JPS6150607A - Separation apparatus by chromatography - Google Patents

Separation apparatus by chromatography

Info

Publication number
JPS6150607A
JPS6150607A JP59169106A JP16910684A JPS6150607A JP S6150607 A JPS6150607 A JP S6150607A JP 59169106 A JP59169106 A JP 59169106A JP 16910684 A JP16910684 A JP 16910684A JP S6150607 A JPS6150607 A JP S6150607A
Authority
JP
Japan
Prior art keywords
column
recovery
valve
amount
liquid
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
JP59169106A
Other languages
Japanese (ja)
Other versions
JPH0620489B2 (en
Inventor
Nobuhiro Oda
信博 織田
Hiroshi Morita
博志 森田
Nobuhiro Matsushita
松下 聿宏
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries 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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP59169106A priority Critical patent/JPH0620489B2/en
Publication of JPS6150607A publication Critical patent/JPS6150607A/en
Publication of JPH0620489B2 publication Critical patent/JPH0620489B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To automatically perform separating opertion so as to always obtain a predetermined recovery ratio, by performing the termination of recovery when the recovery ratio of the objective component flowed out from a column reaches the objective value or more. CONSTITUTION:An objective recovery ratio is inputted to an operation control part by an input device 12. Subsequently, a valve V1 is closed and a valve V2 is opened to flow solution to be separated to a separation agent packed column 6 while the valve V1 is opened and the valve V2 is closed to flow an eluate to the column 6. A valve V3 is closed and a valve V4 is opened and the recovery amount of the objective component flowed out from the column 6 is operated on the basis of the product of the outputs from a flow meter 4 and a concn. detector 7 and the elapse time and outlet concn. from the start point of the flow of the eluate by the operation control part 11. This calculated recovery ratio is compared with the recovery objective amount calculated from a preset recovery ratio and, at the point when the calculated recovery amount reaches the objective value or more, the valve V3 is opened and the valve V4 is closed to finish recovery.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は分離用充填剤を内蔵するカラムを用いたクロマ
トグラフィー(以下クロマトグラフィーという。)によ
る分離装置に関するものであり、詳しくは、予め設定さ
れた回収率となるように回収画分と非回収画分との境界
を判定し、この判定結果に基き回収画分と非回収画分と
を分取する手段を制御するよう構成したクロマトグラフ
ィーによる分離装置に関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a separation device by chromatography (hereinafter referred to as chromatography) using a column containing a separation packing material. A chromatography device configured to determine the boundary between the recovered fraction and the non-recovered fraction so that the recovery rate is determined, and to control means for separating the recovered fraction and the non-recovered fraction based on the determination result. The present invention relates to a separation device according to the present invention.

[従来の技術] クロマトグラフィーは、可溶性物質を分離、精製する目
的で用いられ、製薬、食品、精密化学等の分野における
工業的規模での分離、精製に応用されている。
[Prior Art] Chromatography is used for the purpose of separating and purifying soluble substances, and is applied to separation and purification on an industrial scale in fields such as pharmaceuticals, foods, and fine chemistry.

このクロマトグラフィーによる分離装置においては、回
収画分(カラムから流出する液における。目的成分を含
有する回収部分)と非回収画分(目的成分が少ないか又
は実質的に含有しない部分)とを適確に判別し、分取す
ることが重要である。
In this chromatographic separation device, the recovered fraction (the recovered portion containing the target component in the liquid flowing out from the column) and the non-recovered fraction (the portion containing little or substantially no target component) are separated. It is important to accurately identify and separate.

従来のクロマトグラフィーによる分離装置において、分
離用カラムから排出される液の回収画分と非回収画分と
の境界を検知する方法としては、 ■ 予め目的成分の純品を、試料溶液の分離操作と同じ
条件でカラムに流してそのリテンションタイムを知り、
このリテンションタイム付近をタイマにて判断する、 ■ 目的成分がその他の成分と完全に分離されているよ
うな条件では、その目的成分のリテンションタイムに基
いて判断する、 ■ 分離度が低くとも良い試料については、経験的に認
められたリテンションタイムとなるようタイマ管理する
、 等の方法が行なわれている。
In a conventional chromatographic separation device, the method for detecting the boundary between the recovered fraction and the non-recovered fraction of the liquid discharged from the separation column is as follows: Run it through the column under the same conditions as and find out its retention time.
Judge around this retention time using a timer. ■ Under conditions where the target component is completely separated from other components, judge based on the retention time of the target component. ■ Samples that are good even if the degree of separation is low. For this purpose, methods such as timer management are used to maintain empirically recognized retention times.

