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JP2015188381A - Separation device and separation method - Google Patents

Separation device and separation method Download PDF

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JP2015188381A
JP2015188381A JP2014068397A JP2014068397A JP2015188381A JP 2015188381 A JP2015188381 A JP 2015188381A JP 2014068397 A JP2014068397 A JP 2014068397A JP 2014068397 A JP2014068397 A JP 2014068397A JP 2015188381 A JP2015188381 A JP 2015188381A
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culture solution
megakaryocytes
storage tank
charge
charge supply
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雄一郎 津田
Yuichiro Tsuda
雄一郎 津田
元井 昌司
Masashi Motoi
昌司 元井
豊治 寺田
Toyoji Terada
豊治 寺田
義生 野上
Yoshio Nogami
義生 野上
和正 柴田
Kazumasa Shibata
和正 柴田
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Toray Engineering Co Ltd
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Toray Engineering Co Ltd
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Priority to PCT/JP2015/055016 priority patent/WO2015146415A1/en
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Abstract

PROBLEM TO BE SOLVED: To provide a separation device and a separation method for efficiently removing megakaryocytes from culture solution in which platelets and megakaryocytes exist in a mixed manner, without adversely affecting the platelets.SOLUTION: There is provided a separation device 1 for removing megakaryocytes from culture solution in which megakaryocytes M and platelets P exist in a mixed manner, the separation device comprising: a culture solution storage tank 2 storing culture solution SI therein; culture solution feeding means which has a function of sending the culture solution SI in the culture solution storage tank 2; and a recovery liquid storage tank 10 which supplies electric charge having polarity opposite to electric charge electrified onto a surface of the megakaryocytes M to a wall surface of an electric charge supply flow passage 7 by electric charge supply means 8 to make the megakaryocytes M in the culture solution SI adhere onto the wall surface of the electric charge supply flow passage 7 and remove the megakaryocytes, recovers recovery liquid SO, from which the megakaryocytes M have been removed, from the culture solution SI, and stores the recovery liquid.

Description

本発明は培養液から特定の成分を除去する分離装置および分離方法に関する。詳しくは、巨核球と血小板が含まれる培養液から、巨核球を除去する分離装置および分離方法に関する。   The present invention relates to a separation apparatus and a separation method for removing a specific component from a culture solution. Specifically, the present invention relates to a separation apparatus and a separation method for removing megakaryocytes from a culture solution containing megakaryocytes and platelets.

血液関連疾患の治療において血球細胞の輸血が行われている。なかでも血小板は止血において必須の細胞であるため、白血病、骨髄移植、抗癌治療などにおいては血小板の量的・質的低下に基づいた出血の予防や治療のための唯一の対処療法として、血小板輸血が行われている。輸血に用いられる血小板製剤は献血により賄われ、また、昨今では、献血者の全体数が減少する一方でウイルス感染症に汚染された献血者は増加するという現象もあり、献血に代わる安定した血小板供給源が求められ、その研究が活発に行われている。   Blood cells are transfused in the treatment of blood-related diseases. Since platelets are essential cells for hemostasis, platelets are the only treatment for leukemia, bone marrow transplantation, anticancer treatment, etc., as the only treatment for the prevention and treatment of bleeding based on the quantitative and qualitative decrease of platelets. A blood transfusion is taking place. Platelet preparations used for blood transfusions are covered by blood donation, and recently, there is also a phenomenon that the number of blood donors contaminated with viral infections increases while the total number of blood donors decreases, and stable platelets instead of blood donation A source is sought and research is actively underway.

その中でも、非特許文献1に記載の方法は、ヒトiPS細胞から自己複製が可能な巨核球を誘導することに成功している。巨核球は血小板を産生する細胞であることから、これにより血小板を安定的に大量に供給することも可能と成り得る。   Among them, the method described in Non-Patent Document 1 has succeeded in inducing megakaryocytes capable of self-replication from human iPS cells. Since megakaryocytes are cells that produce platelets, it may be possible to supply platelets stably and in large quantities.

非特許文献1の方法においては、培養液中の巨核球の自己複製を強制的に止めることにより、巨核球が成熟して血小板を産生する旨が記されている。ところで、培養液中の巨核球は同時に成熟して血小板を産生するのではなく、全ての巨核球が血小板を産生するのには時間を要する。一方において、血小板の特性は経時劣化するため、全ての巨核球が血小板を産生した段階においては初期に産生された血小板の劣化が進んでいる可能性がある。   In the method of Non-Patent Document 1, it is described that megakaryocytes mature to produce platelets by forcibly stopping self-replication of megakaryocytes in the culture medium. By the way, megakaryocytes in the culture solution do not mature and produce platelets at the same time, but it takes time for all megakaryocytes to produce platelets. On the other hand, since the characteristics of platelets deteriorate with time, at the stage where all megakaryocytes produce platelets, there is a possibility that degradation of platelets produced in the early stage has progressed.

