JPH06218246A - Flat membrane filter machine - Google Patents

Flat membrane filter machine

Info

Publication number
JPH06218246A
JPH06218246A JP2962993A JP2962993A JPH06218246A JP H06218246 A JPH06218246 A JP H06218246A JP 2962993 A JP2962993 A JP 2962993A JP 2962993 A JP2962993 A JP 2962993A JP H06218246 A JPH06218246 A JP H06218246A
Authority
JP
Japan
Prior art keywords
pressure vessel
stock solution
flat membrane
rotating
flat
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
JP2962993A
Other languages
Japanese (ja)
Inventor
Konosuke Matsushita
幸之助 松下
Hisashi Nogaki
久 野垣
Ikuo Itakura
郁夫 板倉
Masaki Kitamura
正樹 北村
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.)
Toto Ltd
Original Assignee
Toto 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 Toto Ltd filed Critical Toto Ltd
Priority to JP2962993A priority Critical patent/JPH06218246A/en
Publication of JPH06218246A publication Critical patent/JPH06218246A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To suppress an excessive load fluctuation of a motor for driving flat membranes and to obviate the generation of a variation in filtrate quality by providing a means for detecting the temp. of the original liquid in the outlet part of a pressure vessel and a means for controlling the rotating speed of the flat membranes in such a manner that the temp. of the original liquid in the outlet part of the pressure vessel does not exceed a prescribed value. CONSTITUTION:The rotary flat membrane filter machine which executes cross flow type filtration of the original liquid by rotating the flat membranes in the pressure vessel 11 is provided with a means 41 for detecting the temp. of the original liquid in the outlet part of the pressure vessel 11 and a means 13 for controlling the rotating speed of the flat membranes in such a manner that the temp. of the original liquid in the outlet part of the pressure vessel 11 does not exceed a prescribed value. Consequently, the flat membrane filter machine which can maintain the temp. of the original liquid in the pressure vessel at an adequate value at all times, can suppress the excessive load fluctuation of the motor 12 for driving the flat membranes according to the temp. control of the original liquid and does not generate the variation in the quality of the filtrate by a difference in the lots of the original liquids is obtd.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、食品製造、医薬品開
発、醗酵等の分野で用いられる平膜濾過機に関するもの
である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a flat membrane filter used in the fields of food production, drug development, fermentation and the like.

【0002】[0002]

【従来の技術】圧力容器中で平膜を回転させることによ
り原液のクロスフロー式濾過を行う回転平膜濾過機、及
び圧力容器内に平膜を固定し、前記圧力容器内で前記平
膜に平行な攪拌板を回転させることにより原液のクロス
フロー式濾過を行う固定平膜濾過機が従来から知られて
いる。平膜濾過機においては、回転する平膜或いは回転
する攪拌板と原液との間の摩擦により熱が発生する。摩
擦熱の発熱量は、濾過工程の進行に伴う原液の濃度上
昇、ひいては原液の粘度上昇と共に増加し、遂には平膜
濾過機が備える熱交換器の能力を上回る。この結果、圧
力容器内の原液の温度が、該原液の性状に悪影響を及ぼ
す程度にまで上昇する。従来の平膜濾過機においては、
作業員が圧力容器出口部の原液の温度を監視し、手動に
より平膜或いは攪拌板の回転数を制御して、圧力容器内
の原液の温度が所定値を超えないようにしていた。
2. Description of the Related Art A rotary flat membrane filter for performing cross-flow filtration of a stock solution by rotating a flat membrane in a pressure vessel, and a flat membrane fixed in a pressure vessel, and the flat membrane is fixed in the pressure vessel. 2. Description of the Related Art A fixed flat sheet membrane filtration machine that performs cross-flow type filtration of a stock solution by rotating parallel stirring plates has been conventionally known. In the flat sheet membrane filter, heat is generated by friction between the rotating flat sheet membrane or the rotating stirring plate and the stock solution. The calorific value of frictional heat increases as the concentration of the stock solution increases with the progress of the filtration process, and as the viscosity of the stock solution increases, and finally exceeds the capacity of the heat exchanger provided in the flat sheet membrane filter. As a result, the temperature of the stock solution in the pressure vessel rises to such an extent that the properties of the stock solution are adversely affected. In a conventional flat sheet membrane filter,
An operator monitors the temperature of the stock solution at the outlet of the pressure vessel and manually controls the rotation speed of the flat membrane or the stirring plate so that the temperature of the stock solution in the pressure vessel does not exceed a predetermined value.

