ス
テップ101)。次いで、前述の各流量検知手段18,
19からの検出値に基づいて、実際の前記吸込口3への
流入量qaと前記吐出口6からの吐出量qを検知し、こ
れらの検出値から、A/Bと、q/(q−qa)との大
小関係を比較し(ステップ102)、その判断結果に応
じて、A/Bがq/(q−qa)よりも小さければ前記
調節弁8を吸込口3側に移動させて、吸込口3の開口面
積を少なくすることによって、相対的に、前記吸込口4
からの流入量を増大させて、流量比率の変動を修正する
(ステップ103,104)。同様に、A/Bがq/
(q−qa)よりも大きい時には、前記調節弁8を吸込
口4側に移動させて、吸込口4の開口面積を少なくする
ことによって、相対的に、前記吸込口4からの流入量を
減少させて、流量比率の変動を修正する(ステップ11
0,111)。また、A/Bがq/(q−qa)に等し
い時には、前記調節弁8の位置は、そのままに保って、
現状の維持を図る(ステップ120)。
Specifically, as shown in FIG. 2, the control means 21 adjusts the position of the control valve 8 and the rotation of the outer rotation gear 25. Before the operation of the internal gear pump 10, the flow rates A and B (initial setting values) of the raw material liquids 12 and 13 and the flow rate Q (initial setting value) at the discharge port 6 are stored (step 101). Then, the above-mentioned flow rate detecting means 18,
Based on the detected value from 19, the actual inflow amount qa into the suction port 3 and the actual discharge amount q from the discharge port 6 are detected, and from these detected values, A / B and q / (q- qa) is compared (step 102), and if A / B is smaller than q / (q-qa) according to the determination result, the control valve 8 is moved to the suction port 3 side, By reducing the opening area of the suction port 3, the suction port 4 is relatively
The amount of inflow from is increased to correct the fluctuation of the flow rate ratio (steps 103 and 104). Similarly, A / B is q /
When it is larger than (q-qa), the control valve 8 is moved to the suction port 4 side to reduce the opening area of the suction port 4, thereby relatively reducing the inflow amount from the suction port 4. Then, the fluctuation of the flow rate is corrected (step 11
0,111). When A / B is equal to q / (q-qa), the position of the control valve 8 is kept as it is,
The current situation is maintained (step 120).

【0020】次いで、前記初期設定による吐出量Qと、
稼働後の流量検知手段19によって検出された実際の吐
出量qとの大小を比較して(ステップ130)、Q<q
であれば前記外転ギヤ25の回転を下げることで増大し
た流量を低減させ(ステップ131,132)、一方、
Q>qであれば前記外転ギヤ25の回転を上げることで
減少した流量の回復を図り(ステップ140,14
1)、Q=qであれば吐出量の変化がないため前記外転
ギヤ25の回転をそのままに保って、現状の維持を図る
(ステップ150)。
Next, the discharge amount Q by the initial setting,
The magnitude is compared with the actual discharge amount q detected by the flow rate detecting means 19 after the operation (step 130), and Q <q
If so, the increased flow rate is reduced by lowering the rotation of the outer rotation gear 25 (steps 131 and 132).
If Q> q, the rotation of the outer rotation gear 25 is increased to recover the reduced flow rate (steps 140, 14).
1) If Q = q, there is no change in the discharge amount, so the rotation of the outer rotation gear 25 is maintained as it is, and the current state is maintained (step 150).

【0021】そして、以上の流量比率の修正及び吐出量
の修正が終了したら、ステップ102に戻って、再び同
様の処理を繰り返す。
When the correction of the flow rate ratio and the correction of the discharge amount are completed, the process returns to step 102 and the same processing is repeated again.