[発明が解決しようとする問題点] しかし上記従来の方法では、いずれも、試料を分離カラ
ムに導入してからの経過時間のみを判断しており、pH
1塩類濃度、温度、流量等の分離条件が分離操作中に変
化した場合であっても、その変化前に設定された条件で
しか運転ができず。
[Problems to be solved by the invention] However, in all of the above conventional methods, only the elapsed time since the sample was introduced into the separation column is determined, and the pH
1. Even if separation conditions such as salt concentration, temperature, flow rate, etc. change during separation operation, operation can only be performed under the conditions set before the change.

変化に対応できない。そのため、回収画分の回収率を一
定に保つことは困難であった。
Unable to respond to change. Therefore, it was difficult to keep the recovery rate of the recovered fraction constant.

c問題点を解決するための手段] 上記問題点を解決するために、本発明は、分離用充填剤
を内蔵したカラムに被分離液及び溶離液を供給し、この
方ラムを通すことにより回収画分と非回収画分とを分離
するようにした装置において、予め目的成分の目標回収
率を設定する。そして、演算制御器で、カラムに導入さ
れる目的成分の総量とこの目標回収率とから目的成分の
回収目標量を演算する。また、カラムへの液の導入量と
、カラムから排出される液中の目的成分濃度を演算制御
器に入力する。演算制御器では、入力データに基き、カ
ラムからの目的成分の流出量を演算して、その時点まで
の回収量を演算(積算)すると共に、演算された回収量
を目標回収量と比較し、実際の回収量が回収目標差以上
になった時点で、カラムに後続して設置された回収画分
と非回収画分とを分取する手段を切換えるよう構成した
ものである。
c. Means for Solving Problems] In order to solve the above problems, the present invention provides a solution to be separated and an eluent that are supplied to a column containing a separation packing material, and are passed through the column to collect the collected fraction. In an apparatus designed to separate fractions and unrecovered fractions, a target recovery rate of the target component is set in advance. Then, the arithmetic controller calculates the target amount of the target component to be recovered from the total amount of the target component introduced into the column and this target recovery rate. Further, the amount of liquid introduced into the column and the target component concentration in the liquid discharged from the column are input to the arithmetic controller. The arithmetic controller calculates the flow rate of the target component from the column based on the input data, calculates (integrates) the amount recovered up to that point, and compares the calculated recovery amount with the target recovery amount. When the actual recovery amount exceeds the target recovery difference, the means for separating the recovered fraction and the non-recovered fraction installed subsequent to the column is switched.

即ち、本発明は、 分離用充填剤を内蔵したカラムと、分離目的成分を含む
被分離液と溶離液とを該カラムに供給する手段と、該カ
ラムから排出される液を分取する手段と、前記カラムの
入口及び出口のうち少なくとも出口に設けられた液中の
目的成分濃度を検出する濃度検出器と、前記カラムへの
被分離液の流入量を検出する流量検出手段と、前記濃度
検出器及び流量検出手段の出力が入力され、これに基い
てカラムからの目的成分流出量を演算すると共に、目的
成分のカラムへの総流入量と予め設定された回収率とか
ら目的成分の回収目標量を演算し、目的成分流出量が回
収目標量以上になったときに前記分取手段を切替制御す
る演算制御器と、からなるクロマトグラフィーによる分
離装置、を要旨とするものである。
That is, the present invention comprises a column containing a separation packing material, a means for supplying a liquid to be separated and an eluent containing target components to the column, and a means for fractionating the liquid discharged from the column. , a concentration detector for detecting the concentration of a target component in a liquid, which is provided at least at an inlet and an outlet of the column, a flow rate detection means for detecting an inflow amount of the liquid to be separated into the column, and the concentration detection means. The output of the device and the flow rate detection means are input, and based on this, the flow rate of the target component from the column is calculated, and the recovery target of the target component is calculated from the total flow rate of the target component into the column and the preset recovery rate. The gist of the invention is a chromatographic separation device comprising: a calculation controller that calculates the amount of the target component flowing out and switches and controls the separation means when the amount of the target component flowing out exceeds the target amount of collection.