また、血小板と巨核球が混在した状態で血小板製剤とすると、免疫系が活性化するという影響があって好ましくない。このため、血小板と巨核球が存在する培養液から巨核球を除去する必要がある。   In addition, it is not preferable to use a platelet preparation in a state where platelets and megakaryocytes are mixed because the immune system is activated. For this reason, it is necessary to remove megakaryocytes from a culture solution containing platelets and megakaryocytes.

Nakamuraら、”Expandable Megakaryocyte Cell Lines Enable Clinically−Applicable Generation of Platelets from Human Induced Pluripotent Stem Cells”、[online]、2014/2/13、Cell Stem Cell、[平成26年3月27日検索]、インターネット<URL;http://www.cell.com/cell−stem−cell/newartcles>Nakamura et al., “Expandable Megakalyte Cell Lines Enable Clinically-Appliable Generation of Privates, 27th Heisei, Cell 2” URL; http: // www. cell. com / cell-stem-cell / newarts>

培養液から特定の細胞成分を除去する方法としては、遠心分離が一般的に用いられるが、巨核球と血小板とは比重が近いため、大きな遠心加速度を付与する必要がある。このため、遠心分離法では、巨核球と血小板が分離できても、大きな遠心加速度により破壊される血小板が増え、血小板の回収率が低下する問題がある。   Centrifugation is generally used as a method for removing specific cell components from the culture solution. However, megakaryocytes and platelets are close in specific gravity, and therefore it is necessary to apply a large centrifugal acceleration. For this reason, in the centrifugal separation method, even if megakaryocytes and platelets can be separated, there is a problem that the platelets destroyed by a large centrifugal acceleration increase and the platelet recovery rate decreases.

本発明は、このような事情を鑑みてなされたものであり、血小板と巨核球が混在する培養液から、巨核球を効率よく取り除き、かつ血小板に悪影響を及ぼさない分離装置および分離方法を提供するものである。   The present invention has been made in view of such circumstances, and provides a separation apparatus and a separation method that efficiently remove megakaryocytes from a culture solution in which platelets and megakaryocytes coexist and do not adversely affect platelets. Is.

上記課題を解決するために、請求項1に記載の発明は、巨核球と血小板が混在する培養液から巨核球を除去する分離装置であって、培養液を貯える培養液貯槽と、前記培養液貯槽内の培養液を送液する機能を有する培養液送液手段と、培養液から巨核球を除去した回収液を回収して貯える回収液貯槽と、電荷供給手段とを備える分離装置である。   In order to solve the above-mentioned problem, the invention described in claim 1 is a separation device that removes megakaryocytes from a culture solution in which megakaryocytes and platelets are mixed, a culture solution storage tank for storing the culture solution, and the culture solution A separator comprising a culture solution feeding means having a function of feeding a culture solution in a storage tank, a collected solution storage tank for collecting and storing a collected solution obtained by removing megakaryocytes from the culture solution, and a charge supply means.

本発明の分離装置により、培養液から巨核球を除去した回収液を得ることが出来る。   With the separation device of the present invention, a recovered solution from which megakaryocytes have been removed from the culture solution can be obtained.

請求項2に記載の発明は、請求項1に記載の分離装置であって、培養液貯槽と回収液貯槽間に電荷供給手段として機能する電荷供給流路を備え、前記電荷供給流路の回収液貯槽側の接続先を、回収液貯槽または、培養液貯槽への帰還流路の何れかに切り換える機能を有する流出先切換バルブを備え、前記電荷供給流路に巨核球表面に帯電している電荷と逆の極性の電荷を供給することで、流動する培養液中の巨核球を前記電荷供給流路の壁面に付着させる機能を有していることを特徴とする分離装置である
本発明の分離装置では、電荷供給流路で巨核球が壁面に付着して行くため、流体中の巨核球の比率が下がる。このため、最終的には培養液から巨核球を除去することが出来る。
The invention according to claim 2 is the separation apparatus according to claim 1, further comprising a charge supply channel functioning as a charge supply means between the culture solution storage tank and the recovery solution storage tank, wherein the charge supply channel is recovered. An outflow destination switching valve having a function of switching the connection destination on the liquid storage tank side to either the recovery liquid storage tank or the return flow path to the culture liquid storage tank is provided, and the surface of the megakaryocyte is charged in the charge supply flow path The separation device according to the present invention has a function of attaching megakaryocytes in a flowing culture solution to the wall surface of the charge supply channel by supplying a charge having a polarity opposite to the charge. In the separation device, megakaryocytes adhere to the wall surface in the charge supply flow path, so the ratio of megakaryocytes in the fluid decreases. For this reason, finally, megakaryocytes can be removed from the culture solution.