【0003】[0003]

【発明が解決しようとする課題】従来の平膜濾過機にお
いては、手動により圧力容器内の原液の温度制御をして
いたので、原液の温度を常時適正値に維持することは困
難であった。また、手動により平膜或いは攪拌板の回転
数を制御していたので、平膜或いは攪拌板を駆動するモ
ータの負荷変動が大きくなりがちであった。特に高濃縮
運転時には原液粘度が急激に増大するため、手動による
回転数制御が間に合わず、定格値を超える電流が流れて
濾過機が停止するトラブルが発生するおそれがあった。
さらに、手動による原液の温度制御では、原液のロット
の相違による粘度のばらつきに対処できず、ロット毎に
透過液の品質が異なるという事態を招くおそれがあっ
た。本発明は上記問題に鑑みてなされたものであり、圧
力容器内の原液の温度を常に適正値に維持することがで
き、原液の温度制御にともなう平膜或いは攪拌板を駆動
するモータの過大な負荷変動を抑制でき、さらに原液の
ロットの相違による透過液の品質のばらつきを生じない
平膜濾過機を提供することを目的とする。
In the conventional flat sheet membrane filtration machine, since the temperature of the stock solution in the pressure vessel was manually controlled, it was difficult to always maintain the temperature of the stock solution at an appropriate value. . Further, since the rotation speed of the flat film or the stirring plate is manually controlled, the load fluctuation of the motor for driving the flat film or the stirring plate tends to be large. Particularly during high-concentration operation, the viscosity of the undiluted solution rapidly increases, so that manual rotation speed control cannot be performed in time, and there is a risk that a current that exceeds the rated value will flow and the filter will stop.
Further, manual temperature control of the stock solution cannot cope with variations in viscosity due to different lots of the stock solution, which may lead to a situation in which the quality of the permeated solution differs from lot to lot. The present invention has been made in view of the above problems, the temperature of the stock solution in the pressure vessel can always be maintained at an appropriate value, and the motor for driving the flat membrane or the stirring plate accompanying the temperature control of the stock solution is excessive. It is an object of the present invention to provide a flat sheet membrane filtration machine capable of suppressing load fluctuations and causing no variation in permeated liquid quality due to difference in stock solution lots.

【0004】[0004]