【0022】上述の液混合装置1では、内接形歯車ポン
プ10を利用する方式により該内接形歯車ポンプ10を
連続稼働させることで、複数液の混合・移送処理を連続
的に実施でき、前記内接形歯車ポンプ10の稼働を制御
することで、処理量を任意量に調整することができる。
また、内接形歯車ポンプ10を利用する方式のため、従
来のラインミキサーを利用する方式のものと比較する
と、装置をコンパクト化することができる。
In the liquid mixing apparatus 1 described above, by continuously operating the internal gear pump 10 by the method of utilizing the internal gear pump 10, it is possible to continuously carry out the mixing / transferring process of a plurality of liquids. By controlling the operation of the internal gear pump 10, the processing amount can be adjusted to an arbitrary amount.
Further, since the system uses the internal gear pump 10, the device can be made compact as compared with the system using the conventional line mixer.

【0023】そして、運用中に、原料タンク15,16
中の液面変化によるサクションヘッドの変動や温度等の
影響による原料液12,13の粘度変化によって、内接
形歯車ポンプ10の各吸込口3,4への原料液12,1
3の流入比が変化した場合には、それらの原料液12,
13の流入比の変化の発生が直ちに流量検知手段18,
19によって検知され、これら検知手段18,19の検
知信号に基づいて内接形歯車ポンプ10の調節弁8を操
作する制御手段21が、元の適性な混合比率を維持すべ
く前記調節弁8の位置を自動調整する。したがって、運
用中の混合比率の変動を防止し、高精度の混合・移送を
行うことができる。
During operation, the raw material tanks 15 and 16
Due to the fluctuation of the suction head due to the change of the liquid level in the inside and the change of the viscosity of the raw material liquids 12 and 13 due to the influence of temperature and the like, the raw material liquids 12 and 1 to the respective suction ports 3 and 4 of the internal gear pump 10 are changed.
When the inflow ratio of No. 3 changes, those raw material liquids 12,
Immediately after the change of the inflow ratio of 13, the flow rate detecting means 18,
The control means 21 which operates the control valve 8 of the internal gear pump 10 based on the detection signals of the control means 8 and 19 detected by the control means 19 of the control valve 8 maintains the original proper mixing ratio. Adjust the position automatically. Therefore, it is possible to prevent fluctuations in the mixing ratio during operation and perform highly accurate mixing and transfer.

【0024】なお、前記流量検知手段18,19の装備
位置は、上述の実施形態の場合に限定するものではな
い。前記二つの吸込口3,4側及び吐出口6側の内の少
なくとも二箇所の流量を検知することができれば、混合
比率の変動を検知することができ、その検知信号に基づ
く前記調節弁8の制御や外転ギヤ25の回転数の制御に
よって、混合比率や吐出量を初期の設定値に戻すことが
可能である。したがって、図3(a)に示すように、内
接形歯車ポンプ10の吸込口4側と吐出口6側との二箇
所に流量検知手段41を装備するようにしてもよく、ま
た、図3(b)に示すように、内接形歯車ポンプ10の
二つの吸込口3,4側のそれぞれに流量検知手段41を
装備するようにしてもよく、また、図3(c)に示すよ
うに、二つの吸込口3,4側および吐出口6側の全てに
流量検知手段41を装備するようにしてもよい。
The equipment positions of the flow rate detecting means 18 and 19 are not limited to those in the above embodiment. If it is possible to detect the flow rate at least at two positions on the two suction ports 3, 4 side and the discharge port 6 side, it is possible to detect the variation of the mixing ratio, and the control valve 8 based on the detection signal can be detected. It is possible to return the mixing ratio and the discharge amount to the initial set values by control or control of the rotation speed of the outer gear 25. Therefore, as shown in FIG. 3A, the flow rate detecting means 41 may be provided at two locations on the suction port 4 side and the discharge port 6 side of the internal gear pump 10. As shown in (b), the flow rate detecting means 41 may be provided on each of the two suction ports 3, 4 of the internal gear pump 10, and as shown in FIG. 3 (c). The flow rate detecting means 41 may be provided on all of the two suction ports 3 and 4 and the discharge port 6 side.

【0025】図3(a)の構成とした場合の制御手段2
1における処理を図4に、図3(b)の構成とした場合
の制御手段21における処理を図5に、図3(c)の構
成とした場合の制御手段21における処理を図6に、そ
れぞれ示す。
Control means 2 in the case of the configuration of FIG.
4 shows the processing in FIG. 1, the processing in the control means 21 in the case of the configuration of FIG. 3B is shown in FIG. 5, the processing in the control means 21 in the case of the configuration of FIG. 3C is shown in FIG. Shown respectively.

