JP2000139454A - Separation and recovery of cell and recovery required cell-containing liquid - Google Patents

Separation and recovery of cell and recovery required cell-containing liquid

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Publication number
JP2000139454A
JP2000139454A JP10327539A JP32753998A JP2000139454A JP 2000139454 A JP2000139454 A JP 2000139454A JP 10327539 A JP10327539 A JP 10327539A JP 32753998 A JP32753998 A JP 32753998A JP 2000139454 A JP2000139454 A JP 2000139454A
Authority
JP
Japan
Prior art keywords
cell
cells
capturing means
temperature
recovery
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
JP10327539A
Other languages
Japanese (ja)
Inventor
Masaya Sumida
政哉 澄田
Shuji Terajima
修司 寺嶋
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.)
Asahi Kasei Medical Co Ltd
Original Assignee
Asahi Medical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Asahi Medical Co Ltd filed Critical Asahi Medical Co Ltd
Priority to JP10327539A priority Critical patent/JP2000139454A/en
Publication of JP2000139454A publication Critical patent/JP2000139454A/en
Pending legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M47/00Means for after-treatment of the produced biomass or of the fermentation or metabolic products, e.g. storage of biomass
    • C12M47/04Cell isolation or sorting
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M47/00Means for after-treatment of the produced biomass or of the fermentation or metabolic products, e.g. storage of biomass
    • C12M47/20Heating or cooling

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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Zoology (AREA)
  • Wood Science & Technology (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Organic Chemistry (AREA)
  • Chemical & Material Sciences (AREA)
  • Biotechnology (AREA)
  • Sustainable Development (AREA)
  • Microbiology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Biomedical Technology (AREA)
  • Clinical Laboratory Science (AREA)
  • Cell Biology (AREA)
  • Molecular Biology (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Medicines Containing Material From Animals Or Micro-Organisms (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for separating and recovering cells capable of recovering a nuclear cell such as hematopoietic stem cell in high yield by an inexpensive, simple and short time operation. SOLUTION: A cell-containing liquid stored at a cell-containing temperature A and containing a cell required for recovery and a cell required for removal is introduced into a cell capturing means substantially capturing the cell required for recovery and substantially passing the cell required for removal at a cell- separating temperature B, then the liquid containing the cell required for removal is released from the cell capturing means. Next, a liquid is introduced into the cell capturing means and the cell required for recovery capturing in the cell capturing means is recovered from the cell capturing means. The cell-storing temperature A is related to the cell-separating temperature B as follows: 0 deg.C<A<30 deg.C, 0 deg.C<B<30 deg.C and (absolute value of A-B) <15 deg.C.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、各種の細胞の混合
溶液から必要な細胞のみを分離、回収する方法に関す
る。得られた細胞は造血幹細胞移植療法等、細胞を用い
て行う各種疾病の治療及び免疫学や細胞生物学等の基礎
科学分野で用いることが可能となる。
The present invention relates to a method for separating and recovering only necessary cells from a mixed solution of various cells. The obtained cells can be used in the treatment of various diseases using cells, such as hematopoietic stem cell transplantation therapy, and in basic science fields such as immunology and cell biology.

【0002】[0002]

