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JP3662132B2 - Simulated moving bed chromatographic separation system - Google Patents
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JP3662132B2 - Simulated moving bed chromatographic separation system - Google Patents

Simulated moving bed chromatographic separation system Download PDF

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JP3662132B2
JP3662132B2 JP33250098A JP33250098A JP3662132B2 JP 3662132 B2 JP3662132 B2 JP 3662132B2 JP 33250098 A JP33250098 A JP 33250098A JP 33250098 A JP33250098 A JP 33250098A JP 3662132 B2 JP3662132 B2 JP 3662132B2
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flow path
raw material
nozzle
chromatographic separation
material liquid
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JP2000155114A (en
JP2000155114A5 (en
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裕路 小川
隆之 増田
学 安田
康平 佐藤
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Organo Corp
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Organo Corp
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Description

【0001】
【発明の属する技術分野】
本発明は、擬似移動層式クロマト分離装置に関し、更に詳しくは、擬似移動層式クロマト分離装置における回転弁の改良に関する。
【0002】
【従来の技術】
クロマト分離装置は、製糖業や製薬業などの製造業において、天然又は化学反応によって得られる複数の成分からなる原材料の流体から一種以上の成分を抽出する目的で広く用いられている。クロマト分離装置には、従来から用いられている回分固定層方式の他に、最近では移動層方式の装置が種々提案されている。
【0003】
図5は、移動層方式のクロマト分離装置の原理を示す分離塔の断面模式図である。分離塔50には、予め充填剤(吸着剤)52を充填し、これに溶離剤を満たしておく。2種の成分A及びCを有する原料液を原料供給口Fから導入し、溶離剤を溶離剤供給口Dから一定の線速度となるように供給する。各成分A及びCは、充填剤との親和力の差により、分離塔50内を異なる線速度で移動し、例えば親和力の小さな成分Aは大きな線速度で移動し、親和力が大きな成分Cは小さな線速度で移動する。このため、成分Aを多く含む画分と成分Cを多く含む画分とに分離できる。
【0004】
移動層方式の分離装置では、充填剤を成分Aの移動速度と成分Cの移動速度との中間の速度で溶離剤の流れと逆の方向に移動させる状態を作り出す。このようにすることにより、図示のように、原料液の供給位置を境にして成分Aは、溶離剤の流れ方向で見て原料供給位置の前方で、また、成分Cは原料供給位置の後方で取り出すことができる。この方式は、充填剤を均一に移動させることの困難性から、実際に工業的に用いるには難点がある。
【0005】
充填剤を移動させることなく、移動層方式と同等の分離性能を得ることが出来る擬似移動層方式の分離装置が実用化されている。図6にこの分離装置の原理を示した。この方式では、分離塔50を複数(図の例では12個)のカラム54に分割し、これを無端状に接続している。充填剤の移動に代えて、原料液F及び溶離剤Dの供給位置と、成分A及びCの抜出し位置とを溶離剤の流れ方向に移動させる。これにより、時間の経過と共に、系内の液の分布は循環液の流れ方向に移動する。一定時間経過後でこの濃度分布が1カラム分移動した後に、原料液及び溶離剤の供給位置と、成分A及びCの抜出し位置とを循環液の流れ方向に1カラム分移動させる。この操作を繰り返せば、常に最適な位置で各液の供給と抜出しとを行うことが出来る。
【0006】
上記循環液の供給位置及び抜出し位置の移動には、一般には、順次にバルブを切り換える方式が用いられる。この切換えには、カラム1台毎に4個の個別の弁を用いる個別弁方式(例えば、特開平4−334504号公報)と、全体のカラムの流れを1つの回転弁による切換えで制御する回転弁方式(例えば、特開平8−323104号公報)とがある。回転弁方式は、配管構成及び制御が簡素になるため、近年多用されている。
【0007】
【発明が解決しようとする課題】