本発明において流量検出手段としては、流量計を用いて
も良いが、カラムへの液供給装置として定量ポンプを用
いた場合には、この定量ポンプ吐出量をもって流量デー
タとし、これを演算制御器に入力させるようにしても良
い。
In the present invention, a flow meter may be used as the flow rate detection means, but if a metering pump is used as the liquid supply device to the column, the metering pump discharge amount is used as flow rate data, and this is sent to the arithmetic controller. You may also be asked to input it.

また、本発明においては、濃度検出器はカラムの出口側
にのみ設けても良く、入口側、出口側の両方に設けても
良い。
Further, in the present invention, the concentration detector may be provided only on the outlet side of the column, or may be provided on both the inlet side and the outlet side.

入口側の濃度検出器を省略する場合には、被分離液中の
目的成分濃度は、予め自動又は手動にて分析しておき、
この分析結果を演算制御器に入力しておく。
If the concentration detector on the inlet side is omitted, the concentration of the target component in the liquid to be separated should be analyzed automatically or manually in advance.
The results of this analysis are input into the arithmetic controller.

本発明において、分離用充填剤としては、従来公知の各
種のもの、例えば、シリカゲル、アルミナ、イオン交換
樹脂、活性体等のいずれをも採用できる。
In the present invention, as the separation filler, any of various conventionally known fillers such as silica gel, alumina, ion exchange resins, active materials, etc. can be employed.

[作用] このような本発明によれば、カラムから流出する目的成
分の回収率((その時点までの目的成分の流出量)/(
カラムに導入された目的成分の総量))を検出しながら
分離操作を行ない、予め設定された回収率となるように
、自動的に分取手段の流路切替が行なわれる。
[Operation] According to the present invention, the recovery rate of the target component flowing out from the column ((amount of target component flowing out up to that point)/(
The separation operation is performed while detecting the total amount of the target component introduced into the column, and the flow path of the separation means is automatically switched to achieve a preset recovery rate.

[実施例] 以下図面を参照して実施例について説明する。[Example] Examples will be described below with reference to the drawings.

第1図は本発明の実施例に係るクロマトグラフィーによ
る分離装置の系統図である。
FIG. 1 is a system diagram of a chromatographic separation apparatus according to an embodiment of the present invention.

1は溶離液貯槽であって、送液ポンプ3、流量計4及び
入口側の濃度検出器5がこの順に設置された配管21を
介して分離剤充填カラム6に接続されている。
Reference numeral 1 denotes an eluent storage tank, which is connected to a separation agent-filled column 6 through a pipe 21 in which a liquid feed pump 3, a flow meter 4, and a concentration detector 5 on the inlet side are installed in this order.

また2は被分離液貯槽であって、配管22を介して溶離
液貯槽lとポンプ3との間の部分に接続されている。V
l、V2は、それぞれ、溶離液貯槽1及び被分離液貯槽
2の液流出側に設けられたバルブである。
Reference numeral 2 denotes a liquid storage tank to be separated, which is connected to a portion between the eluent storage tank l and the pump 3 via a pipe 22. V
1 and V2 are valves provided on the liquid outflow sides of the eluent storage tank 1 and the liquid to be separated storage tank 2, respectively.

分離剤充填カラム6の出口側には1分取手段8に接続す
るための配管23が設けられており、この配管23の途
中には出口側の濃度検出器7が設−けられている。
A piping 23 for connecting to the one-separation means 8 is provided on the exit side of the separating agent-filled column 6, and a concentration detector 7 on the exit side is provided in the middle of this piping 23.

分取手段8の構成について説明すると、配管23の後流
部分が配管24.25に分岐しており、配管24には非
回収画分出口バルブv3が設けられ、配管25には回収
画分出口バルブv4が設けられ、その下流側に回収画分
回収槽9が設けられている。
To explain the configuration of the fractionation means 8, the downstream part of the pipe 23 branches into pipes 24 and 25, the pipe 24 is provided with an outlet valve v3 for the non-recovered fraction, and the pipe 25 is provided with an outlet for the collected fraction. A valve v4 is provided, and a recovered fraction recovery tank 9 is provided downstream of the valve v4.