【課題を解決するための手段】上記課題を解決するため
に、本発明においては、圧力容器中で平膜を回転させる
ことにより原液のクロスフロー式濾過を行う回転平膜濾
過機において、圧力容器出口部の原液の温度を検出する
手段と、圧力容器出口部の原液の温度が所定値を超えな
いように平膜の回転数を制御する手段とを備える回転平
膜濾過機を提供する。また、本発明においては、圧力容
器内に平膜を固定し、前記圧力容器内で前記平膜に平行
な攪拌板を回転させることにより原液のクロスフロー式
濾過を行う固定平膜濾過機において、圧力容器出口部の
原液の温度を検出する手段と、圧力容器出口部の原液の
温度が所定値を超えないように攪拌板の回転数を制御す
る手段とを備える固定平膜濾過機を提供する。圧力容器
出口部の原液の温度を検出する手段と、圧力容器出口部
の原液の温度が所定値を超えないように平膜または攪拌
板の回転数を制御する手段とに代えて、平膜または攪拌
板を回転させるためのモータのトルクを検出する手段
と、平膜または攪拌板を回転させるためのモータのトル
クが所定値を超えないように平膜または攪拌板の回転数
を制御する手段とを設けても良く、或いは、平膜または
攪拌板を回転させるためのモータの消費電力を検出する
手段と、平膜または攪拌板を回転させるためのモータの
消費電力が所定値を超えないように平膜または攪拌板の
回転数を制御する手段とを設けても良い。
In order to solve the above-mentioned problems, in the present invention, in a rotary flat membrane filter for performing cross-flow filtration of a stock solution by rotating a flat membrane in a pressure vessel, a pressure vessel Provided is a rotary flat sheet membrane filtration device comprising means for detecting the temperature of the stock solution at the outlet and means for controlling the rotation speed of the flat membrane so that the temperature of the stock solution at the outlet of the pressure vessel does not exceed a predetermined value. Further, in the present invention, a flat membrane filter is fixed in a pressure vessel, and a fixed flat membrane filter for performing cross-flow filtration of a stock solution by rotating a stirring plate parallel to the flat membrane in the pressure vessel, (EN) Provided is a fixed flat membrane filter equipped with means for detecting the temperature of the stock solution at the outlet of the pressure vessel and means for controlling the rotation speed of the stirring plate so that the temperature of the stock solution at the outlet of the pressure vessel does not exceed a predetermined value. . Instead of the means for detecting the temperature of the stock solution at the outlet of the pressure vessel and the means for controlling the rotation speed of the flat plate or stirring plate so that the temperature of the stock solution at the outlet of the pressure vessel does not exceed a predetermined value, a flat film or A means for detecting the torque of the motor for rotating the stirring plate, and a means for controlling the rotation speed of the flat film or the stirring plate so that the torque of the motor for rotating the flat film or stirring plate does not exceed a predetermined value. May be provided, or a means for detecting the power consumption of the motor for rotating the flat film or the stirring plate and the power consumption of the motor for rotating the flat film or the stirring plate should not exceed a predetermined value. A means for controlling the rotation speed of the flat film or the stirring plate may be provided.

【0005】[0005]

【作用】本発明にあっては、回転平膜濾過機または固定
平膜濾過機は、それぞれ、圧力容器出口部の原液の温度
を検出する手段と、圧力容器出口部の原液の温度が所定
値を超えないように平膜または攪拌板の回転数を制御す
る手段とを備えているので、圧力容器内の原液の温度
は、人手に頼ることなく、自動的に適正値に維持され
る。平膜または攪拌板を回転させるためのモータのトル
クを検出する手段と、平膜または攪拌板を回転させるた
めのモータのトルクが所定値を超えないように平膜また
は攪拌板の回転数を制御する手段と設けることにより、
或いは平膜または攪拌板を回転させるためのモータの消
費電力を検出する手段と、平膜または攪拌板を回転させ
るためのモータの消費電力が所定値を超えないように平
膜または攪拌板の回転数を制御する手段とを設けること
により、前記と同様に、圧力容器内の原液の温度を、人
手に頼ることなく自動的に適正値に維持することができ
る。
According to the present invention, the rotary flat membrane filter or the fixed flat membrane filter has means for detecting the temperature of the stock solution at the outlet of the pressure vessel and the temperature of the stock solution at the outlet of the pressure vessel to a predetermined value. Therefore, the temperature of the stock solution in the pressure vessel is automatically maintained at an appropriate value without relying on human hands. Means for detecting the torque of the motor for rotating the flat film or stirring plate, and controlling the rotation speed of the flat film or stirring plate so that the torque of the motor for rotating the flat film or stirring plate does not exceed a predetermined value. By providing a means to
Alternatively, a means for detecting the power consumption of the motor for rotating the flat film or the stirring plate and a rotation of the flat film or the stirring plate so that the power consumption of the motor for rotating the flat film or the stirring plate does not exceed a predetermined value. By providing the means for controlling the number, similarly to the above, the temperature of the stock solution in the pressure vessel can be automatically maintained at an appropriate value without relying on human hands.