回転弁方式では、一般には、カラムを含む循環流路を回転させる方式が用いられる。しかし、多数のカラムを含む流路は重量が大きく、これを常時回転させることには構造的な問題が伴う。また、複雑な回転弁や回転継手を使用して循環流路を固定させる方式もある(前記特開平8−323104号公報)が、回転弁や回転継手自体の構造が複雑なため、製造コストがかさむばかりか、装置の維持管理が煩雑となり、或いは、装置の信頼性に問題が生ずる等の欠点がある。
【0008】
本発明は、上記に鑑み、簡易な構造でコストも低い回転弁を有する擬似移動層式クロマト分離装置を提供し、もって、擬似移動層式クロマト分離装置のコストの低減と、装置の小型化、維持管理の簡素化、及び、信頼性の向上とを図ることを目的とする。
【0009】
【課題を解決するための手段】
上記目的を達成するために、本発明の擬似移動層式クロマト分離装置は、入口及び出口を夫々有する少なくとも4つのカラムと、
溶離液を供給する溶離液流路、少なくとも2成分を含む原料液中の第1の成分を抜き出す第1の抜出し流路、及び、前記原料液中の第2の成分を抜き出す第2の抜出し流路を少なくとも含む可撓性配管と、
円筒又は円錐状の固定面と、前記各カラムに対応して配設される固定流路とを有する固定部、及び、前記固定面に褶動しつつ回転する回転面と、前記各可撓性配管に対応して配設される回転流路とを有する回転部から成る回転弁とを備え、
前記各固定流路は、相互に連通する、前記固定面に露出する第1ノズル、1つのカラムの出口に連通する第2ノズル、及び、前記1つのカラムに隣接するカラムの入口に連通する第3ノズルを有し、前記固定流路によって前記カラムを全体として無端状に接続するものであり、
前記各回転流路は、一端が前記回転面に露出して前記固定流路の前記第1ノズルに周期的に連通すると共に、他端が対応する前記可撓性配管に接続されることを特徴とする。
【0010】
本発明の擬似移動層式クロマト分離装置によると、回転弁の構成が簡素になるので、装置全体のコスト低減、装置の小型化、維持管理の簡素化、信頼性の向上が可能となる。
【0011】
本発明で使用される回転弁の材質に特に制限はないが、回転部と固定部の褶動面における円滑な褶動のためには、回転部又は固定部の何れか一方をテフロン樹脂やポリエチレン樹脂等で製作するのが好ましい。この場合、他方をステンレス材等で製作する。可撓性チューブには、ナイロンチューブや、テフロンチューブ、PEEKチューブ、ステンレスチューブ等が好適に用いられる。
【0012】
本発明の好ましい構成では、前記原料液を供給する原料液流路及び該原料液流路に対応する前記回転流路を更に含み、前記原料液流路が更に前記可撓性配管として構成される。該構成は、2成分を含む原料液を継続的に供給し、該原料液を各成分に分離する形式のクロマト分離装置に好適に使用できる。例えば3成分を含む原料液を各成分に分離する形式のクロマト分離装置の場合には、分離工程の1サイクルに1回原料液を循環路中に供給する原料液流路があればよく、該原料液流路は固定配管として構成することが出来る。
【0013】
また、前記固定流路の第1ノズルから第2ノズルと第3ノズルとに分岐する分岐部を、第1ノズルに隣接して配設することも本発明の好ましい態様である。これによって、回転部の回転によって流路を切り換えた際に生ずる、異なる成分を有する循環液の混合を防止する。
【0014】
前記回転部が、予め設定した角度に延べ回転角度が達すると逆転し、所定の回転角度位置に戻ることも本発明の好ましい態様である。これによって、回転部の回転角度を例えば360°以下に制限できるので、可撓性配管の捻れを最小限に抑えることができ、ステンレスチューブ等を可撓性配管として好適に用いることができる。
【0015】
【発明の実施の形態】
図面を参照し、本発明の一実施形態例の擬似移動層式クロマト分離装置(以下、単にクロマト分離装置と呼ぶ)に基づいて本発明を更に詳細に説明する。
【0016】
図1は、本発明の一実施形態例のクロマト分離装置の全体構成を示す模式的斜視図である。クロマト分離装置は、回転弁10を有し、回転弁10は、半径方向内側に配設された略円錘台形状の回転部(回転体)30と、回転体30の円錐面に摺接する円錐台状の内周面及び略円筒形状の外形を有する固定部32とで構成される。回転体30には内部に4つの回転流路が形成され、4つの回転流路は、可撓性配管44として構成された、成分A及び成分Cを含有する原料液を供給する原料液チューブと、溶離剤を供給する溶離剤供給チューブと、分離成分Aを抜き出す第1の抜出しチューブと、分離成分Cを抜き出す第2の抜出しチューブとに夫々接続している。可撓性チューブ44の太さは例えば1〜5mm程度である。
【0017】
回転弁10の外側固定部32には、その半径方向外側に隣接して8つのカラム20が円周方向に略等間隔に配設されている。8つのカラム20は、配管22、逆止弁34、及び、回転弁10の固定部32内の固定流路を介して無端の円環状に接続されている。カラムの大きさは、例えば、長さが10〜50cmで直径が1〜10cm程度である。回転弁10の回転体30は、系内を移動する循環液の移動速度に対応し、ステッピングモータ24によって図面上で反時計方向に回転される。この回転は、一回の動作で1周の1/8だけ回転する間欠的な回転であり、例えば5分間隔で1ノッチ動き、約40分程度で1周する。この場合、回転体30は、最初の角度位置から7/8周すると、反転して最初の角度位置に戻る。なお、カラム20を連結した循環路内には、1乃至複数台の図示しない循環ポンプが適当な位置に配設される。
【0018】
回転体30の回転角度は、回転角度位置を検出するフォトインタラプタ26及び穴あき円板28によって検出され、フォトインタラプタ26は、穴を透過した光を検出すると直ちにステッピングモータ24を所定角度逆転させて、回転体30を最初の角度位置に戻す。