10は、この装置の制御を行なう演算制御器であって、
演算制御部11と、この演算制御部11に予め設定され
た回収率を入力させるための入力部12を有している。
10 is an arithmetic controller that controls this device,
It has an arithmetic control section 11 and an input section 12 for inputting a preset recovery rate into the arithmetic control section 11.

演算制御部11へは、流量計4、濃度検出器5.7及び
入力部12からそれぞれデータ信号が入力される。演算
制御部11は、これらの信号をデジタル信号に変換する
A/D変換器、入出力装置、中央処理装置、プログラム
やデータを記憶する記憶装置、これらを接続するデータ
バス等を備えている。また、演算制御部11は、演算結
果を制御信号として出力するためのD/A変換器を有す
る。
Data signals are input to the calculation control section 11 from the flow meter 4, the concentration detector 5.7, and the input section 12, respectively. The arithmetic control unit 11 includes an A/D converter that converts these signals into digital signals, an input/output device, a central processing unit, a storage device that stores programs and data, a data bus that connects these, and the like. Further, the arithmetic control section 11 includes a D/A converter for outputting the arithmetic result as a control signal.

なお演算制御部11はタイマをも内蔵している。Note that the calculation control section 11 also has a built-in timer.

次に上記実施例装置の作動について、回収両分の展開速
度が非回収画分の展開速度よりも大きい場合を例にとっ
て説明する。
Next, the operation of the apparatus of the above embodiment will be explained, taking as an example a case where the development speed of both recovered fractions is higher than the development speed of the non-recovered fraction.

■ まず入力器12によって、目標回収率を演算制御部
11へ入力する。
(2) First, the input device 12 inputs the target recovery rate to the arithmetic control section 11 .

■ 付いてバルブvIを開、v2を閉とし、ポンプ3を
作動させて分離剤充填カラム6に溶離液を若干流した後
、バルブv1を閉、v2を開とし被分離液をカラム6に
流す、このときバルブV3は開、v4は閉としておく。
■ Then, open valve vI, close valve v2, operate pump 3, and allow some eluent to flow into column 6 filled with separation agent, then close valve v1, open valve v2, and flow the liquid to be separated into column 6. , At this time, valve V3 is open and valve V4 is closed.

演算制御部11へは流量計4、検出器5から検出信号が
送られてくると共に、演算制御部11に内蔵されたタイ
マにより被分離液流通開始時からの経過時間が測定され
ている。
Detection signals are sent from the flow meter 4 and the detector 5 to the calculation control unit 11, and a timer built in the calculation control unit 11 measures the elapsed time from the start of the flow of the liquid to be separated.

■ 所定時間、カラムに被分離液を流した後、バルブV
+を開、v2を閉とし、カラム6に溶離液を流す。
■ After flowing the liquid to be separated through the column for a predetermined period of time, close the valve V.
+ is opened, v2 is closed, and the eluent is allowed to flow through column 6.

■ 次いでバルブv3を閉、■4を開とする。■ Next, close valve v3 and open ■4.

■ 演算制御部11は、流量計4と検出器5からの出力
及び被分離液を流した時間の積により、カラム6に供給
した目的成分の総量を演算する。
(2) The calculation control unit 11 calculates the total amount of the target component supplied to the column 6 based on the product of the outputs from the flowmeter 4 and the detector 5 and the time during which the liquid to be separated is allowed to flow.

■ 演算制御部11には、出口側検出器7からも検出信
号出力値が入力されており、演算制御部11では、流量
計4の出力、溶離液流通開始時からの経過時間及び出口
側濃度の積により、その時点までに分離剤充填カラム6
から流出した目的成分の積算量(回収量)を演算する。
■ The detection signal output value is also input from the outlet side detector 7 to the calculation control unit 11, and the calculation control unit 11 receives the output of the flowmeter 4, the elapsed time from the start of eluent flow, and the concentration at the exit side. By the product of
Calculate the cumulative amount (recovery amount) of the target component that has flowed out.