【0006】[0006]

【実施例】本発明の実施例に係る固定平膜濾過機を以下
に説明する。図1に示すように、本発明の実施例に係る
固定平膜濾過機は、固定平膜モジュール10を備えてい
る。固定平膜モジュール10は、図示しない円環板状の
セラミック製固定平膜と、前記固定平膜に平行な図示し
ない攪拌板とを内蔵する圧力容器11と、攪拌板を回転
駆動するモータ12と、モータ12の回転数を制御する
インバータ13とを有している。濾過対象液である原液
を貯蔵する原液タンク20には、その下部外表面に、熱
交換用のジャケット21が取り付けられている。原液タ
ンク20の内部には、熱交換促進用の攪拌機22が配設
されている。
EXAMPLE A fixed flat sheet membrane filter according to an example of the present invention will be described below. As shown in FIG. 1, the fixed flat sheet membrane filter according to the embodiment of the present invention includes a fixed flat sheet membrane module 10. The fixed flat membrane module 10 includes a pressure vessel 11 containing a circular fixed circular plate-shaped ceramic fixed flat membrane (not shown), a stirring plate (not shown) parallel to the fixed flat membrane, and a motor 12 for rotating the stirring plate. , And an inverter 13 for controlling the rotation speed of the motor 12. A stock solution tank 20 for storing a stock solution which is a liquid to be filtered is provided with a jacket 21 for heat exchange on an outer surface of a lower portion thereof. Inside the stock solution tank 20, a stirrer 22 for accelerating heat exchange is arranged.

【0007】原液タンク20の下端部は、配管30を介
して圧力容器11の下端部に連通している。配管30の
途上には、循環ポンプ31が配設されている。原液タン
ク20の上端部は、配管40を介して圧力容器11の上
端部に連通している。配管40の途上には、圧力容器1
1の近傍部位に温度センサー41と、圧力センサー・コ
ントローラー42と、圧力調整弁43とが配設されてい
る。圧力容器に内蔵されたセラミック製固定平膜は、配
管50を介して図示しない透過液貯蔵タンクに連通して
いる。インバータ13の作動はコントロールユニット6
0により制御される。コントロールユニット60には、
温度センサー41からの温度信号が入力され、コントロ
ールユニット60からはインバータ13に制御信号が出
力される。コントロールユニット60には、温度センサ
ー41からの温度信号に基づいてインバータ13の作動
をフィードバッグ制御するフィードバック制御回路が組
み込まれている。
The lower end of the stock solution tank 20 communicates with the lower end of the pressure vessel 11 via a pipe 30. A circulation pump 31 is provided in the middle of the pipe 30. The upper end of the stock solution tank 20 communicates with the upper end of the pressure vessel 11 via a pipe 40. On the way of the pipe 40, the pressure vessel 1
A temperature sensor 41, a pressure sensor controller 42, and a pressure adjusting valve 43 are arranged in the vicinity of 1. The ceramic fixed flat membrane contained in the pressure vessel communicates with a permeate storage tank (not shown) via a pipe 50. The operation of the inverter 13 is the control unit 6
Controlled by 0. The control unit 60 has
The temperature signal from the temperature sensor 41 is input, and the control unit 60 outputs a control signal to the inverter 13. The control unit 60 incorporates a feedback control circuit that feed-back controls the operation of the inverter 13 based on the temperature signal from the temperature sensor 41.