【従来の技術】臍帯血幹細胞は、ドナー侵襲皆無の造血
幹細胞移植ソースとして注目を集めており、欧米諸国を
中心にさかんに臨床応用が試みられている。臍帯血幹細
胞は、他の造血幹細胞移植、即ち、骨髄移植あるいは末
梢血幹細胞移植のようにドナーから採取されてすぐ患者
に移植されることはまれであるので、採取時から使用時
まで保存しておくことが必要である(特に非血縁者間移
植の場合)。臍帯血は凍結保存に際し、解凍後の破壊赤
血球による副作用防止及び凍結保存時の体積を小さくす
る目的で、有核細胞を分離(赤血球を除去)すべきであ
るとされており、現在はほとんどの場合に分離保存が行
われている(南江堂、「末梢血幹細胞移植」173ペー
ジ)。特公平8−69号公報には、臍帯血をフィコール
ハイパキュー(比重液による遠心分離法であり、以下こ
れをフィコール法と略す)で分離するためのプロトコー
ルの詳細が開示されている。しかしながら、フィコール
法は実験室レベルの、非常に煩雑で長時間を要する操作
であるという問題がある。また、WO96/17514
公報にはヒドロキシエチルスターチを用いて臍帯血中の
赤血球を凝集沈降分離し、有核細胞濃縮液を得るための
バッグシステム、方法及びその方法により得られた細胞
液が開示されている。本法は煩雑な操作を少なくすると
いう点では従来のフィコール法と比べ若干の改善となっ
ているが、遠心分離が2回必要であるため、やはり長時
間の作業を要することになる。一方、フィコール法や赤
血球凝集除去法に代わる造血幹細胞分離方法も散見され
るようになった。特開平8−104643号公報では赤
血球は通過するフィルターに造血幹細胞を捕捉させた
後、最初の通液方向とは逆方向の液流を惹起させて造血
幹細胞を回収する方法が開示されている。ところで、臍
帯血は分娩時に胎盤及び/又は臍帯から採血され、細胞
分離に供せられるまで、通常10〜72時間保存され
る。この時の温度としては、冷蔵(約4℃)ないし室温
(約25℃)が採用されている。幹細胞の細胞機能維持
の観点からは、室温保存の方が好ましいという報告(C
ampos他:Cryobiology、vol.3
2、1995)、両者差が無いという報告(斉藤、他:
日本輸血学会誌第44巻5号、1998年)がある。し
かしながら、細胞分離性能の観点から、いかなる温度が
最適かという検討、より詳しく言うと細胞分離に供せら
れるまでの細胞保存温度(以下単に「細胞保存温度」と
略す)と細胞分離に供せられる際の温度(以下単に「細
胞分離温度」と略す)をコントロールして、細胞分離時
の細胞回収率の向上や細胞分離処理に要する時間(以下
単に「細胞分離時間」と略す)の短縮化を目指した検討
は一切なされていない。前述の特開平8−104643
号公報においても細胞保存温度、細胞分離温度の記載は
一切無い。
2. Description of the Related Art Cord blood stem cells have attracted attention as a source of hematopoietic stem cell transplantation without donor invasion, and clinical applications thereof have been attempted mainly in Europe and the United States. Umbilical cord blood stem cells are rarely transplanted to patients immediately after being collected from a donor like other hematopoietic stem cell transplants, i.e., bone marrow transplants or peripheral blood stem cell transplants. (Especially for unrelated transplants). It is said that umbilical cord blood should be separated from nucleated cells (removal of red blood cells) in order to prevent side effects due to destroyed red blood cells after thawing and to reduce the volume during frozen storage during cryopreservation. In some cases, isolation and preservation are performed (Nankodo, “Peripheral Blood Stem Cell Transplantation”, page 173). Japanese Patent Publication No. 8-69 discloses details of a protocol for separating umbilical cord blood by Ficoll-Hypaque (a centrifugation method using a specific gravity solution, which is hereinafter abbreviated as Ficoll method). However, the Ficoll method has a problem that it is an extremely complicated and time-consuming operation at the laboratory level. WO96 / 17514
The publication discloses a bag system and a method for agglutinating and separating erythrocytes in cord blood using hydroxyethyl starch to obtain a nucleated cell concentrate, and a cell solution obtained by the method. This method is a slight improvement over the conventional Ficoll method in terms of reducing complicated operations, but it also requires a long operation because centrifugation is required twice. On the other hand, hematopoietic stem cell separation methods, which are alternatives to the Ficoll method and the hemagglutination removal method, have also been occasionally found. JP-A-8-104463 discloses a method of collecting hematopoietic stem cells by causing a filter through which red blood cells pass to capture hematopoietic stem cells and then inducing a liquid flow in a direction opposite to the first flow direction. By the way, umbilical cord blood is collected from the placenta and / or umbilical cord at the time of delivery and is usually stored for 10 to 72 hours until it is subjected to cell separation. As the temperature at this time, refrigeration (about 4 ° C.) to room temperature (about 25 ° C.) is employed. From the viewpoint of maintaining cell functions of stem cells, it was reported that storage at room temperature was more preferable (C
ampos et al .: Cryobiology, vol. 3
2, 1995), reports that there is no difference between them (Saito, et al .:
Japanese Society of Transfusion, Vol. 44, No. 5, 1998). However, from the viewpoint of cell separation performance, it is examined what temperature is optimal, more specifically, cell storage temperature (hereinafter simply referred to as “cell storage temperature”) and cell separation temperature before cell separation is performed. Temperature (hereinafter simply referred to as “cell separation temperature”) to improve the cell recovery rate during cell separation and shorten the time required for cell separation processing (hereinafter simply referred to as “cell separation time”). No studies were aimed at. Japanese Patent Application Laid-Open No. 8-104463 described above.
No publication describes the cell storage temperature or cell separation temperature.