請求項3に記載の発明は、請求項2に記載の分離装置であって、緩衝液を貯える緩衝液貯槽と、前記緩衝液貯槽内の緩衝液を送液する緩衝液送液手段と、前記電荷供給流路入口の接続先を、培養液送液手段または緩衝液送液手段の何れかに切り換える機能を有する流入先切換バルブを備え、緩衝液で前記壁面に付着している付着物を剥離して、電荷供給流路を洗浄する機能を有していることを特徴とする分離装置である。   Invention of Claim 3 is the separation apparatus of Claim 2, Comprising: The buffer solution storage tank which stores a buffer solution, The buffer solution sending means which sends the buffer solution in the said buffer solution tank, The said Equipped with an inflow destination switching valve having a function of switching the connection destination of the charge supply channel inlet to either the culture solution feeding means or the buffer solution feeding means, and the deposits adhering to the wall surface are removed with the buffer solution. Thus, the separator has a function of cleaning the charge supply channel.

本発明の分離装置によると、電荷供給流路の壁面に付着している付着物による分離性能低下を防ぐことが出来る。   According to the separation device of the present invention, it is possible to prevent a decrease in separation performance due to deposits adhering to the wall surface of the charge supply channel.

請求項4に記載の発明は、巨核球と血小板が混在する培養液を、培養液貯槽から流路に流動させる過程において、培養液貯槽及び流路の壁面に、巨核球表面に帯電している電荷と逆の極性の電荷を供給して、巨核球を前記壁面に付着させることにより、培養液から巨核球を除去することを特徴とする分離方法である。   In the invention according to claim 4, the surface of the megakaryocyte is charged on the wall surface of the culture solution storage tank and the flow channel in the process of flowing the culture solution containing megakaryocytes and platelets from the culture solution storage tank to the flow channel. The separation method is characterized in that the megakaryocytes are removed from the culture solution by supplying a charge having a polarity opposite to the charge and attaching the megakaryocytes to the wall surface.

本発明の分離方法により、流路の流動方向に沿って、巨核球が流路の壁面に付着して行くため、流体中の巨核球の比率が下がる。このため、最終的には培養液から巨核球を除去することが出来る。   According to the separation method of the present invention, megakaryocytes adhere to the wall surface of the channel along the flow direction of the channel, so that the ratio of megakaryocytes in the fluid decreases. For this reason, finally, megakaryocytes can be removed from the culture solution.

請求項5に記載の発明は、請求項4に記載の分離方法であって、流路の壁面に、巨核球に帯電している電荷と同じ極性の電荷を供給することで、前記壁面に付着している付着物を剥離して、流路を洗浄することを特徴とする分離方法である。   Invention of Claim 5 is the separation method of Claim 4, Comprising: It adheres to the said wall surface by supplying the electric charge of the same polarity as the electric charge currently charged to the megakaryocyte to the wall surface of a flow path The separation method is characterized in that the attached matter is peeled off and the flow path is washed.

本発明の分離方法によると、流路の壁面に付着している主な付着物である巨核球を容易に剥離することが出来、流路を効率的に洗浄することが出来る。   According to the separation method of the present invention, megakaryocytes, which are main deposits adhering to the wall surface of the flow path, can be easily peeled off, and the flow path can be washed efficiently.

血小板と巨核球が混在する培養液から、巨核球を効率よく取り除き、かつ血小板に悪影響を及ぼさない分離が可能となる。   It is possible to efficiently remove megakaryocytes from a culture medium in which platelets and megakaryocytes are mixed, and to separate them without adversely affecting the platelets.

本発明の一実施形態における分離装置の構成を説明する図である。It is a figure explaining the structure of the separation apparatus in one Embodiment of this invention. 本発明の一実施形態における電荷供給流路の機能を説明する図である。It is a figure explaining the function of the electric charge supply flow path in one Embodiment of this invention. 本発明の一実施形態における電荷供給流路の機能を断面で説明する図である。It is a figure explaining the function of the electric charge supply channel in one embodiment of the present invention by a section. 本発明の別の実施形態における分離装置の構成を説明する図である。It is a figure explaining the structure of the separation apparatus in another embodiment of this invention. 本発明の別の実施形態における筒型モジュールについて説明する図である。It is a figure explaining the cylindrical module in another embodiment of this invention. 本発明の別の実施形態を用いた巨核球の分離を説明する図である。It is a figure explaining isolation | separation of the megakaryocyte using another embodiment of this invention. 本発明の別の実施形態を用いた機能例を説明する図である。It is a figure explaining the example of a function using another embodiment of the present invention. 培養液貯槽で巨核球を付着させる実施形態を説明するための図である。It is a figure for demonstrating embodiment to which a megakaryocyte is made to adhere in a culture solution storage tank.