【0026】図3(a)のように、吸込口4側と吐出口
6側とに流量検知手段41を装備した場合には、上記実
施形態の場合と同様であるが図4に示すように、前記内
接形歯車ポンプ10の稼働前に、原料液体12,13の
流量A,B(初期設定値)と、前記吐出口6における流
量Q(初期設定値)とを記憶する(ステップ201)。
次いで、前述の各流量検知手段41,41からの検出値
に基づいて、実際の前記吸込口4への流入量qbと前記
吐出口6からの吐出量qを検知し、これらの検出値か
ら、A/Bと、(q−qb)/qとの大小関係を比較し
(ステップ202)、その判断結果に応じて、A/Bが
(q−qb)/qよりも小さければ前記調節弁8を吸込
口3側に移動させて、吸込口3の開口面積を少なくする
ことによって、相対的に、前記吸込口4からの流入量を
増大させて、流量比率の変動を修正する(ステップ20
3,204)。同様に、A/Bが(q−qb)/qより
も大きい時には、前記調節弁8を吸込口4側に移動させ
て、吸込口4の開口面積を少なくすることによって、相
対的に、前記吸込口4からの流入量を減少させて、流量
比率の変動を修正する(ステップ210,211)。ま
た、A/Bが(q−qb)/qに等しい時には、前記調
節弁8の位置は、そのままに保って、現状の維持を図る
(ステップ220)。
When the flow rate detecting means 41 is provided on the suction port 4 side and the discharge port 6 side as shown in FIG. 3 (a), it is the same as in the above embodiment, but as shown in FIG. Before operation of the internal gear pump 10, the flow rates A and B (initial setting values) of the raw material liquids 12 and 13 and the flow rate Q (initial setting value) at the discharge port 6 are stored (step 201). .
Next, based on the detection values from the flow rate detecting means 41, 41, the actual inflow amount qb into the suction port 4 and the actual discharge amount q from the discharge port 6 are detected, and from these detection values, The magnitude relation between A / B and (q-qb) / q is compared (step 202), and if A / B is smaller than (q-qb) / q according to the judgment result, the control valve 8 Is moved toward the suction port 3 to reduce the opening area of the suction port 3, thereby relatively increasing the inflow amount from the suction port 4 and correcting the fluctuation of the flow rate ratio (step 20).
3,204). Similarly, when A / B is larger than (q-qb) / q, the control valve 8 is moved to the suction port 4 side to reduce the opening area of the suction port 4, thereby relatively The amount of inflow from the suction port 4 is reduced to correct the fluctuation of the flow rate ratio (steps 210 and 211). When A / B is equal to (q-qb) / q, the position of the control valve 8 is kept as it is, and the current state is maintained (step 220).

【0027】次いで、前記初期設定による吐出量Qと、
稼働後の吐出口6側の流量検知手段41によって検出さ
れた実際の吐出量qとの大小を比較して(ステップ23
0)、Q<qであれば前記外転ギヤ25の回転を下げる
ことで増大した流量を低減させ(ステップ231,23
2)、一方、Q>qであれば前記外転ギヤ25の回転を
上げることで減少した流量の回復を図り(ステップ24
0,241)、Q=qであれば吐出量の変化がないため
前記外転ギヤ25の回転をそのままに保って、現状の維
持を図る(ステップ250)。そして、以上の流量比率
の修正及び吐出量の修正が終了したら、ステップ202
に戻って、再び同様の処理を繰り返す。
Next, the discharge amount Q by the initial setting,
The size is compared with the actual discharge amount q detected by the flow rate detecting means 41 on the discharge port 6 side after the operation (step 23).
0) and Q <q, the flow rate increased by reducing the rotation of the outer gear 25 is reduced (steps 231, 23).
2) On the other hand, if Q> q, the flow rate reduced by increasing the rotation of the outer gear 25 is restored (step 24).
0, 241) and Q = q, there is no change in the discharge amount, so that the rotation of the outer rotation gear 25 is kept as it is and the current state is maintained (step 250). When the correction of the flow rate and the correction of the discharge amount are completed, step 202
Then, the same processing is repeated again.