■ この計算された回収量と、予め設定された回収率か
ら求められる回収目標量とを比較し、計算された回収量
が設定された回収目標量と等しいかもしくは大きくなっ
た時点で、バルブv3を開、■4を閉とし、回収画分の
回収槽9への回収を終了する。
■ This calculated collection amount is compared with the collection target amount determined from the preset collection rate, and when the calculated collection amount is equal to or larger than the set collection target amount, the valve v3 is opened and 4 is closed to complete the collection of the collected fraction into the collection tank 9.

なお上記演算例は本発明の一例であるから、本発明がこ
れに限定されるものではない。
Note that since the above calculation example is an example of the present invention, the present invention is not limited thereto.

例えば、■の後で、回収量を目的成分の総流入量で除し
て回収率に換算し、この回収率を目標回収率と比較する
ようにしても良い。
For example, after (2), the recovery amount may be divided by the total inflow amount of the target component to convert it into a recovery rate, and this recovery rate may be compared with the target recovery rate.

[実験例1] 第1図の装置において、分離用九庸剤として、1010
0Oの東洋曹達工業(株)製ヨノく一ル(il標)HW
−40cをパイレックスガラス製のカラム(内径50m
m、長さ500 mm)に充填し、充填剤充填カラム6
とした。ポンプ3としては日本精密(株)酸パーソナル
ポンプ(定量ポンプ)を用いた。検出器5.7としては
示差屈折率計を使用した。
[Experimental Example 1] In the apparatus shown in Fig. 1, 1010
0O Yonokuichiru (il mark) HW manufactured by Toyo Soda Kogyo Co., Ltd.
-40c to a Pyrex glass column (inner diameter 50m)
m, length 500 mm), and fill the column 6 with packing material.
And so. As pump 3, an acid personal pump (metering pump) manufactured by Nippon Seimitsu Co., Ltd. was used. A differential refractometer was used as the detector 5.7.

被分離液としては、水あめ溶液を糖濃度lO%となるよ
うに調整したものを用い、このうちグルコースの入って
いない糖を回収することとした。
As the liquid to be separated, a starch syrup solution adjusted to have a sugar concentration of 10% was used, and sugars containing no glucose were recovered.

溶離剤としては、蒸留水を用いた。Distilled water was used as the eluent.

なお流量計4は、ポンプ3として定量ポンプを採用した
ところから、この定量ポンプをもって代用した。目標回
収率は60%とした。
Note that since a metering pump was used as the pump 3, this metering pump was used instead of the flow meter 4. The target recovery rate was set at 60%.

まず入力部12から、目標回収率0.6を入力した。そ
してカラム6内に溶離液を若干流した後、バルブV+を
閉、V2を開、■4を閉、v3を開とし、上記水あめ溶
液を4ornl1分の流速で100mu通液し、次いで
バルブVIを開、■2を閉とすると共に、バルブv4を
開とし、v3を閉として、溶離液(蒸留水)を40m文
/分で通液した。
First, a target recovery rate of 0.6 was input from the input unit 12. After slightly flowing the eluent into column 6, close valve V+, open V2, close ■4, and open v3, and pass 100 mu of the above starch syrup solution at a flow rate of 4 or 1 minute, then close valve VI. With valve v4 open and valve v3 closed, the eluent (distilled water) was passed through at a rate of 40 m/min.

演算制御部ll内では、検出器5.7からの検出濃度信
号を0.5秒毎に読込み、検出器5で検出される、グル
コースの入っていない糖濃度1こ流量と通液時間を乗じ
て総波人−借を演算する。そして、これに目標回収XJ
0.6を乗じた値と、出【1側検出器7から検出された
値に濃酸40mす7分を乗じた値の積算値(回収量)と
を比較し、前者の値に比べ後者の値が等しいか又は大き
くなった時点でバルブV3.V4を切換える操作を行な
った。この結果を表1に示す。
In the arithmetic control unit 11, the detected concentration signal from the detector 5.7 is read every 0.5 seconds, and the sugar concentration without glucose detected by the detector 5 is multiplied by the flow rate and the liquid flow time. to calculate the total wave person-borrow. And this is the target collection XJ
Compare the value multiplied by 0.6 and the integrated value (recovered amount) of the value detected from output 1 side detector 7 multiplied by 40 m of concentrated acid + 7 minutes, and compare the former value with the latter. When the values of V3. are equal to or greater than V3. I performed an operation to switch V4. The results are shown in Table 1.