以下に、本発明の実施形態について、図を用いて説明する。   Embodiments of the present invention will be described below with reference to the drawings.

図1は、巨核球Mおよび血小板Pが混在する培養液SIから、巨核球Mを除去する分離装置1の構成を示している。培養液貯槽2には培養液SIが貯えられており、ポンプ3は培養液貯槽2中の培養液SIを送液する培養液送液手段である。また、緩衝液貯槽4には緩衝液Bが貯えられており、ポンプ5は緩衝液貯槽4中の緩衝液Bを送液する緩衝液送液手段である。ポンプ3およびポンプ5の送液側には切換バルブ6があり、切換バルブ6の先には電荷供給流路7があって、ポンプ3またはポンプ5から送液される液の何れかを電荷供給流路7に通液する流入先切換機能をバルブ6は有している。電荷供給流路7は、液体を流す流路であるが、壁面に電荷が供給される構成となっている。電荷供給手段8は、電荷供給流路7の壁面に電荷を供給する機能を有している。電荷供給流路7の流出側には切換バルブ9があり、切換バルブ9は流出先を回収液貯槽10または帰還流路11の何れかに切り換える流出先切換機能を有している。回収液貯槽10は電荷供給流路7で巨核球Mを除去した回収液SOが貯えられるようになっている。また、帰還流路11は培養液貯槽2と接続されている。   FIG. 1 shows a configuration of a separation apparatus 1 that removes megakaryocytes M from a culture solution SI in which megakaryocytes M and platelets P are mixed. The culture solution SI is stored in the culture solution storage tank 2, and the pump 3 is a culture solution supply means for supplying the culture solution SI in the culture solution storage tank 2. Moreover, the buffer solution B is stored in the buffer solution storage tank 4, and the pump 5 is a buffer solution supply means for supplying the buffer solution B in the buffer solution storage tank 4. There is a switching valve 6 on the liquid feed side of the pump 3 and the pump 5, and there is a charge supply channel 7 at the tip of the switch valve 6, and charge is supplied to either the liquid fed from the pump 3 or the pump 5. The valve 6 has an inflow destination switching function for passing through the flow path 7. The charge supply channel 7 is a channel through which liquid flows, and is configured to supply charges to the wall surface. The charge supply means 8 has a function of supplying charges to the wall surface of the charge supply channel 7. A switching valve 9 is provided on the outflow side of the charge supply flow path 7, and the switching valve 9 has an outflow destination switching function for switching the outflow destination to either the recovery liquid storage tank 10 or the return flow path 11. The recovery liquid storage tank 10 is configured to store the recovery liquid SO from which the megakaryocytes M are removed by the charge supply channel 7. The return channel 11 is connected to the culture medium storage tank 2.