【0028】図3(b)のように、二つの吸込口3,4
のそれぞれに流量検知手段41を装備した場合には、図
5に示すように、前記内接形歯車ポンプ10の稼働前
に、原料液体12,13の流量A,B(初期設定値)
と、前記吐出口6における流量Q(初期設定値)とを記
憶する(ステップ301)。次いで、前述の各流量検知
手段41,41からの検出値に基づいて、二つの吸込口
3,4への実際の流入量qa,qb及び吐出量qを検知
し、これらの検出値から、A/Bと、qa/qbとの大
小関係を比較し(ステップ302)、その判断結果に応
じて、A/Bがqa/qbよりも小さければ前記調節弁
8を吸込口3側に移動させて、吸込口3の開口面積を少
なくすることによって、相対的に、前記吸込口4からの
流入量を増大させて、流量比率の変動を修正する(ステ
ップ303,304)。同様に、A/Bがqa/qbよ
りも大きい時には、前記調節弁8を吸込口4側に移動さ
せて、吸込口4の開口面積を少なくすることによって、
相対的に、前記吸込口4からの流入量を減少させて、流
量比率の変動を修正する(ステップ310,311)。
また、A/Bがqa/qbに等しい時には、前記調節弁
8の位置は、そのままに保って、現状の維持を図る(ス
テップ320)。
As shown in FIG. 3B, the two suction ports 3 and 4 are provided.
When the flow rate detection means 41 is provided in each of the above, as shown in FIG. 5, the flow rates A and B of the raw material liquids 12 and 13 (initial setting values) are set before the operation of the internal gear pump 10.
And the flow rate Q (initial setting value) at the discharge port 6 are stored (step 301). Next, based on the detection values from the above-mentioned flow rate detecting means 41, 41, the actual inflow amounts qa, qb and the discharge amount q into the two suction ports 3, 4 are detected, and from these detection values, A / B and qa / qb are compared in magnitude (step 302), and if A / B is smaller than qa / qb, the control valve 8 is moved to the suction port 3 side according to the result of the determination. By reducing the opening area of the suction port 3, the amount of inflow from the suction port 4 is relatively increased to correct the fluctuation of the flow rate ratio (steps 303 and 304). Similarly, when A / B is larger than qa / qb, the control valve 8 is moved to the suction port 4 side to reduce the opening area of the suction port 4,
Relatively, the amount of inflow from the suction port 4 is reduced to correct the fluctuation of the flow rate ratio (steps 310 and 311).
When A / B is equal to qa / qb, the position of the control valve 8 is kept as it is, and the current state is maintained (step 320).

【0029】次いで、前記初期設定による吐出量Qと、
稼働後の吐出口6側の流量検知手段41によって検出さ
れた実際の吐出量qとの大小を比較して(ステップ33
0)、Q<qであれば前記外転ギヤ25の回転を下げる
ことで増大した流量を低減させ(ステップ331,33
2)、一方、Q>qであれば前記外転ギヤ25の回転を
上げることで減少した流量の回復を図り(ステップ34
0,341)、Q=qであれば吐出量の変化がないため
前記外転ギヤ25の回転をそのままに保って、現状の維
持を図る(ステップ350)。そして、以上の流量比率
の修正及び吐出量の修正が終了したら、ステップ302
に戻って、再び同様の処理を繰り返す。
Next, the discharge amount Q by the initial setting,
The size is compared with the actual discharge amount q detected by the flow rate detecting means 41 on the discharge port 6 side after the operation (step 33).
0), and if Q <q, the flow rate increased by reducing the rotation of the outer gear 25 is reduced (steps 331, 33).
2) On the other hand, if Q> q, the rotation of the outer rotation gear 25 is increased to recover the reduced flow rate (step 34).
0,341) and Q = q, there is no change in the discharge amount, so that the rotation of the outer rotation gear 25 is maintained as it is and the current state is maintained (step 350). When the correction of the flow rate ratio and the correction of the discharge amount are completed, step 302
Then, the same processing is repeated again.