【0019】
図2は、回転弁10の回転部30と各原料タンク及び分離製品タンクとの接続関係を示している。本クロマト分離装置には、2成分系の原料液タンク12、溶離剤タンク14、A成分タンク16、及び、C成分タンク18が付属している。これらタンクは、回転部30の原料液供給口F、溶離剤供給口D、成分A抜出し口A、及び、成分C抜出し口Cに、夫々、固定配管42、ポンプ40、及び、可撓性チューブ44を介して接続されている。原料液には、2以上の成分が含まれていればよく、3以上の成分が含まれていてもよい。
【0020】
図3は、回転弁10の固定部32と各カラム20との接続関係を示す、回転弁10の横断面を含む模式図である。固定部32には、各カラム20からの配管22に接続される流路(固定流路)38が各カラムに対応して形成される。各固定流路38は、固定部32の内側固定面に露出する第1のノズルと、互に隣接するカラム20の出口及び入口に夫々接続する第2及び第3のノズルとを有し、これらノズル相互は、各固定流路において固定部32の円錐状内面(固定面)の近傍でY字状に連通している。この各Y字状連通部は、所定の回転角度位置で、回転体30の回転方向に見て順次に並んで配設された原料液の供給口F、成分Aの抜出し口A、溶離剤の供給口D、及び、成分Cの抜出し口Cに接続された、回転体30内の流路(回転流路)36と連通する。各カラム20と固定部32とを接続する配管22の途中には、循環液の流れを回転体30の回転方向である反時計方向に制限するための逆止弁34が配設される。
【0021】
図4は、回転弁10の構造について、一部を縦断面で示す側面図である。回転弁10は、内側の回転体30と、外側の固定部32とから構成され、回転体30は、シャフト46を介してステッピングモータに駆動される。回転体30は、全体として、下面が上面よりも小さな円錐台の形状を有する。固定部32は、底部の半径がやや小さな略円筒形状の外周面を有し、その内周面は、回転体30の円錐面に褶接する円錐台形状を有する。回転体30には、各タンクに対応する回転流路36が内部に形成され、回転流路36は、回転体30の円錐面と下面との間にL字状に配設される。回転流路36の円錐台下面側の端部は、継手48を介して可撓性チューブ44に接続され、前述の通り可撓性チューブ44を介して各タンクに連通している。
【0022】
回転流路36の円錐台斜面側の端部は、図示の回転角度位置で、固定部32側の固定流路38の第1のノズルに連通している。固定流路38の第1のノズルから横方向に伸びる一方の分岐は、第2のノズルを介して対応するカラム20の出口に連通し、そのカラム20から循環液が流入する入口流路を構成する。また、その第1のノズルから斜め下方に伸びる他方の分岐は、第3のノズルを介して下流側の隣接するカラム20の入口に連通し、このカラム20に循環液が流出する出口流路を構成する。各分岐は、固定部32の外面とほぼ直交して伸びており、切削等により加工する際の製作上の便宜が図られる。
【0023】
回転弁30には、上記の通り可撓性チューブ44が接続している。ここで、回転体30を、反時計方向に間欠的に回転させ、この延べ回転角度が原位置から略360°に及ぶと、可撓性チューブ44には少なからぬ捻れが生ずる。しかしこの捻れは、回転部30が原位置に戻る次の逆回転によって解消する。このように、本実施形態例のクロマト分離装置では、回転弁10の回転体30と各タンクとの接続に可撓性チューブ44を使用したので、回転弁10とカラム20との接続を固定配管22で行うことができ、装置構成が簡素になる利点がある。可撓性チューブ44としては、プラスチック製又はステンレス製等のチューブが使用できる。ここで、捻れを効果的に吸収するために、可撓性チューブ44を螺旋状に加工してある。
【0024】
回転弁10の固定部32は、例えば耐食性のあるステンレス材などで製作し、回転体30には、潤滑性を備えたテフロン樹脂やポリエチレン樹脂を用いることが好ましい。また、これに代えて、回転体30をステンレス材で製作し、固定部32を潤滑性を備えたテフロン樹脂やポリエチレン樹脂で製作しても良い。
【0025】
本実施形態例のクロマト分離装置は、回転弁を有する従来の擬似移動層式クロマト分離装置と同様に動作し、原料供給口F及び溶離剤供給口Dから夫々原料液及び溶離剤を供給し、循環液の移動速度に対応して回転弁を回転させることにより、A及びCの抜出し口から夫々成分A及びCを抜き出す。
【0026】
以上、本発明をその好適な実施形態例に基づいて説明したが、本発明の擬似移動層式クロマト分離装置は、上記実施形態例の構成にのみ限定されるものではなく、上記実施形態例の構成から種々の修正及び変更を施した擬似移動層クロマト分装置も、本発明の範囲に含まれる。
【0027】
【発明の効果】
以上説明したように、本発明の擬似移動層式クロマト分離装置によれば、無端状に接続されるカラムを回転弁の固定部に接続したことにより、擬似移動層式クロマト分離装置全体の機械的構造が簡素化され、その維持管理作業も容易になる。また、回転弁の構造の複雑化を伴うことなく、回転弁近傍の部品の点数を削減し、配管構造も簡素化できたことから、クロマト分離装置の製造コストを低減できる効果がある。
【図面の簡単な説明】
【図1】本発明の一実施形態例の擬似移動層式クロマト分離装置の構成を示す模式的斜視図。
【図2】図1のクロマト分離装置の回転弁の回転部と各タンクとを接続する配管のブロック図。
【図3】図1のクロマト分離装置の固定部と各カラムとの接続を示す、回転弁の横断面を含む模式図。
【図4】図1に示した回転弁の縦断面図。