次に、分離装置1により培養液SIから巨核球Mを除去する方法について説明する。まず、切換バルブ6の流入先をポンプ3とし、切換バルブ9の流出先を回収液貯槽10とした状態で、ポンプ3を駆動すれば培養液貯槽2中の培養液SIが電荷供給流路7内を流動する。この段階で、電荷供給手段8により電荷供給流路7の壁面に巨核球表面に帯電している電荷と逆の極性の電荷を供給する。そうすると、図2(a)のように、培養液SI中の巨核球Mが電荷供給流路7の壁面に付着するようになる。すなわち、流路の断面が円筒形状の場合を例にとると、図3(a)のように培養液SI中の巨核球Mには主流路7の壁面側へのクーロン力が働き、壁面に付着する。このため、電荷供給流路7を培養液SIが流動することにより、培養液SIから壁面に付着し、上流から下流に行く程、巨核球の比率が減少することになる。そこで、電荷供給流路7の長さおよび、電荷供給流路7の壁面への供給電荷量を適切に設定することにより、回収液貯槽10には巨核球Mを含まない回収液SOが流れ込む。電荷供給流路7の長さおよび壁面への電荷供給量が不足すると、回収液SO中に巨核球Mが残り、回収液SOを培養液貯槽2に戻して再度分離を行う必要がある。なお、培養液を電荷供給流路7に1回だけ流しただけで全ての巨核球を分離出来ないことが明らかな場合は、切換バルブ9の流出先を帰還流路11としてもよい。この場合、ポンプ3を駆動すれば培養液貯槽3→電荷供給流路7→帰還流路11→培養液貯槽3の循環を所定時間行った後に切換バルブ9の流出先を回収液貯槽11にすることで、巨核球を含まない回収液SOを得ることが出来る。   Next, a method for removing the megakaryocytes M from the culture solution SI using the separation device 1 will be described. First, when the pump 3 is driven in a state where the inflow destination of the switching valve 6 is the pump 3 and the outflow destination of the switching valve 9 is the recovery liquid storage tank 10, the culture liquid SI in the culture liquid storage tank 2 is transferred to the charge supply channel 7. Flows inside. At this stage, the charge supply means 8 supplies a charge having a polarity opposite to the charge charged on the megakaryocyte surface to the wall surface of the charge supply channel 7. Then, as shown in FIG. 2A, the megakaryocyte M in the culture solution SI comes to adhere to the wall surface of the charge supply channel 7. That is, taking the case where the cross section of the flow path is cylindrical as an example, the Coulomb force acting on the wall surface side of the main flow path 7 acts on the megakaryocyte M in the culture solution SI as shown in FIG. Adhere to. For this reason, when the culture solution SI flows through the charge supply channel 7, the ratio of megakaryocytes decreases from the culture solution SI to the wall surface and from upstream to downstream. Accordingly, by appropriately setting the length of the charge supply channel 7 and the amount of charge supplied to the wall surface of the charge supply channel 7, the recovery liquid SO that does not contain the megakaryocytes M flows into the recovery liquid storage tank 10. When the length of the charge supply channel 7 and the amount of charge supplied to the wall surface are insufficient, the megakaryocytes M remain in the recovered solution SO, and it is necessary to return the recovered solution SO to the culture solution storage tank 2 and perform separation again. In addition, when it is clear that all megakaryocytes cannot be separated only by flowing the culture solution through the charge supply channel 7 once, the flow-out destination of the switching valve 9 may be the return channel 11. In this case, if the pump 3 is driven, the culture medium storage tank 3 → the charge supply flow path 7 → the return flow path 11 → the circulation of the culture liquid storage tank 3 is performed for a predetermined time, and then the outlet of the switching valve 9 is changed to the recovery liquid storage tank 11. As a result, it is possible to obtain a recovered liquid SO that does not contain megakaryocytes.

以上のように、分離装置1により培養液SIから巨核球Mを除去する操作を行うと、電荷供給流路7の壁面に巨核球Mが付着した状態となる。このため、この巨核球除去操作を続けると、電荷供給流路7の壁面に多数の巨核球Mが付着することになる。このような状態では、培養液SIの流動により電荷供給流路7の壁面から巨核球Mが剥離することも起こりうる。また、長期使用しなかった場合等においては、電荷供給流路7の壁面への不純物蓄積も懸念される。そこで、分離装置1は、電荷供給流路7を洗浄する機能を備えていることが望ましい。   As described above, when the megakaryocyte M is removed from the culture solution SI by the separation device 1, the megakaryocyte M is attached to the wall surface of the charge supply channel 7. For this reason, if this megakaryocyte removal operation is continued, a large number of megakaryocytes M adhere to the wall surface of the charge supply channel 7. In such a state, the megakaryocyte M may be detached from the wall surface of the charge supply channel 7 due to the flow of the culture solution SI. Further, when not used for a long period of time, there is a concern that impurities accumulate on the wall surface of the charge supply channel 7. Therefore, it is desirable that the separation device 1 has a function of cleaning the charge supply channel 7.

電荷供給流路7を洗浄するために、図1の分離装置1において、切換バルブ6の流入先をポンプ5、切換バルブ9の流出先を帰還流路11としてポンプ5を駆動すれば、電荷供給流路7に緩衝液Bが流動する。この緩衝液Bの流速を上げることにより、電荷供給流路7の壁面に付着した巨核球Mおよび不純物は剥離し、培養液貯槽2側に流れ込むため電荷供給流路7が洗浄される。   In order to wash the charge supply flow path 7, if the pump 5 is driven using the pump 5 as the inflow destination of the switching valve 6 and the return flow path 11 as the outflow destination of the switching valve 9 in the separation device 1 of FIG. Buffer B flows through the flow path 7. By increasing the flow rate of the buffer solution B, the megakaryocytes M and impurities adhering to the wall surface of the charge supply channel 7 are separated and flow into the culture solution storage tank 2 side, so that the charge supply channel 7 is washed.