【0003】[0003]

【発明が解決しようとする課題】本発明の目的は、安価
で且つ簡便・短時間操作で、造血幹細胞等、有核細胞が
高率に回収できる細胞分離回収方法を提供することにあ
る。
SUMMARY OF THE INVENTION An object of the present invention is to provide a method for separating and recovering nucleated cells such as hematopoietic stem cells at a high rate at a low cost, with simple and easy operation.

【0004】[0004]

【課題を解決するための手段】本発明者らはかかる問題
点を解決すべく、細胞保存温度と細胞分離温度に着目し
て鋭意検討を進めた結果、細胞保存温度と細胞分離温度
の差が細胞分離性能に多大な影響を及ぼすことを見出
し、本発明を完成するに至った。即ち、本発明は細胞保
存温度Aで保存された回収必要細胞と除去対象細胞を含
む細胞含有液を、該回収必要細胞を実質的に捕捉し該除
去対象細胞を実質的に通過させる細胞捕捉手段に細胞分
離温度Bで導入し、除去対象細胞含有液を該細胞捕捉手
段から導出させ、次に該細胞捕捉手段に液体を導入して
該細胞捕捉手段に捕捉されている該回収必要細胞を該細
胞捕捉手段から回収する細胞分離方法において、細胞保
存温度Aと細胞分離温度Bが、0℃<A<30℃且つ0
℃<B<30℃且つ|A−B|<15℃であることを特
徴とする細胞分離回収方法である。また本発明は細胞保
存温度Aで保存された回収必要細胞と除去対象細胞を含
む細胞含有液を、該回収必要細胞を実質的に捕捉し該除
去対象細胞を実質的に通過させる細胞捕捉手段に細胞分
離温度Bで導入し、除去対象細胞含有液を該細胞捕捉手
段から導出させ、次に該細胞捕捉手段に液体を導入して
該細胞捕捉手段に捕捉されている該回収必要細胞を該細
胞捕捉手段から回収する細胞分離方法により得られた実
質的に除去対象細胞を含まない細胞含有液であって、細
胞保存温度Aと細胞分離温度Bが、0℃<A<30℃且
つ0℃<B<30℃且つ|A−B|<15℃である回収
必要細胞含有液である。
Means for Solving the Problems In order to solve these problems, the present inventors have conducted intensive studies focusing on the cell storage temperature and the cell separation temperature, and as a result, the difference between the cell storage temperature and the cell separation temperature has been found. The inventors have found that the present invention has a great effect on cell separation performance, and have completed the present invention. That is, the present invention provides a cell capturing means for substantially capturing a cell containing a cell containing a cell to be recovered and a cell to be removed stored at a cell storage temperature A, and substantially passing the cell to be removed. At a cell separation temperature B, and a liquid containing the cells to be removed is led out from the cell capturing means. Then, a liquid is introduced into the cell capturing means to collect the cells to be collected which have been captured by the cell capturing means. In the cell separation method of recovering from the cell capturing means, the cell storage temperature A and the cell separation temperature B are 0 ° C. <A <30 ° C. and 0 ° C.
C. <B <30.degree. C. and | AB | <15.degree. C. In addition, the present invention provides a cell-containing means containing a cell-containing liquid containing the cells to be recovered and the cells to be removed stored at the cell storage temperature A, which substantially captures the cells to be recovered and substantially passes the cells to be removed. The cell-retaining temperature is introduced at the cell separation temperature B, and the liquid containing the cells to be removed is led out from the cell-capturing means. A cell-containing liquid substantially free of cells to be removed obtained by the cell separation method recovered from the capturing means, wherein the cell storage temperature A and the cell separation temperature B are 0 ° C <A <30 ° C and 0 ° C < B <30 ° C. and | A−B | <15 ° C. The cell-containing solution requires recovery.