【図5】一般的な移動層クロマト分離装置の原理を示す、分離塔の模式的断面図。
【図6】一般的な擬似移動層式クロマト分離装置の原理を示す、分離塔の模式的断面図。
【符号の説明】
10:回転弁
12、14、16、18:タンク
20:カラム
22:循環配管
24:ステッピングモータ
26:フォトインタラプタ
28:穴あき円板
30:回転体(回転部)
32:固定部
34:逆止弁
36:回転流路
38:固定流路
40:ポンプ
42:配管
44:可撓性配管
46:シャフト
48:継手
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a simulated moving bed type chromatographic separation apparatus, and more particularly to improvement of a rotary valve in the simulated moving bed type chromatographic separation apparatus.
[0002]
[Prior art]
BACKGROUND ART Chromatographic separation apparatuses are widely used in the manufacturing industry such as sugar industry and pharmaceutical industry for the purpose of extracting one or more components from a raw material fluid consisting of a plurality of components obtained by natural or chemical reaction. Various chromatographic separation apparatuses have recently been proposed in addition to the batch fixed bed system conventionally used.
[0003]
FIG. 5 is a schematic sectional view of a separation tower showing the principle of a moving bed type chromatographic separation apparatus. The separation tower 50 is preliminarily filled with a filler (adsorbent) 52 and filled with an eluent. A raw material liquid having two kinds of components A and C is introduced from a raw material supply port F, and an eluent is supplied from an eluent supply port D so as to have a constant linear velocity. The components A and C move at different linear velocities in the separation column 50 due to the difference in affinity with the packing material. For example, the component A having a low affinity moves at a high linear velocity, and the component C having a high affinity has a small line. Move at speed. For this reason, it is separable into the fraction which contains many components A, and the fraction which contains many components C.
[0004]
In the moving bed type separation device, a state is created in which the filler is moved in the direction opposite to the flow of the eluent at a speed intermediate between the moving speed of component A and the moving speed of component C. By doing so, as shown in the figure, the component A is in front of the raw material supply position as viewed in the flow direction of the eluent, and the component C is behind the raw material supply position, as shown in the figure. Can be taken out with. This method is difficult to use industrially due to the difficulty of moving the filler uniformly.