更に、緩衝液Bを電荷供給流路7に流動させる過程において、電荷供給流路7の壁面に巨核球表面に帯電している電荷と同じ極性の電荷を供給すれば、前記壁面付着した巨核球Mを容易に剥離することが出来る。   Further, in the process of flowing the buffer solution B into the charge supply channel 7, if a charge having the same polarity as the charge charged on the megakaryocyte surface is supplied to the wall surface of the charge supply channel 7, the megakaryocyte attached to the wall surface M can be easily peeled off.

これを分離装置1を用いて説明する。まず、切換バルブ6の流入先をポンプ5とし、切換バルブ9の流出先を帰還流路11とした状態で、ポンプ5を駆動すれば緩衝液貯槽4中の緩衝液Bが電荷供給流路7内を流動する。この段階で、電荷供給手段8により電荷供給流路7の壁面に巨核球表面に帯電している電荷と同じ極性の電荷を供給する。そうすると、図2(b)のように、主流路7の壁面に付着した巨核球Mが壁面から剥離し緩衝液Bに混ざった状態となる。すなわち、流路の断面が円筒形状の場合を例にとると、図3(b)のように電荷供給流路7の壁面に付着したの巨核球Mには壁面から離れるクーロン力が働き、壁面から剥離する。剥離した巨核球Mおよび血小板Pは緩衝液Bの流動により、帰還流路11を経て培養液貯槽2に流れ込む。   This will be described using the separation device 1. First, when the pump 5 is driven in a state where the inflow destination of the switching valve 6 is the pump 5 and the outflow destination of the switching valve 9 is the return flow path 11, the buffer solution B in the buffer solution storage tank 4 becomes the charge supply flow path 7. Flows inside. At this stage, charges having the same polarity as the charges charged on the megakaryocyte surface are supplied to the wall surface of the charge supply channel 7 by the charge supply means 8. Then, as shown in FIG. 2B, the megakaryocytes M attached to the wall surface of the main flow path 7 are separated from the wall surface and mixed with the buffer solution B. That is, taking the case where the cross section of the channel is cylindrical as an example, the Coulomb force acting away from the wall surface acts on the megakaryocyte M attached to the wall surface of the charge supply channel 7 as shown in FIG. Peel from. The peeled megakaryocytes M and platelets P flow into the culture medium storage tank 2 through the return channel 11 due to the flow of the buffer B.

図4は本発明の別の実施形態である分離装置100の構成を示している。図1の分離装置1との違いは、電荷供給流路7が複数の筒型モジュールによって構成されていることである。図1における電荷供給流路7と、図4における筒型モジュール71(筒型モジュール72、73、74についても同じ)との関係は図5(a)と図5(b)に示すとおり筒の長さが短くなっている。なお、図5において、電荷供給流路7および筒型モジュールを円筒形としているが、断面形状は円に限定されるものではなく流路を形成出来れば、多角形形状等であっても良い。また、図4においては、筒型モジュール71、72、73、74によって主流路7を構成しているが、筒型モジュールの数は4個に限るわけではなく、これより少なくても、多くても良く、必要に応じて電荷供給流路7の長さ(筒型モジュールの数)を決めれば良い。   FIG. 4 shows a configuration of a separation apparatus 100 which is another embodiment of the present invention. The difference from the separation device 1 of FIG. 1 is that the charge supply flow path 7 is constituted by a plurality of cylindrical modules. The relationship between the charge supply channel 7 in FIG. 1 and the cylindrical module 71 in FIG. 4 (the same applies to the cylindrical modules 72, 73 and 74) is the same as that shown in FIGS. 5 (a) and 5 (b). The length is shortened. In FIG. 5, the charge supply channel 7 and the cylindrical module are cylindrical, but the cross-sectional shape is not limited to a circle, and may be a polygonal shape or the like as long as the channel can be formed. Further, in FIG. 4, the main flow path 7 is constituted by the cylindrical modules 71, 72, 73, 74. However, the number of the cylindrical modules is not limited to four. It is also possible to determine the length of the charge supply channel 7 (the number of cylindrical modules) as necessary.