【0005】[0005]

【発明の実施の形態】以下本発明を詳細に説明する。本
発明で言う回収必要細胞とは分離回収して何らかの用途
に用いる細胞を言い、除去対象細胞とは先述の用途には
不要であるか、又は何らかの病因細胞である等の理由
で、回収必要細胞に混入することが問題となるため積極
的に除去することが必要である細胞のことを言う。これ
らを含む細胞含有液としては、末梢血、骨髄、臍帯血
(臍帯血管から採取されたものだけでなく、胎盤血管か
ら採取されたものも含む)、リンパ液及びこれらに遠心
分離等何らかの処理を施したもの、あるいは各種臓器や
組織から抽出した細胞を何らかの液体に再浮遊させたも
のがあげられる。本発明で言う回収必要細胞を実質的に
捕捉し、除去対象細胞を実質的に通過させる細胞捕捉手
段とは、例えば回収必要細胞は実質的に捕捉し、除去対
象細胞は実質的に通過させる材料を充填した液体流入口
と液体流出口を有する容器、あるいは成型容器で、容器
内面に細胞捕捉面が存在するものがあげられる。回収必
要細胞を実質的に捕捉し、除去対象細胞は実質的に通過
する材料は、回収必要細胞を選択的に捕捉できる限り通
常用いられている細胞捕捉材であればいかなる材料も使
用できるが、成型性、滅菌性や細胞毒性が低いという点
で好ましいものを例示すると、ポリエチレン、ポリプロ
ピレン、ポリスチレン、アクリル樹脂、ナイロン、ポリ
エステル、ポリカーボネート、ポリアクリルアミド、ポ
リウレタン等の合成高分子、アガロース、セルロース、
酢酸セルロース、キチン、キトサン、アルギン酸塩等の
天然高分子、ハイドロキシアパタイト、ガラス、アルミ
ナ、チタニア等の無機材料、ステンレス、チタン、アル
ミニウム等の金属があげられる。また、これらの捕捉材
はこのままでも用いることができるが、細胞の選択的通
過あるいは捕捉を行う等の必要に応じ、表面改質を施し
たものでもよい。例えば、血小板通過性を高めるにはW
O87/05812公報で提案されている非イオン性親
水基と塩基性含窒素官能基を有するポリマーのコートに
よる方法等があげられ、細胞の選択的捕捉を行う場合、
アミノ酸、ペプチド、糖類、糖タンパク(抗体、接着分
子等のバイオリガンドを含む)といった特定の細胞に親
和性のあるリガンドを、例えば特開平2−261833
号公報で提案されているハロアセトアミド法により固定
する方法等があげられる。また、捕捉材の形状としては
粒状、繊維塊、織布、不織布、スポンジ状多孔質体、平
板等があげられるが、体積あたりの表面積が大きいとい
う点で粒状、繊維塊、織布、不織布、スポンジ状多孔質
体が好ましく、更に、取り扱い性の点から繊維塊、織
布、不織布、スポンジ状構造体といった多孔質構造体が
好ましく、中でも不織布、スポンジ状構造体が細胞液の
流れ性、製造性の点からより好ましい。不織布の場合、
抗CD34モノクローナル抗体等、特定の細胞に特異的
に結合するいわゆるバイオリガンド類を表面に固定しな
い場合、通常、繊維径は1.0μm以上30μm以下で
あり、好ましくは1.0μm以上20μm以下であり、
更により好ましくは1.5μm以上10μm以下であ
る。1.0μm未満では回収必要細胞が強固に捕捉され
てしまい回収困難となる可能性があり好ましくない。3
0μmを超えると、回収必要細胞は繊維に捕捉されず素
通りする可能性が高くなる。いずれの場合でも回収率の
低下につながるおそれがあるので好ましくない。また、
スポンジ状構造体の場合、孔径は通常2.0μm以上3
0μm以下であり、好ましくは2.5μm以上25μm
以下であり、更により好ましくは3.0μm以上20μ
m以下である。2.0μm未満では流れ性が著しく劣
り、通液自体が困難になるおそれがあり、また30μm
を超えると、回収必要細胞の捕捉率の低下を招くので好
ましくない。回収必要細胞は捕捉し、除去対象細胞は実
質的に通過する材料を充填する容器の材質としては、成
型性、滅菌性や細胞毒性が低いという点で好ましいもの
を例示すると、ポリエチレン、ポリプロピレン、ポリス
チレン、アクリル樹脂、ナイロン、ポリエステル、ポリ
カーボネート、ポリアクリルアミド、ポリウレタン、塩
化ビニル等の合成高分子、ハイドロキシアパタイト、ガ
ラス、アルミナ、チタニア等の無機材料、ステンレス、
チタン、アルミニウム等の金属があげられる。本発明で
言う「回収必要細胞は実質的に捕捉し」とは回収必要細
胞を60%以上捕捉することを言い、また「除去対象細
胞は実質的に通過する」とは細胞含有液中の除去対象細
胞が60%以上通過することを言う。本発明において、
前記細胞捕捉手段に導入して捕捉されている回収必要細
胞を回収する液体は生理的溶液であればいかなるものも
使用可能であるが、幾つか例示すると、生理食塩水、D
−PBSやHBSSなどの緩衝液、RPMI1640な
どの培地があげられる。これらの生理的溶液に、、細胞
保護、栄養補給、凍結保存時の凍害防止、粘度向上(回
収率向上に有効な場合がある)等の目的で必要に応じ、
デキストラン、ヒドロキシエチルデンプン、ジメチルス
ルホキシド、アルブミン、グロブリン、ゼラチン、グル
コース、サッカロース、トレハロース等を添加してもよ
い。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail. The cells requiring recovery referred to in the present invention refer to cells that are separated and recovered and used for some purpose, and the cells to be removed are unnecessary for the above-mentioned purposes or are cells that need to be recovered because they are any pathogenic cells. It is a cell that needs to be actively removed because it causes a problem of contamination. Cell-containing solutions containing these include peripheral blood, bone marrow, umbilical cord blood (including not only those collected from umbilical cord blood vessels, but also those collected from placental blood vessels), lymph fluids, and those subjected to some treatment such as centrifugation. Or cells obtained by resuspending cells extracted from various organs or tissues in some liquid. The cell-capturing means for substantially capturing the cells to be recovered and substantially passing the cells to be removed as referred to in the present invention is, for example, a material that substantially captures the cells to be recovered and substantially passes the cells to be removed. And a molded container having a liquid inlet and a liquid outlet filled with, and having a cell trapping surface on the inner surface of the container. Any material can be used as long as the material that substantially captures the cells requiring recovery and the cells to be removed substantially pass is used as long as the material can be selectively captured. Examples of preferable moldability, sterility and low cytotoxicity are polyethylene, polypropylene, polystyrene, acrylic resin, nylon, polyester, polycarbonate, polyacrylamide, polyurethane and other synthetic polymers, agarose, cellulose,