[0005]
A pseudo moving bed type separation apparatus that can obtain separation performance equivalent to that of the moving bed type without moving the filler has been put into practical use. FIG. 6 shows the principle of this separation apparatus. In this method, the separation tower 50 is divided into a plurality of (in the example shown in the figure, 12) columns 54 and connected endlessly. Instead of the movement of the filler, the supply position of the raw material liquid F and the eluent D and the extraction position of the components A and C are moved in the eluent flow direction. Thereby, with the passage of time, the distribution of the liquid in the system moves in the flow direction of the circulating liquid. After the concentration distribution has moved by one column after a lapse of a fixed time, the supply position of the raw material liquid and the eluent and the extraction position of components A and C are moved by one column in the direction of the circulating liquid flow. By repeating this operation, it is possible to always supply and withdraw liquids at optimum positions.
[0006]
In order to move the circulating fluid supply position and the extraction position, generally, a method of sequentially switching valves is used. For this switching, an individual valve system using four individual valves for each column (for example, Japanese Patent Laid-Open No. 4-334504) and a rotation for controlling the entire column flow by switching with one rotary valve. There is a valve system (for example, JP-A-8-323104). The rotary valve system has been widely used in recent years because the piping configuration and control are simplified.
[0007]
[Problems to be solved by the invention]
In the rotary valve method, generally, a method of rotating a circulation flow path including a column is used. However, a flow path including a large number of columns is heavy, and there are structural problems associated with constantly rotating the flow path. In addition, there is a method of fixing the circulation flow path using a complicated rotary valve or rotary joint (JP-A-8-323104). However, the structure of the rotary valve or rotary joint itself is complicated, so that the manufacturing cost is low. In addition to being bulky, there are drawbacks such as complicated maintenance of the apparatus or problems with the reliability of the apparatus.
[0008]
In view of the above, the present invention provides a simulated moving bed type chromatographic separation device having a rotary valve with a simple structure and low cost, thereby reducing the cost of the simulated moving bed type chromatographic separation device and reducing the size of the device, The purpose is to simplify maintenance and improve reliability.
[0009]
[Means for Solving the Problems]
In order to achieve the above object, the simulated moving bed chromatographic separation apparatus of the present invention comprises at least four columns each having an inlet and an outlet,
An eluent flow path for supplying the eluent, a first extraction flow path for extracting the first component in the raw material liquid containing at least two components, and a second extraction flow for extracting the second component in the raw material liquid Flexible piping including at least a path;
A fixing part having a cylindrical or conical fixing surface, a fixing channel disposed corresponding to each column, a rotating surface that rotates while swinging on the fixing surface, and each of the flexibility A rotary valve having a rotary part having a rotary flow path arranged corresponding to the pipe,
Each fixed flow path communicates with each other, a first nozzle exposed on the fixed surface, a second nozzle communicated with an outlet of one column, and a first nozzle communicated with an inlet of a column adjacent to the one column. Having three nozzles, and connecting the column endlessly as a whole by the fixed flow path,
One end of each of the rotating channels is exposed to the rotating surface and periodically communicates with the first nozzle of the fixed channel, and the other end is connected to the corresponding flexible pipe. And
[0010]
According to the simulated moving bed chromatographic separation apparatus of the present invention, the configuration of the rotary valve is simplified, so that the cost of the entire apparatus can be reduced, the apparatus can be reduced in size, the maintenance can be simplified, and the reliability can be improved.
[0011]
There is no particular limitation on the material of the rotary valve used in the present invention, but for smooth peristalsis on the sliding surface of the rotating part and the fixed part, either the rotating part or the fixed part is made of Teflon resin or polyethylene. It is preferable to manufacture with resin. In this case, the other is made of stainless steel or the like. As the flexible tube, a nylon tube, a Teflon tube, a PEEK tube, a stainless steel tube or the like is preferably used.
[0012]
In a preferred configuration of the present invention, it further includes a raw material liquid channel for supplying the raw material liquid and the rotating flow channel corresponding to the raw material liquid channel, and the raw material liquid channel is further configured as the flexible pipe. . This configuration can be suitably used for a chromatographic separation apparatus in which a raw material liquid containing two components is continuously supplied and the raw material liquid is separated into each component. For example, in the case of a chromatographic separation apparatus in which a raw material liquid containing three components is separated into each component, it is sufficient if there is a raw material liquid flow path for supplying the raw material liquid into the circulation path once in one cycle of the separation step. The raw material liquid channel can be configured as a fixed pipe.
[0013]
It is also a preferred aspect of the present invention that a branching portion that branches from the first nozzle of the fixed flow path to the second nozzle and the third nozzle is disposed adjacent to the first nozzle. This prevents mixing of circulating fluids having different components that occur when the flow path is switched by the rotation of the rotating part.