図4の分離装置100によって、各筒型モジュール71、72、73、74に巨核球表面に帯電している電荷と逆極性の電荷を供給した状態で、培養液が流動する際の巨核球Mと血小板Pの混合状態を例示したのが図6であり、巨核球Mが壁面に付着することにより、徐々に除去される様子を表している。なお、前述のとおり、連結する筒型モジュールの数が換えられるので、図7のように巨核球Mの濃度が低い培養液SIの分離操作においては、分離モジュール74を省いても良い。   The megakaryocyte M when the culture fluid flows in a state in which the cylindrical module 71, 72, 73, 74 is supplied with a charge having a polarity opposite to that charged on the megakaryocyte surface by the separation device 100 of FIG. FIG. 6 illustrates an example of the mixed state of the platelets P and the platelets P, and shows how the megakaryocytes M are gradually removed by adhering to the wall surface. Since the number of cylindrical modules to be connected is changed as described above, the separation module 74 may be omitted in the separation operation of the culture solution SI having a low concentration of the megakaryocyte M as shown in FIG.

ここまで説明した実施の形態においては、電荷供給流路7の壁面に電荷を供給して巨核球Mを付着しているが、培養液貯槽2に電荷を供給して培養液貯槽の壁面に巨核球Mを吸着させることも可能である。その場合の一例を、図1の分離装置1の培養液貯槽2の壁面にも電荷供給手段8から電荷を供給出来るようにした、図8の分離装置101について説明する。分離装置101では、電荷供給手段8から培養液貯槽2の壁面に、巨核球表面に帯電している電荷と逆の極性の電荷を供給した状態で、切換バルブ6の流入先をポンプ3、切換バルブ9の流出先を帰還流路11としてポンプ3を駆動する。こうすることで、培養液SIは、培養液貯槽2→電荷供給流路7→帰還流路11→培養液貯槽2を循環することにより、循環する液体内の巨核球Mが、培養液貯槽2の壁面に吸着していく。そこで、所定の循環条件(流速、時間、等)を経た段階で、切換バルブ9の流出先を回収液貯槽10とすれば、巨核球Mが含まれない回収液SOが得られる。また、この段階の、巨核球Mを含まない回収液SOを回収液貯槽10に導入するのに際して、ポンプ3の流出先が回収液貯槽10になるような流路およびバルブを設けて送液しても良い。   In the embodiment described so far, the charge is supplied to the wall surface of the charge supply channel 7 and the megakaryocytes M are attached, but the charge is supplied to the culture solution storage tank 2 and the meganucleus is applied to the wall surface of the culture solution storage tank. It is also possible to adsorb the sphere M. An example of such a case will be described with respect to the separation device 101 of FIG. 8 in which charges can be supplied from the charge supply means 8 to the wall surface of the culture medium storage tank 2 of the separation device 1 of FIG. In the separation device 101, the inflow destination of the switching valve 6 is switched to the pump 3 while the charge supply means 8 supplies the wall surface of the culture solution storage tank 2 with the charge having the opposite polarity to the charge charged on the megakaryocyte surface. The pump 3 is driven with the flow-out destination of the valve 9 as the return flow path 11. In this way, the culture solution SI is circulated through the culture solution storage tank 2 → the charge supply channel 7 → the return flow channel 11 → the culture solution storage tank 2, so that the megakaryocytes M in the circulating liquid are transferred to the culture solution storage tank 2. It will be adsorbed on the wall. Thus, if the flow-out destination of the switching valve 9 is the recovery liquid storage tank 10 after a predetermined circulation condition (flow velocity, time, etc.), the recovery liquid SO that does not contain the megakaryocytes M is obtained. At this stage, when the recovered liquid SO that does not contain the megakaryocyte M is introduced into the recovered liquid storage tank 10, a flow path and a valve are provided so that the outflow destination of the pump 3 becomes the recovered liquid storage tank 10. May be.

なお、培養液貯槽2の壁面に電荷を供給して巨核球Mを除去する場合においては、電荷供給流路7の部分は電荷供給機能のない通常の流路であっても良いが、培養液貯槽2と電荷供給流路7の両方に、巨核球表面に帯電している電荷と逆の極性の電荷を供給して、巨核球Mを付着させても良い。   In addition, when supplying a charge to the wall surface of the culture solution storage tank 2 to remove the megakaryocytes M, the charge supply channel 7 may be a normal channel without a charge supply function. The megakaryocyte M may be attached to both the storage tank 2 and the charge supply channel 7 by supplying a charge having a polarity opposite to the charge charged on the megakaryocyte surface.

本発明は巨核球と血小板が混在する培養液から巨核球を除去する用途に適するが、これに限定されるものではなく、微粒子や細胞が混在する懸濁液から特定の微粒子または細胞を除去するような用途全般にも適用可能である。   The present invention is suitable for use in removing megakaryocytes from a culture solution in which megakaryocytes and platelets are mixed. However, the present invention is not limited to this, and specific microparticles or cells are removed from a suspension containing microparticles and cells. It can also be applied to such general purposes.