【0008】上記構成を有する本実施例に係る固定平膜
濾過機の作動を説明する。原液タンク20内に貯蔵され
た原液が、循環ポンプ31の作動により、配管30を介
して圧力容器11に供給される。インバータ13の制御
の下にモータ12が所定回転数で回転し、圧力容器11
に内蔵された攪拌板が所定回転数で回転する。これによ
り圧力容器11内の原液が攪拌され、圧力容器11に内
蔵されたセラミック製固定平膜により原液がクロスフロ
ー濾過される。透過液は配管50を介して図示しない透
過液貯蔵タンクに送られる。濃縮された原液は、配管4
0を介して原液貯蔵タンクに戻される。原液は、原液タ
ンク20、配管30、圧力容器11、配管40で構成さ
れる閉回路内を循環し、所望の濃度まで濃縮される。圧
力調整弁43が圧力センサー・コントローラー42によ
りフィードバック制御されることにより、圧力容器11
内の原液の圧力、ひいてはセラミック製固定平膜の膜間
差圧が適正値に維持される。図示しない冷却水供給源か
らジャケット21に供給された冷却水と、原液タンク2
0内の原液との間の熱交換により、原液が冷却される。
攪拌機22の作動により、冷却水と原液との間の熱交換
が促進される。
The operation of the fixed flat sheet membrane filter according to this embodiment having the above structure will be described. The stock solution stored in the stock solution tank 20 is supplied to the pressure vessel 11 via the pipe 30 by the operation of the circulation pump 31. Under the control of the inverter 13, the motor 12 rotates at a predetermined rotation speed,
The stirrer plate built into the machine rotates at a predetermined speed. As a result, the stock solution in the pressure vessel 11 is agitated, and the stock solution is cross-flow filtered by the ceramic fixed flat membrane contained in the pressure vessel 11. The permeated liquid is sent to a permeated liquid storage tank (not shown) through the pipe 50. The concentrated stock solution is pipe 4
It is returned to the stock solution storage tank via 0. The stock solution circulates in a closed circuit composed of the stock solution tank 20, the pipe 30, the pressure vessel 11, and the pipe 40, and is concentrated to a desired concentration. The pressure control valve 43 is feedback-controlled by the pressure sensor controller 42 so that the pressure vessel 11
The pressure of the undiluted solution in the liquid, and eventually the transmembrane pressure difference of the ceramic fixed flat membrane, is maintained at an appropriate value. Cooling water supplied to the jacket 21 from a cooling water supply source (not shown) and the stock solution tank 2
The stock solution is cooled by heat exchange with the stock solution in 0.
The operation of the stirrer 22 promotes heat exchange between the cooling water and the stock solution.

【0009】インバータ13の作動、ひいてはモータ1
2及び圧力容器11に内蔵された攪拌板の回転数は、温
度センサー41からの温度信号に基づき、コントロール
ユニット60により、温度センサー41が設置された部
位における配管40内の原液の温度、すなわち圧力容器
11の出口部の原液の温度が所定値を超えないようにフ
ィードバック制御される。これにより、圧力容器11内
の原液の温度は常に適正値に維持される。短い時間間隔
で最適制御が繰り返されるので、圧力容器11内の原液
の温度制御に伴いモータ12の負荷が大きく変動するお
それは無い。また、仮に運転時に原液粘度が急激に増大
しても、モータ12に定格値を超える電流が流れるおそ
れは無く、従って固定平膜モジュール10が停止するお
それも無い。さらに、原液のロットの相違により透過液
に品質のばらつきを生ずるおそれも無い。
The operation of the inverter 13, and thus the motor 1
2 and the number of rotations of the stirring plate built in the pressure vessel 11 are based on the temperature signal from the temperature sensor 41, and the control unit 60 controls the temperature of the stock solution in the pipe 40 at the position where the temperature sensor 41 is installed, that is, the pressure. Feedback control is performed so that the temperature of the stock solution at the outlet of the container 11 does not exceed a predetermined value. As a result, the temperature of the stock solution in the pressure vessel 11 is always maintained at an appropriate value. Since the optimum control is repeated at short time intervals, there is no possibility that the load on the motor 12 will greatly change due to the temperature control of the stock solution in the pressure vessel 11. Further, even if the stock solution viscosity suddenly increases during operation, there is no possibility that a current exceeding the rated value will flow in the motor 12, and therefore the fixed flat sheet membrane module 10 will not stop. Further, there is no possibility that the quality of the permeated liquid varies due to the difference in lots of the stock solution.