【0030】図3(c)のように、二つの吸込口3,4
と吐出口6とのそれぞれに流量検知手段41を装備した
場合には、制御手段21における処理としては、図3
(b)の場合と同様でよい。ただし、吐出口6からの吐
出量qが41によって直接検出されるため、吸込口3側
に配置した流量検知手段41の検出値qaと吸込口4側
に配置した流量検知手段41の検出値qbとの和を演算
処理することで吐出量qを求める必要がなくなる。
As shown in FIG. 3C, the two suction ports 3 and 4 are provided.
When the flow rate detecting means 41 is provided in each of the discharge port 6 and the discharge port 6, the processing in the control means 21 is as shown in FIG.
It may be similar to the case of (b). However, since the discharge amount q from the discharge port 6 is directly detected by 41, the detected value qa of the flow rate detection unit 41 arranged on the suction port 3 side and the detection value qb of the flow rate detection unit 41 arranged on the suction port 4 side. It becomes unnecessary to obtain the discharge amount q by calculating the sum of

【0031】また、混合させるべき原料液体12,13
が、互いに粘度の異なる液体の場合、混合比率が変動し
た場合には、それによって吐出される混合液の粘度が変
化する。従って、図6に示すように、前述の流量検知手
段の代りに粘度検知手段43を吐出口6側に装備し、該
粘度検知手段43の検知信号に基づいて前記制御手段2
1が調節弁8の位置や外転ギヤ25の回転数を制御する
構成とすることで、運用中の混合比率の変動を防止し、
高精度の混合・移送を行うことができる。なお、粘度検
知手段43としては、吐出口6から吐出される混合液の
粘度を直接測定可能なインライン粘度計を用いることが
好ましい。
Further, the raw material liquids 12 and 13 to be mixed
However, in the case of liquids having different viscosities, when the mixing ratio changes, the viscosity of the mixed liquid discharged changes accordingly. Therefore, as shown in FIG. 6, instead of the above-described flow rate detecting means, a viscosity detecting means 43 is provided on the discharge port 6 side, and the control means 2 is based on the detection signal of the viscosity detecting means 43.
1 is configured to control the position of the control valve 8 and the rotation speed of the outer rotation gear 25, thereby preventing a change in the mixing ratio during operation,
High precision mixing and transfer can be performed. As the viscosity detecting unit 43, it is preferable to use an in-line viscometer that can directly measure the viscosity of the mixed liquid discharged from the discharge port 6.

【0032】なお、前述の図6のように内接形歯車ポン
プ10の吐出口6側に粘度検知手段43を装備した場合
には、前記制御手段21における制御処理は、図7のよ
うになる。ただし、この例では、吸込口3に流入する原
料液体12の方が、吸込口4に流入される原料液体13
よりも粘度が大きいものとする。前記内接形歯車ポンプ
10の稼働前に、所望する混合液の粘度ηを初期値とし
て記憶する(ステップ401)。次いで、稼働後に粘度
検知手段43が逐次検知する粘度ηcと、初期値ηとの
大小関係を比較し(ステップ402)、その判断結果に
応じて、ηがηcよりも小さければ、粘度の高い原料液
体12の流入割合が増えたことを意味しているため、前
記調節弁8を吸込口3側に移動させて吸込口3の開口面
積を少なくすることによって、相対的に、前記吸込口4
からの流入量を増大させて、粘度の変動を修正する(ス
テップ403,404)。一方、ηがηcよりも大きい
時には、吸込口4側の流入量が増えたことを意味するた
め、前記調節弁8を吸込口4側に移動させて、吸込口4
の開口面積を少なくすることによって、相対的に、前記
吸込口4からの流入量を減少させて、粘度の変動を修正
する(ステップ410,411)。また、ηがηcに等
しい時には、前記調節弁8の位置は、そのままに保っ
て、現状の維持を図り(ステップ420)、ステータ4
02に戻って以上の処理を繰り返す。
When the viscosity detecting means 43 is provided on the discharge port 6 side of the internal gear pump 10 as shown in FIG. 6, the control processing by the control means 21 is as shown in FIG. . However, in this example, the raw material liquid 12 that flows into the suction port 3 is the raw material liquid 13 that flows into the suction port 4.
The viscosity is higher than that. Before the operation of the internal gear pump 10, the desired viscosity η of the mixed liquid is stored as an initial value (step 401). Next, the magnitude relationship between the viscosity ηc sequentially detected by the viscosity detecting means 43 after the operation and the initial value η is compared (step 402), and if η is smaller than ηc according to the determination result, the raw material having high viscosity is obtained. Since it means that the inflow rate of the liquid 12 has increased, the control valve 8 is moved to the suction port 3 side to reduce the opening area of the suction port 3 and thus the suction port 4 is relatively moved.
The amount of inflow from is corrected to correct the fluctuation of viscosity (steps 403 and 404). On the other hand, when η is larger than ηc, it means that the inflow amount on the suction port 4 side has increased. Therefore, the control valve 8 is moved to the suction port 4 side to change the suction port 4 side.
By reducing the opening area of No. 1, the amount of inflow from the suction port 4 is relatively decreased, and the fluctuation of viscosity is corrected (steps 410 and 411). Further, when η is equal to ηc, the position of the control valve 8 is kept as it is, and the current state is maintained (step 420).
Returning to 02, the above processing is repeated.