Examples include natural polymers such as cellulose acetate, chitin, chitosan, and alginate; inorganic materials such as hydroxyapatite, glass, alumina, and titania; and metals such as stainless steel, titanium, and aluminum. These trapping materials can be used as they are, but may be surface-modified as necessary, such as for selective passage or trapping of cells. For example, to increase platelet permeability W
O87 / 05812 discloses a method of coating with a polymer having a nonionic hydrophilic group and a basic nitrogen-containing functional group, and the like.
Ligands having affinity for specific cells, such as amino acids, peptides, saccharides, glycoproteins (including bioligands such as antibodies and adhesion molecules) are disclosed in, for example, JP-A-2-261833.
And a method of fixing by the haloacetamide method proposed in Japanese Patent Application Publication No. Examples of the shape of the trapping material include granular, fibrous mass, woven fabric, nonwoven fabric, sponge-like porous body, and flat plate, but in terms of a large surface area per volume, granular, fibrous mass, woven fabric, nonwoven fabric, A sponge-like porous body is preferable, and a porous structure such as a fiber mass, a woven fabric, a nonwoven fabric, and a sponge-like structure is preferable from the viewpoint of handleability. It is more preferable from the viewpoint of properties. For non-woven fabric,
When so-called bioligands that specifically bind to specific cells such as an anti-CD34 monoclonal antibody are not immobilized on the surface, the fiber diameter is usually 1.0 μm or more and 30 μm or less, preferably 1.0 μm or more and 20 μm or less. ,
Still more preferably, it is 1.5 μm or more and 10 μm or less. If the thickness is less than 1.0 μm, cells that need to be collected may be firmly captured and may be difficult to collect, which is not preferable. 3
If it exceeds 0 μm, the cells that need to be collected are more likely to pass through without being captured by the fibers. In either case, the recovery rate may be reduced, which is not preferable. Also,
In the case of a sponge-like structure, the pore size is usually 2.0 μm or more and 3
0 μm or less, preferably 2.5 μm or more and 25 μm
Or less, still more preferably 3.0 μm or more and 20 μm or more.
m or less. If it is less than 2.0 μm, the flowability is extremely poor, and it may be difficult to pass the liquid itself.
Exceeding the number is not preferred because it leads to a decrease in the capture rate of the cells requiring recovery. Cells that need to be collected are captured, and the cells to be removed are filled with a material that substantially passes through the container. Synthetic polymers such as acrylic resin, nylon, polyester, polycarbonate, polyacrylamide, polyurethane, and vinyl chloride; inorganic materials such as hydroxyapatite, glass, alumina, and titania; stainless steel;
Examples include metals such as titanium and aluminum. In the present invention, "substantially capture the cells required for recovery" means capturing 60% or more of the cells required for recovery, and "substantial passage of the cells to be removed" means removal in the cell-containing liquid. It means that the target cells pass by 60% or more. In the present invention,
Any liquid may be used as a liquid for recovering cells to be recovered which has been captured by being introduced into the cell capturing means, as long as it is a physiological solution.
-Buffers such as PBS and HBSS, and culture media such as RPMI1640. These physiological solutions may be added as necessary for the purpose of protecting cells, supplementing nutrition, preventing frost damage during cryopreservation, improving viscosity (may be effective for improving recovery rate), etc.
Dextran, hydroxyethyl starch, dimethyl sulfoxide, albumin, globulin, gelatin, glucose, saccharose, trehalose and the like may be added.