[0014]
It is also a preferred aspect of the present invention that the rotating portion reverses when the rotation angle reaches a preset angle and returns to a predetermined rotation angle position. Thereby, since the rotation angle of the rotating part can be limited to, for example, 360 ° or less, twisting of the flexible piping can be minimized, and a stainless tube or the like can be suitably used as the flexible piping.
[0015]
DETAILED DESCRIPTION OF THE INVENTION
With reference to the drawings, the present invention will be described in more detail based on a simulated moving bed type chromatographic separation apparatus (hereinafter simply referred to as a chromatographic separation apparatus) according to an embodiment of the present invention.
[0016]
FIG. 1 is a schematic perspective view showing the overall configuration of a chromatographic separation apparatus according to an embodiment of the present invention. The chromatographic separation apparatus includes a rotary valve 10, and the rotary valve 10 has a substantially frustum-shaped rotary part (rotary body) 30 disposed radially inward, and a cone that is in sliding contact with the conical surface of the rotary body 30. It is comprised with the fixed part 32 which has a trapezoid internal peripheral surface and a substantially cylindrical external shape. The rotating body 30 has four rotating flow paths formed therein, and the four rotating flow paths are configured as a flexible pipe 44 and a raw material liquid tube for supplying a raw material liquid containing the component A and the component C. And an eluent supply tube for supplying the eluent, a first extraction tube for extracting the separation component A, and a second extraction tube for extracting the separation component C, respectively. The thickness of the flexible tube 44 is, for example, about 1 to 5 mm.
[0017]
Eight columns 20 are arranged on the outer fixed portion 32 of the rotary valve 10 at substantially equal intervals in the circumferential direction adjacent to the outer side in the radial direction. The eight columns 20 are connected in an endless ring shape through a fixed flow path in the fixed portion 32 of the piping 22, the check valve 34, and the rotary valve 10. The column size is, for example, about 10 to 50 cm in length and about 1 to 10 cm in diameter. The rotating body 30 of the rotary valve 10 corresponds to the moving speed of the circulating fluid moving in the system, and is rotated counterclockwise on the drawing by the stepping motor 24. This rotation is an intermittent rotation that rotates by 1/8 of one revolution in one operation, and for example, moves one notch at intervals of 5 minutes and makes one revolution in about 40 minutes. In this case, the rotator 30 reverses and returns to the initial angular position after 7/8 rounds from the initial angular position. In the circulation path connecting the columns 20, one or more circulation pumps (not shown) are arranged at appropriate positions.
[0018]
The rotation angle of the rotating body 30 is detected by a photo interrupter 26 and a holed disk 28 for detecting the rotation angle position. The photo interrupter 26 reverses the stepping motor 24 by a predetermined angle immediately after detecting the light transmitted through the hole. The rotating body 30 is returned to the initial angular position.
[0019]
FIG. 2 shows a connection relationship between the rotating unit 30 of the rotary valve 10 and each raw material tank and separated product tank. The chromatographic separation apparatus includes a two-component raw material liquid tank 12, an eluent tank 14, an A component tank 16, and a C component tank 18. These tanks are connected to a raw material liquid supply port F, an eluent supply port D, a component A extraction port A, and a component C extraction port C of the rotating unit 30, respectively, a fixed pipe 42, a pump 40, and a flexible tube. 44 is connected. The raw material liquid only needs to contain two or more components, and may contain three or more components.
[0020]
FIG. 3 is a schematic view including a cross section of the rotary valve 10 showing a connection relationship between the fixed portion 32 of the rotary valve 10 and each column 20. A flow path (fixed flow path) 38 connected to the pipe 22 from each column 20 is formed in the fixed portion 32 corresponding to each column. Each fixed flow path 38 has a first nozzle exposed on the inner fixed surface of the fixed portion 32, and second and third nozzles respectively connected to the outlet and inlet of the column 20 adjacent to each other. The nozzles communicate with each other in a Y shape in the vicinity of the conical inner surface (fixed surface) of the fixed portion 32 in each fixed flow path. Each Y-shaped communication portion is arranged at a predetermined rotation angle position in sequence in the rotation direction of the rotator 30, the raw material liquid supply port F, the component A extraction port A, and the eluent. It communicates with a flow path (rotary flow path) 36 in the rotating body 30 connected to the supply port D and the component C extraction port C. A check valve 34 for restricting the flow of the circulating fluid in the counterclockwise direction that is the rotational direction of the rotating body 30 is disposed in the middle of the pipe 22 that connects each column 20 and the fixed portion 32.