【0033】このように、前記内接形歯車ポンプ10の
調節弁8の位置を自動制御することで、混合液の粘度の
変動をも防止することができる。
As described above, by automatically controlling the position of the control valve 8 of the internal gear pump 10, it is possible to prevent the fluctuation of the viscosity of the mixed liquid.

【0034】なお、上述の実施形態は、いずれも、内接
形歯車ポンプ10が一つで、二つの原料液を混合する場
合を示したが、本発明の液混合装置及び方法は、前述の
実施形態の液混合装置1を多段に接続して、三種以上の
原料液を所望の比率で混合・移送するようにしてもよ
い。
In each of the above-mentioned embodiments, the number of the internal gear pumps 10 is one and two raw material liquids are mixed, but the liquid mixing apparatus and method of the present invention are the same as those described above. The liquid mixing apparatus 1 of the embodiment may be connected in multiple stages to mix and transfer three or more raw material liquids at a desired ratio.

【0035】[0035]

【発明の効果】本発明の液混合装置及び方法によれば、
内接形歯車ポンプを利用する方式で、該内接形歯車ポン
プを連続稼働させることにより、複数液の混合・移送処
理を連続的に実施でき、前記内接形歯車ポンプの稼働を
制御することで、処理量を任意量に調整することができ
る。また、内接形歯車ポンプを利用する方式のため、従
来のラインミキサーを利用する方式のものと比較する
と、装置をコンパクト化することができる。そして、運
用中に、原料タンク中の液面変化によるサクションヘッ
ドの変動や温度等の影響による原料液の粘度変化によっ
て、内接形歯車ポンプの各吸込口への原料液の流入比が
変化した場合には、それらのサクションヘッドの変動や
原料液の粘度変化に基づく原料液の流入比の変化の発生
は直ちに流量検知手段または粘度検出手段によって検知
され、これらの検知手段の検知信号に基づいて内接形歯
車ポンプの調節弁を操作する制御手段が、元の適性な混
合比率を維持すべく前記調節弁の位置を自動調整する。
したがって、運用中の混合比率の変動を防止し、高精度
の混合・移送を行うことができる。
According to the liquid mixing apparatus and method of the present invention,
By using the internal gear pump, by continuously operating the internal gear pump, it is possible to continuously carry out mixing and transfer processing of a plurality of liquids, and to control the operation of the internal gear pump. Thus, the processing amount can be adjusted to an arbitrary amount. Further, since the system uses the internal gear pump, the apparatus can be made compact as compared with the system using the conventional line mixer. Then, during operation, the inflow ratio of the raw material liquid to each suction port of the internal gear pump changed due to the fluctuation of the suction head due to the change of the liquid level in the raw material tank and the change of the viscosity of the raw material liquid due to the influence of temperature etc. In this case, the change in the suction head and the change in the inflow ratio of the raw material liquid due to the change in the viscosity of the raw material liquid are immediately detected by the flow rate detection means or the viscosity detection means, and based on the detection signals of these detection means. The control means for operating the control valve of the internal gear pump automatically adjusts the position of the control valve to maintain the original proper mixing ratio.
Therefore, it is possible to prevent fluctuations in the mixing ratio during operation and perform highly accurate mixing and transfer.