【0010】攪拌板と原液との摩擦による発熱量とモー
タ13のトルクとの間に一定の相関があることに鑑みる
と、図1で一点鎖線で示すように、インバータ13が備
えるトルクメータ13aからのトルク信号、すなわちモ
ータ12のトルクを表示する信号をコントロールユニッ
ト60に入力し、前記トルク信号に基づいてインバータ
13、ひいてはモータ12の回転数をフィードバック制
御することによっても、圧力容器11内の原液の温度を
適正値に維持することができる。また、攪拌板と原液と
の摩擦による発熱量とモータ13の消費電力との間に一
定の相関があることに鑑みると、図1で二点鎖線で示す
ように、インバータ13が備える消費電力メータ13b
からの消費電力信号、すなわちモータ12の消費電力を
表示する信号をコントロールユニット60に入力し、前
記消費電力信号に基づいてインバータ13、ひいてはモ
ータ12の回転数をフィードバック制御することによっ
ても、圧力容器11内の原液の温度を適正値に維持する
ことができる。以上、固定平膜濾過機に着目して本発明
を説明したが、本発明は回転平膜濾過機にも適用できる
ことはいうまでもない。回転平膜濾過機においては、平
膜の回転数がフィードバック制御される。
Considering that there is a constant correlation between the amount of heat generated by the friction between the stirring plate and the stock solution and the torque of the motor 13, as shown by the alternate long and short dash line in FIG. Of the stock solution in the pressure vessel 11 by inputting a torque signal of the motor 12, that is, a signal indicating the torque of the motor 12 to the control unit 60 and performing feedback control of the rotation speed of the inverter 13, and thus the motor 12, based on the torque signal. The temperature of can be maintained at an appropriate value. Further, considering that there is a certain correlation between the amount of heat generated by the friction between the stirring plate and the stock solution and the power consumption of the motor 13, as shown by the chain double-dashed line in FIG. 13b
The power consumption signal from the pressure vessel, that is, a signal indicating the power consumption of the motor 12 is input to the control unit 60, and the rotation speed of the inverter 13 and the motor 12 is feedback-controlled based on the power consumption signal. The temperature of the stock solution in 11 can be maintained at an appropriate value. Although the present invention has been described above with a focus on the fixed flat sheet membrane filter, it goes without saying that the present invention can also be applied to a rotary flat sheet membrane filter. In a rotary flat membrane filter, the rotation speed of the flat membrane is feedback-controlled.

【0011】[0011]

【効果】以上説明したごとく、本発明においては、回転
平膜濾過機または固定平膜濾過機は、それぞれ、圧力容
器出口部の原液の温度を検出する手段と、圧力容器出口
部の原液の温度が所定値を超えないように平膜または攪
拌板の回転数を制御する手段とを備えているので、圧力
容器内の原液の温度は、人手に頼ることなく、自動的に
適正値に維持される。短い時間間隔で最適制御が繰り返
されるので、原液の温度制御に伴い平膜或いは攪拌板を
駆動するモータの負荷が大きく変動するおそれは無い。
また、運転時に原液粘度が急激に増大しても、平膜或い
は攪拌板を駆動するモータに定格値を超える電流が流れ
るおそれは無く、従って濾過機が停止するおそれも無
い。さらに、原液のロットの相違により透過液に品質の
ばらつきを生ずるおそれも無い。
As described above, in the present invention, the rotary flat membrane filter or the fixed flat membrane filter respectively has a means for detecting the temperature of the stock solution at the outlet of the pressure vessel and the temperature of the stock solution at the outlet of the pressure vessel. The temperature of the stock solution in the pressure vessel is automatically maintained at an appropriate value without relying on human hands, as it is equipped with means for controlling the rotation speed of the flat membrane or stirring plate so that the temperature does not exceed a predetermined value. It Since the optimum control is repeated at short time intervals, there is no possibility that the load of the motor that drives the flat membrane or the stirring plate will change significantly with the temperature control of the stock solution.
Further, even if the viscosity of the stock solution rapidly increases during operation, there is no possibility that an electric current exceeding the rated value will flow to the motor that drives the flat membrane or the stirring plate, and therefore the filter will not stop. Further, there is no possibility that the quality of the permeated liquid varies due to the difference in lots of the stock solution.