また被分離液の糖濃度を7%及び15%に変えた水あめ
溶液を用いた場合について、■−記と同様に試験を行な
った。その結果を表1に示す。
In addition, tests were conducted in the same manner as in section ①- using starch syrup solutions in which the sugar concentration of the liquid to be separated was changed to 7% and 15%. The results are shown in Table 1.

表  1 表1より、目標値通りの回収率で、十分に分離されたこ
とが明らかである。
Table 1 From Table 1, it is clear that sufficient separation was achieved with the recovery rate meeting the target value.

[実験例2] 実験例1で用いたものと同じ装置及び同じ充填剤を用い
、糖濃度7%、15%の場合について同様の条件で分離
操作を行なった。
[Experimental Example 2] Using the same apparatus and the same packing material as those used in Experimental Example 1, separation operations were performed under the same conditions for sugar concentrations of 7% and 15%.

ただし回収終了点は、実験例1で回収率を60%とし糖
濃度を10%としたときの分離力ラム6出口の検出器7
の出力を基準とし、検出器7の出力値がこの値以下にな
った時点で回収、非回収のバルブ切換えを行なうように
した。結果を表2に示す。分離カラム6の出口側検出器
7の値が、設定値よりも小さくなった時点で、回収、非
回収バルブを切換える方式では、表2に示したように回
収率及び回収液のグルコース排除率は大きく変動した。
However, the recovery end point is determined by the detector 7 at the outlet of the separation force ram 6 when the recovery rate is 60% and the sugar concentration is 10% in Experimental Example 1.
When the output value of the detector 7 becomes below this value, the valve is switched between recovery and non-recovery. The results are shown in Table 2. In the method in which the recovery/non-recovery valve is switched when the value of the detector 7 on the outlet side of the separation column 6 becomes smaller than the set value, the recovery rate and the glucose elimination rate of the recovered liquid are as shown in Table 2. It fluctuated greatly.

表  2 [実験例3] 実験例1で用いたものと同じ装置及び充填剤を用い、糖
濃度7.15%の場合について、同様の条件で分離操作
を行なった。
Table 2 [Experimental Example 3] Using the same apparatus and packing material as those used in Experimental Example 1, a separation operation was performed under the same conditions at a sugar concentration of 7.15%.

ただし、回収終了点は、実験例1で回収率を60%とし
糖濃度を10%としたときに回収、非回収のバルブ切換
えを行なった時間を基準とし、この時間になったときに
、バルブの切換えを行なった。結果を表3に示す。
However, the recovery end point is based on the time when the valve is switched between recovery and non-recovery when the recovery rate is 60% and the sugar concentration is 10% in Experimental Example 1. The switch was made. The results are shown in Table 3.

表3に示すように、タイマだけで、回収非回収バルブの
操作を行なった場合、被分離液の濃度変化に伴い、回収
率及び回収液のグルコース排除率が大きく変動すること
が認められた。
As shown in Table 3, when the recovery and non-recovery valve was operated using only the timer, it was observed that the recovery rate and the glucose elimination rate of the recovery liquid varied greatly as the concentration of the liquid to be separated changed.

表  3 [効果] 以上の通り、本発明の装置は、カラムから流出する目的
成分の回収率を演算し、この回収率が目標回収率以上に
なったときに、回収の終了を行なうように構成したもの
であり、常に所定の回収率となるように自動的に分離操
作が行なわれる。
Table 3 [Effects] As described above, the device of the present invention is configured to calculate the recovery rate of the target component flowing out from the column, and to terminate the recovery when this recovery rate exceeds the target recovery rate. The separation operation is automatically performed so that a predetermined recovery rate is always achieved.