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

【図1】本発明の一実施形態に基づく液混合装置の概略
構成図である。
FIG. 1 is a schematic configuration diagram of a liquid mixing apparatus according to an embodiment of the present invention.

【図2】図1に示した液混合装置の動作説明図である。FIG. 2 is an operation explanatory view of the liquid mixing apparatus shown in FIG.

【図3】本発明に係る液混合装置における流量検知手段
の装備位置例の説明図である。
FIG. 3 is an explanatory view of an example of the equipment position of the flow rate detecting means in the liquid mixing apparatus according to the present invention.

【図4】図3(a)に示した構成の場合の動作説明図で
ある。
FIG. 4 is an operation explanatory diagram in the case of the configuration shown in FIG.

【図5】図3(b)に示した構成の場合の動作説明図で
ある。
FIG. 5 is an operation explanatory diagram in the case of the configuration shown in FIG.

【図6】本発明の他の実施形態に基づく液混合装置の概
略構成図である。
FIG. 6 is a schematic configuration diagram of a liquid mixing apparatus according to another embodiment of the present invention.

【図7】図6に示した構成の場合の動作説明図である。FIG. 7 is an operation explanatory diagram in the case of the configuration shown in FIG.

【符号の説明】[Explanation of symbols]

1 液混合装置 3,4 吸込口 6 吐出口 8 調節弁 10 内接形歯車ポンプ 12,13 原料液体 15,16 原料タンク 18,19,41 流量検知手段 21 制御手段 43 粘度検知手段 DESCRIPTION OF SYMBOLS 1 Liquid mixing device 3,4 Suction port 6 Discharge port 8 Control valve 10 Internal gear pump 12,13 Raw material liquid 15,16 Raw material tank 18,19,41 Flow rate detection means 21 Control means 43 Viscosity detection means