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

【図1】本発明の実施例に係る固定平膜濾過機の全体構
成図である。
FIG. 1 is an overall configuration diagram of a fixed flat sheet membrane filtering machine according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

10 固定平膜モジュール 11 圧力容器 12 モータ 13 インバータ 13a トルクメータ 13b 消費電力メータ 20 原液タンク 21 ジャケット 22 攪拌機 30 配管 31 循環ポンプ 40 配管 41 温度センサー 60 コントロールユニット 10 Fixed Flat Membrane Module 11 Pressure Vessel 12 Motor 13 Inverter 13a Torque Meter 13b Power Consumption Meter 20 Undiluted Liquid Tank 21 Jacket 22 Stirrer 30 Piping 31 Circulation Pump 40 Piping 41 Temperature Sensor 60 Control Unit

───────────────────────────────────────────────────── フロントページの続き (72)発明者 板倉 郁夫 北九州市小倉北区中島2丁目1番1号 東 陶機器株式会社内 (72)発明者 北村 正樹 北九州市小倉北区中島2丁目1番1号 東 陶機器株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Ikuo Itakura 2-1-1 Nakajima, Kokurakita-ku, Kitakyushu City In Totokiki Co., Ltd. (72) Masaki Kitamura 2-1-1 Nakajima, Kokurakita-ku, Kitakyushu No. Totoki Equipment Co., Ltd.