[0021]
FIG. 4 is a side view showing a part of the structure of the rotary valve 10 in a longitudinal section. The rotary valve 10 includes an inner rotary body 30 and an outer fixed portion 32, and the rotary body 30 is driven by a stepping motor via a shaft 46. The rotating body 30 as a whole has a truncated cone shape whose lower surface is smaller than the upper surface. The fixed portion 32 has a substantially cylindrical outer peripheral surface with a slightly smaller radius at the bottom, and the inner peripheral surface has a truncated cone shape that is in contact with the conical surface of the rotating body 30. A rotating flow path 36 corresponding to each tank is formed inside the rotating body 30, and the rotating flow path 36 is disposed in an L shape between the conical surface and the lower surface of the rotating body 30. The end of the rotary channel 36 on the lower side of the truncated cone is connected to the flexible tube 44 via the joint 48 and communicates with each tank via the flexible tube 44 as described above.
[0022]
The end of the rotary channel 36 on the side of the truncated cone is in communication with the first nozzle of the fixed channel 38 on the fixed part 32 side at the rotational angle position shown in the figure. One branch of the fixed channel 38 extending in the lateral direction from the first nozzle communicates with the outlet of the corresponding column 20 via the second nozzle, and constitutes an inlet channel through which the circulating fluid flows from the column 20. To do. Further, the other branch extending obliquely downward from the first nozzle communicates with the inlet of the adjacent column 20 on the downstream side via the third nozzle, and an outlet channel through which the circulating fluid flows out to the column 20 is provided. Constitute. Each branch extends substantially orthogonally to the outer surface of the fixed portion 32, so that the manufacturing convenience when machining by cutting or the like is achieved.
[0023]
As described above, the flexible tube 44 is connected to the rotary valve 30. Here, when the rotating body 30 is intermittently rotated in the counterclockwise direction and the total rotation angle reaches approximately 360 ° from the original position, the flexible tube 44 is not a little twisted. However, this twist is eliminated by the next reverse rotation in which the rotating unit 30 returns to the original position. As described above, in the chromatographic separation apparatus according to the present embodiment, the flexible tube 44 is used for connection between the rotating body 30 of the rotary valve 10 and each tank, so that the connection between the rotary valve 10 and the column 20 is fixed piping. 22 and there is an advantage that the apparatus configuration is simplified. As the flexible tube 44, a tube made of plastic or stainless steel can be used. Here, in order to absorb the twist effectively, the flexible tube 44 is processed into a spiral shape.
[0024]
The fixed portion 32 of the rotary valve 10 is made of, for example, a corrosion-resistant stainless material, and the rotating body 30 is preferably made of Teflon resin or polyethylene resin having lubricity. Alternatively, the rotating body 30 may be made of stainless steel, and the fixed portion 32 may be made of Teflon resin or polyethylene resin having lubricity.
[0025]
The chromatographic separation apparatus of this embodiment operates in the same manner as the conventional simulated moving bed type chromatographic separation apparatus having a rotary valve, and supplies the raw material liquid and the eluent from the raw material supply port F and the eluent supply port D, respectively. By rotating the rotary valve according to the moving speed of the circulating fluid, the components A and C are extracted from the A and C outlets, respectively.
[0026]
As mentioned above, although this invention was demonstrated based on the suitable embodiment example, the simulated moving bed type | formula chromatographic separation apparatus of this invention is not limited only to the structure of the said embodiment example, The said embodiment example is not limited. Pseudo moving bed chromatographic fractionation devices having various modifications and changes in configuration are also included in the scope of the present invention.
[0027]
【The invention's effect】
As described above, according to the simulated moving bed type chromatographic separation apparatus of the present invention, the column connected in an endless manner is connected to the fixed portion of the rotary valve. The structure is simplified and the maintenance work becomes easy. Further, since the number of parts in the vicinity of the rotary valve can be reduced and the piping structure can be simplified without complicating the structure of the rotary valve, the manufacturing cost of the chromatographic separation apparatus can be reduced.
[Brief description of the drawings]
FIG. 1 is a schematic perspective view showing the configuration of a simulated moving bed chromatographic separation apparatus according to an embodiment of the present invention.
FIG. 2 is a block diagram of piping that connects a rotary part of a rotary valve of the chromatographic separation apparatus of FIG. 1 and each tank.
3 is a schematic view including a cross section of a rotary valve, showing a connection between a fixed portion of the chromatographic separation apparatus of FIG. 1 and each column.
4 is a longitudinal sectional view of the rotary valve shown in FIG.