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

第1図は本発明の実施例に係るクロマトグラフィーによ
る分離装置の系統図である。 1・・・・・・溶離液貯槽、  2・・・・・・被分離
液貯槽、3・・・・・・送液ポンプ、  4・・・・・
・流量計、5.7・・・・・・濃度検出器、 6・・・・・・分離剤充填カラム、8・・・・・・分取
装置、9・・・・・・回収画分回収槽、 10・・・・・・演算制御器。
FIG. 1 is a system diagram of a chromatographic separation apparatus according to an embodiment of the present invention. 1... Eluent storage tank, 2... Liquid to be separated storage tank, 3... Liquid sending pump, 4...
・Flowmeter, 5.7...Concentration detector, 6...Separating agent packed column, 8...Preparation device, 9...Recovered fraction Recovery tank, 10... Arithmetic controller.

Claims (1)

【特許請求の範囲】[Claims] (1)分離用充填剤を内蔵したカラムと、分離目的成分
を含む被分離液と溶離液とを該カラムに供給する手段と
、該カラムから排出される液を分取する手段と、前記カ
ラムの入口及び出口のうち少なくとも出口に設けられた
液中の目的成分濃度を検出する濃度検出器と、前記カラ
ムへの被分離液の流入量を検出する流量検出手段と、前
記濃度検出器及び流量検出手段の出力が入力され、これ
に基いてカラムからの目的成分流出量を演算すると共に
、目的成分のカラムへの総流入量と予め設定された回収
率とから目的成分の回収目標量を演算し、目的成分流出
量が回収目標量以上になつたときに前記分取手段を切替
制御する演算制御器と、からなるクロマトグラフィーに
よる分離装置。
(1) A column containing a separation packing material, a means for supplying a liquid to be separated containing a component to be separated and an eluent to the column, a means for fractionating the liquid discharged from the column, and the column. a concentration detector for detecting the concentration of a target component in the liquid, which is provided at least at an inlet and an outlet of the column; a flow rate detection means for detecting the amount of inflow of the liquid to be separated into the column; and the concentration detector and the flow rate. The output of the detection means is input, and based on this, the amount of the target component flowing out from the column is calculated, and the target amount of the target component to be recovered is calculated from the total amount of the target component flowing into the column and the preset recovery rate. and an arithmetic controller that switches and controls the separation means when the outflow amount of the target component exceeds the target recovery amount.
JP59169106A 1984-08-13 1984-08-13 Chromatographic separation device Expired - Fee Related JPH0620489B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59169106A JPH0620489B2 (en) 1984-08-13 1984-08-13 Chromatographic separation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59169106A JPH0620489B2 (en) 1984-08-13 1984-08-13 Chromatographic separation device

Publications (2)

Publication Number Publication Date
JPS6150607A true JPS6150607A (en) 1986-03-12
JPH0620489B2 JPH0620489B2 (en) 1994-03-23

Family

ID=15880412

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59169106A Expired - Fee Related JPH0620489B2 (en) 1984-08-13 1984-08-13 Chromatographic separation device

Country Status (1)

Country Link
JP (1) JPH0620489B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04134262A (en) * 1990-09-27 1992-05-08 Shimadzu Corp Specimen sampling method
CN104897822A (en) * 2014-03-04 2015-09-09 株式会社岛津制作所 Liquid chromatograph control system and liquid chromatograph control method
CN112546673A (en) * 2020-12-18 2021-03-26 欧尚元(天津)有限公司 Parallel uniform-feeding resin column system and feeding control method

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53149870A (en) * 1977-05-26 1978-12-27 Sanmatsu Kougiyou Kk Column chromato separation
JPS5411073A (en) * 1977-06-28 1979-01-26 Asahi Chem Ind Co Ltd Controlling method for directional control valve of flow path

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53149870A (en) * 1977-05-26 1978-12-27 Sanmatsu Kougiyou Kk Column chromato separation
JPS5411073A (en) * 1977-06-28 1979-01-26 Asahi Chem Ind Co Ltd Controlling method for directional control valve of flow path

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04134262A (en) * 1990-09-27 1992-05-08 Shimadzu Corp Specimen sampling method
CN104897822A (en) * 2014-03-04 2015-09-09 株式会社岛津制作所 Liquid chromatograph control system and liquid chromatograph control method
CN112546673A (en) * 2020-12-18 2021-03-26 欧尚元(天津)有限公司 Parallel uniform-feeding resin column system and feeding control method

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