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 圧力容器中で平膜を回転させることによ
り原液のクロスフロー式濾過を行う回転平膜濾過機にお
いて、圧力容器出口部の原液の温度を検出する手段と、
圧力容器出口部の原液の温度が所定値を超えないように
平膜の回転数を制御する手段とを備える回転平膜濾過
機。
1. A rotary flat membrane filter for performing cross-flow filtration of a stock solution by rotating a flat membrane in a pressure container, and means for detecting the temperature of the stock solution at the outlet of the pressure container,
And a means for controlling the rotation speed of the flat sheet membrane so that the temperature of the stock solution at the outlet of the pressure vessel does not exceed a predetermined value.
【請求項2】 圧力容器中で平膜を回転させることによ
り原液のクロスフロー式濾過を行う回転平膜濾過機にお
いて、平膜を回転させるためのモータのトルクを検出す
る手段と、平膜を回転させるためのモータのトルクが所
定値を超えないように平膜の回転数を制御する手段とを
備える回転平膜濾過機。
2. A rotary flat membrane filter for performing cross-flow filtration of a stock solution by rotating a flat membrane in a pressure vessel, a means for detecting a torque of a motor for rotating the flat membrane, and a flat membrane. And a means for controlling the number of rotations of the flat membrane so that the torque of the motor for rotating does not exceed a predetermined value.
【請求項3】 圧力容器中で平膜を回転させることによ
り原液のクロスフロー式濾過を行う回転平膜濾過機にお
いて、平膜を回転させるためのモータの消費電力を検出
する手段と、平膜を回転させるためのモータの消費電力
が所定値を超えないように平膜の回転数を制御する手段
とを備える回転平膜濾過機。
3. A rotary flat membrane filter for performing cross-flow filtration of a stock solution by rotating a flat membrane in a pressure vessel, a means for detecting power consumption of a motor for rotating the flat membrane, and a flat membrane. And a means for controlling the rotation speed of the flat membrane so that the power consumption of the motor for rotating the flat membrane does not exceed a predetermined value.
【請求項4】 圧力容器内に平膜を固定し、前記圧力容
器内で前記平膜に平行な攪拌板を回転させることにより
原液のクロスフロー式濾過を行う固定平膜濾過機におい
て、圧力容器出口部の原液の温度を検出する手段と、圧
力容器出口部の原液の温度が所定値を超えないように攪
拌板の回転数を制御する手段とを備える固定平膜濾過
機。
4. A stationary flat sheet membrane filter for fixing a flat sheet membrane in a pressure vessel, and rotating a stirring plate parallel to the flat sheet membrane in the pressure vessel to carry out cross-flow filtration of the stock solution. A fixed flat sheet membrane filter equipped with means for detecting the temperature of the stock solution at the outlet and means for controlling the rotation speed of the stirring plate so that the temperature of the stock solution at the outlet of the pressure vessel does not exceed a predetermined value.
【請求項5】 圧力容器内に平膜を固定し、前記圧力容
器内で前記平膜に平行な攪拌板を回転させることにより
原液のクロスフロー式濾過を行う固定平膜濾過機におい
て、攪拌板を回転させるためのモータのトルクを検出す
る手段と、攪拌板を回転させるためのモータのトルクが
所定値を超えないように攪拌板の回転数を制御する手段
とを備える固定平膜濾過機。
5. A fixed flat membrane filter for fixing a flat membrane in a pressure vessel, and rotating a stirring plate parallel to the flat membrane in the pressure vessel to perform cross-flow type filtration of the stock solution. A fixed flat sheet membrane filtering machine comprising means for detecting a torque of a motor for rotating the stirring plate, and means for controlling a rotation speed of the stirring plate so that a torque of the motor for rotating the stirring plate does not exceed a predetermined value.
【請求項6】 圧力容器内に平膜を固定し、前記圧力容
器内で前記平膜に平行な攪拌板を回転させることにより
原液のクロスフロー式濾過を行う固定平膜濾過機におい
て、攪拌板を回転させるためのモータの消費電力を検出
する手段と、攪拌板を回転させるためのモータの消費電
力が所定値を超えないように攪拌板の回転数を制御する
手段とを備える固定平膜濾過機。
6. A fixed flat membrane filter for performing cross-flow filtration of a stock solution by fixing a flat membrane in a pressure vessel and rotating a stirring plate parallel to the flat membrane in the pressure vessel. Fixed flat membrane filtration provided with means for detecting the power consumption of the motor for rotating the stirring plate and means for controlling the rotation speed of the stirring plate so that the power consumption of the motor for rotating the stirring plate does not exceed a predetermined value. Machine.
JP2962993A 1993-01-27 1993-01-27 Flat membrane filter machine Pending JPH06218246A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2962993A JPH06218246A (en) 1993-01-27 1993-01-27 Flat membrane filter machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2962993A JPH06218246A (en) 1993-01-27 1993-01-27 Flat membrane filter machine

Publications (1)

Publication Number Publication Date
JPH06218246A true JPH06218246A (en) 1994-08-09

Family

ID=12281384

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2962993A Pending JPH06218246A (en) 1993-01-27 1993-01-27 Flat membrane filter machine

Country Status (1)

Country Link
JP (1) JPH06218246A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108414000A (en) * 2017-12-29 2018-08-17 北京清大国华环境股份有限公司 A kind of quality determining method of flat film product, system, storage medium and equipment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108414000A (en) * 2017-12-29 2018-08-17 北京清大国华环境股份有限公司 A kind of quality determining method of flat film product, system, storage medium and equipment

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