FIG. 5 is a schematic sectional view of a separation tower showing the principle of a general moving bed chromatographic separation apparatus.
FIG. 6 is a schematic cross-sectional view of a separation tower showing the principle of a general pseudo moving bed type chromatographic separation apparatus.
[Explanation of symbols]
10: Rotating valves 12, 14, 16, 18: Tank 20: Column 22: Circulating piping 24: Stepping motor 26: Photo interrupter 28: Perforated disk 30: Rotating body (rotating part)
32: Fixed part 34: Check valve 36: Rotating flow path 38: Fixed flow path 40: Pump 42: Pipe 44: Flexible pipe 46: Shaft 48: Fitting

Claims (5)

入口及び出口を夫々有する少なくとも4つのカラムと、
溶離液を供給する溶離液流路、少なくとも2成分を含む原料液中の第1の成分を抜き出す第1の抜出し流路、及び、前記原料液中の第2の成分を抜き出す第2の抜出し流路を少なくとも含む可撓性配管と、
円筒又は円錐状の固定面と、前記各カラムに対応して配設される固定流路とを有する固定部、及び、前記固定面に褶動しつつ回転する回転面と、前記各可撓性配管に対応して配設される回転流路とを有する回転部から成る回転弁とを備え、
前記各固定流路は、相互に連通する、前記固定面に露出する第1ノズル、1つのカラムの出口に連通する第2ノズル、及び、前記1つのカラムに隣接するカラムの入口に連通する第3ノズルを有し、前記固定流路によって前記カラムを全体として無端状に接続するものであり、
前記各回転流路は、一端が前記回転面に露出して前記固定流路の前記第1ノズルに周期的に連通すると共に、他端が対応する前記可撓性配管に接続されることを特徴とする擬似移動層式クロマト分離装置。
At least four columns each having an inlet and an outlet;
An eluent flow path for supplying the eluent, a first extraction flow path for extracting the first component in the raw material liquid containing at least two components, and a second extraction flow for extracting the second component in the raw material liquid Flexible piping including at least a path;
A fixing part having a cylindrical or conical fixing surface, a fixing channel disposed corresponding to each column, a rotating surface that rotates while swinging on the fixing surface, and each of the flexibility A rotary valve having a rotary part having a rotary flow path arranged corresponding to the pipe,
Each fixed flow path communicates with each other, a first nozzle exposed on the fixed surface, a second nozzle communicated with an outlet of one column, and a first nozzle communicated with an inlet of a column adjacent to the one column. Having three nozzles, and connecting the column endlessly as a whole by the fixed flow path,
One end of each of the rotating channels is exposed to the rotating surface and periodically communicates with the first nozzle of the fixed channel, and the other end is connected to the corresponding flexible pipe. A pseudo moving bed type chromatographic separation apparatus.
前記第1ノズルから、前記第2ノズルと前記第3ノズルとに分岐する分岐部が、前記第1ノズルに隣接して配設される、請求項1に記載の擬似移動層式クロマト分離装置。2. The simulated moving bed chromatographic separation device according to claim 1, wherein a branching portion that branches from the first nozzle into the second nozzle and the third nozzle is disposed adjacent to the first nozzle. 前記可撓性配管は、前記回転部の所定の回転角度に対応する可撓性を有する、請求項1又は2に記載の擬似移動層式クロマト分離装置。The pseudo moving bed type chromatographic separation apparatus according to claim 1, wherein the flexible pipe has flexibility corresponding to a predetermined rotation angle of the rotating unit. 前記回転部は、延べ回転角度が予め設定した角度に達すると逆転して所定の回転角度位置に戻る、請求項1又は2に記載の擬似移動層式クロマト分離装置。3. The simulated moving bed chromatographic separation device according to claim 1, wherein the rotation unit reverses and returns to a predetermined rotation angle position when a total rotation angle reaches a preset angle. 前記原料液を供給する原料液流路及び該原料液流路に対応する前記回転流路を更に含み、前記原料液流路が更に前記可撓性配管として構成される、請求項1乃至4の何れか1項に記載の疑似移動層クロマト分離装置。The raw material liquid flow path for supplying the raw material liquid and the rotating flow path corresponding to the raw material liquid flow path are further included, and the raw material liquid flow path is further configured as the flexible pipe. The simulated moving bed type chromatographic separation apparatus according to any one of the above.
JP33250098A 1998-11-24 1998-11-24 Simulated moving bed chromatographic separation system Expired - Fee Related JP3662132B2 (en)

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