1、100 分離装置
2 培養液貯槽
3 ポンプ
4 緩衝液貯槽
5 ポンプ
6 切換バルブ
7 電荷供給流路
8 電荷供給手段
9 切換バルブ
10 回収液貯槽
11 帰還流路
71、72、73、74 筒型モジュール
B 緩衝液
M 巨核球
P 血小板
SI 培養液
SO 回収液
DESCRIPTION OF SYMBOLS 1,100 Separation apparatus 2 Culture solution storage tank 3 Pump 4 Buffer solution storage tank 5 Pump 6 Switching valve 7 Charge supply flow path 8 Charge supply means 9 Switching valve 10 Recovery liquid storage tank 11 Return flow path 71, 72, 73, 74 Tubular module B buffer M megakaryocyte P platelet SI culture solution SO recovery solution

Claims (5)

巨核球と血小板が混在する培養液から巨核球を除去する分離装置であって、
培養液を貯える培養液貯槽と、
前記培養液貯槽内の培養液を送液する機能を有する培養液送液手段と、
培養液から巨核球を除去した回収液を回収して貯える回収液貯槽と、
電荷供給手段とを備える分離装置。
A separator for removing megakaryocytes from a culture solution containing megakaryocytes and platelets,
A culture solution storage tank for storing the culture solution;
A culture solution feeding means having a function of feeding the culture solution in the culture solution storage tank;
A recovery liquid storage tank for recovering and storing the recovery liquid from which the megakaryocytes have been removed from the culture liquid;
A separation device comprising charge supply means.
請求項1に記載の分離装置であって、
培養液貯槽と回収液貯槽間に電荷供給手段として機能する電荷供給流路を備え、
前記電荷供給流路の回収液貯槽側の接続先を、回収液貯槽または、培養液貯槽への帰還流路の何れかに切り換える機能を有する流出先切換バルブを備え、
前記電荷供給流路に巨核球表面に帯電している電荷と逆の極性の電荷を供給することで、流動する培養液中の巨核球を前記電荷供給流路の壁面に付着させる機能を有していることを特徴とする分離装置。
The separation device according to claim 1,
A charge supply channel functioning as a charge supply means is provided between the culture solution storage tank and the recovery solution storage tank,
An outlet switching valve having a function of switching the connection destination of the charge supply channel on the recovery liquid storage tank side to either the recovery liquid storage tank or the return flow path to the culture liquid storage tank;
By supplying a charge of the opposite polarity to the charge charged on the megakaryocyte surface to the charge supply channel, the megakaryocyte in the flowing culture solution is attached to the wall surface of the charge supply channel. Separation device characterized by that.
請求項2に記載の分離装置であって、
緩衝液を貯える緩衝液貯槽と、
前記緩衝液貯槽内の緩衝液を送液する緩衝液送液手段と、
前記電荷供給流路入口の接続先を、培養液送液手段または緩衝液送液手段の何れかに切り換える機能を有する流入先切換バルブを備え、
緩衝液で前記壁面に付着している付着物を剥離して、電荷供給流路を洗浄する機能を有していることを特徴とする分離装置。
The separation device according to claim 2,
A buffer storage tank for storing the buffer solution;
A buffer solution feeding means for feeding a buffer solution in the buffer solution storage tank;
An inflow destination switching valve having a function of switching the connection destination of the charge supply channel inlet to either the culture solution feeding means or the buffer solution feeding means;
A separation device having a function of separating the deposits adhering to the wall surface with a buffer solution and washing the charge supply channel.
巨核球と血小板が混在する培養液を、培養液貯槽から流路に流動させる過程において、
培養液貯槽及び流路の壁面に、巨核球表面に帯電している電荷と逆の極性の電荷を供給して、巨核球を前記壁面に付着させることにより、培養液から巨核球を除去することを特徴とする分離方法。
In the process of flowing the culture solution containing megakaryocytes and platelets from the culture solution storage tank to the flow path,
Removing the megakaryocytes from the culture solution by supplying a charge of the opposite polarity to the charge on the megakaryocyte surface to the wall of the culture medium reservoir and the flow path, and attaching the megakaryocytes to the wall surface Separation method characterized by.
請求項4に記載の分離方法であって、全電荷供給流路の壁面に巨核球に帯電している電荷と同じ極性の電荷を供給することで、前記壁面に付着している付着物を剥離して、電荷供給流路を洗浄することを特徴とする分離方法。   5. The separation method according to claim 4, wherein a charge having the same polarity as a charge charged on a megakaryocyte is supplied to a wall surface of a total charge supply flow channel, thereby peeling off the attached matter attached to the wall surface. And the separation method characterized by washing | cleaning an electric charge supply flow path.
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