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 二つの吸込口及び一つの吐出口を有する
と共に、前記各吸込口の開口面積を変更して移送比率を
変更可能な調節弁を備えた内接形歯車ポンプと、 前記各吸込口側及び前記吐出口側の少なくとも二箇所に
配設された流量検知手段と、 前記流量検知手段の検知信号に基づいて前記調節弁を調
節し、複数液の移送比率を変更する制御手段とを備え、 複数液の移送・混合・移送比率の調節を行う液混合装
置。
1. An internal gear pump having two suction ports and one discharge port and having a control valve capable of changing a transfer ratio by changing an opening area of each suction port, and each suction. A flow rate detecting means arranged at least at two positions on the mouth side and the discharge side, and a control means for adjusting the adjusting valve based on a detection signal of the flow rate detecting means and changing a transfer ratio of a plurality of liquids. A liquid mixing device that is equipped and that controls the transfer / mixing / transfer ratio of multiple liquids.
【請求項2】 二つの吸込口及び一つの吐出口を有する
と共に、前記各吸込口の開口面積を変更して移送比率を
変更可能な調節弁を備えた内接形歯車ポンプと、 前記吐出口側に配設された粘度検出手段と、 前記粘度検出手段の検知信号に基づいて前記調節弁を調
節し、複数液の移送比率を変更する制御手段とを備え、 複数液の移送・混合・移送比率の調節を行う液混合装
置。
2. An internal gear pump having two suction ports and one discharge port and having a control valve capable of changing a transfer ratio by changing an opening area of each suction port, and the discharge port. And a control unit that adjusts the control valve based on a detection signal of the viscosity detection unit and changes the transfer ratio of a plurality of liquids. Liquid mixing device that adjusts the ratio.
【請求項3】 二つの吸込口及び一つの吐出口を有する
と共に、前記各吸込口の開口面積を変更して移送比率を
変更可能な調節弁を備えた内接形歯車ポンプにより、複
数液の移送・混合・移送比率の調節を行う液混合方法に
おいて、 前記各吸込口側及び前記吐出口側の少なくとも二箇所に
配設された流量検知手段の検知信号に基づいて前記調節
弁を調節し、複数液の移送比率の調節を行うことを特徴
とする液混合方法。
3. An internal gear pump having two suction ports and one discharge port and having a control valve capable of changing a transfer ratio by changing an opening area of each suction port, In a liquid mixing method of adjusting transfer / mixing / transfer ratio, the control valve is adjusted based on a detection signal of a flow rate detection unit disposed at at least two positions on each of the suction port side and the discharge port side, A liquid mixing method comprising adjusting the transfer ratio of a plurality of liquids.
【請求項4】 二つの吸込口及び一つの吐出口を有する
と共に、前記各吸込口の開口面積を変更して移送比率を
変更可能な調節弁を備えた内接形歯車ポンプにより、複
数液の移送・混合・移送比率の調節を行う液混合方法に
おいて、 前記吐出口側に配設された粘度検出手段の検知信号に基
づいて前記調節弁を調節し、所定粘度の混合液を得るこ
とを特徴とする液混合方法。
4. An internal gear pump having two suction ports and one discharge port and having a control valve capable of changing a transfer ratio by changing an opening area of each suction port, In a liquid mixing method of adjusting the transfer / mixing / transfer ratio, the adjusting valve is adjusted based on a detection signal of a viscosity detecting means arranged on the discharge port side to obtain a mixed liquid having a predetermined viscosity. And liquid mixing method.
JP08535896A 1996-04-08 1996-04-08 Liquid mixing apparatus and method Expired - Lifetime JP3976813B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP08535896A JP3976813B2 (en) 1996-04-08 1996-04-08 Liquid mixing apparatus and method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP08535896A JP3976813B2 (en) 1996-04-08 1996-04-08 Liquid mixing apparatus and method

Publications (2)

Publication Number Publication Date
JPH09271654A true JPH09271654A (en) 1997-10-21
JP3976813B2 JP3976813B2 (en) 2007-09-19

Family

ID=13856493

Family Applications (1)

Application Number Title Priority Date Filing Date
JP08535896A Expired - Lifetime JP3976813B2 (en) 1996-04-08 1996-04-08 Liquid mixing apparatus and method

Country Status (1)

Country Link
JP (1) JP3976813B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007532736A (en) * 2004-04-15 2007-11-15 ワッカー ケミー アクチエンゲゼルシャフト Method for continuously producing a silicone emulsion
JP2008525169A (en) * 2004-12-23 2008-07-17 キネマティカ アクチエンゲゼルシャフト Devices that disperse solid, liquid or gaseous substances within a liquid
JP2013544624A (en) * 2010-09-22 2013-12-19 ヘレウス メディカル ゲーエムベーハー Dispensing device that travels at the same rate, method for moving the flow at the same rate, and method for mixing miscible materials

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007532736A (en) * 2004-04-15 2007-11-15 ワッカー ケミー アクチエンゲゼルシャフト Method for continuously producing a silicone emulsion
JP2008525169A (en) * 2004-12-23 2008-07-17 キネマティカ アクチエンゲゼルシャフト Devices that disperse solid, liquid or gaseous substances within a liquid
JP4869250B2 (en) * 2004-12-23 2012-02-08 キネマティカ アクチエンゲゼルシャフト Devices that disperse solid, liquid or gaseous substances within a liquid
US8398294B2 (en) 2004-12-23 2013-03-19 Kinematica Ag Device for dispersing a solid, liquid or gaseous substance in a liquid
JP2013544624A (en) * 2010-09-22 2013-12-19 ヘレウス メディカル ゲーエムベーハー Dispensing device that travels at the same rate, method for moving the flow at the same rate, and method for mixing miscible materials
US9073020B2 (en) 2010-09-22 2015-07-07 Heraeus Medical Gmbh Synchronised dispensing device, method for synchronising flows, and method for mixing a mixable material

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