【0006】本発明による細胞分離回収方法では細胞含
有液を細胞保存温度Aで保存するものであるが、Aは通
常0℃を超え30℃未満であり、好ましくは2℃以上2
5℃以下であり、更により好ましくは3℃以上25℃以
下である。Aが0℃以下でも30℃以上でも細胞機能に
ダメージを与えるおそれがあり好ましくない。また、本
発明による細胞分離回収方法では細胞含有液を細胞分離
温度Bで細胞捕捉手段に導入するものであるが、Bは通
常0℃を超え30℃未満であり、好ましくは2℃以上2
5℃以下であり、更により好ましくは3℃以上25℃以
下である。Bが0℃以下でも30℃以上でも細胞機能に
ダメージを与えるおそれがあり好ましくない。また本発
明では細胞保存温度Aと細胞分離温度Bの差の絶対値|
A−B|が15℃未満であり、好ましくは10℃未満、
更により好ましくは5℃未満である。15℃以上では細
胞処理時間の増大と細胞回収率の低下が観察されており
好ましくない。|A−B|が15℃以上で細胞処理時間
が増大及び/又は細胞回収率が低下する理由は明らかで
はないが、本発明者は以下のように考察している。細胞
にとって細胞捕捉手段に捕捉されることは少なからずス
トレスが生じていると考えられる。その際、細胞保存温
度と細胞分離温度の差が大きいということは細胞周囲の
環境変化によるストレスをも加えてしまうこととなり、
最悪の場合細胞が破壊されDNA等の粘着性物質が放出
されるか、そこまで至らないとしてもストレスによる刺
激を原因とする凝固系の活性化(フィブリンの析出)、
細胞自身の粘着能の亢進等が惹起されると考える。これ
らの結果として細胞処理時間の増大、細胞回収率の低下
に結びつくものと推察している。本発明による細胞分離
回収方法は回収必要細胞が有核細胞である場合に好適に
用いられる。有核細胞とは細胞内に核を有する細胞のこ
とを言い、例えば白血球、顆粒球、好中球、好酸球、好
塩基球、骨髄球、赤芽球、リンパ球、Tリンパ球、ヘル
パーTリンパ球、サプレッサーTリンパ球、細胞傷害性
Tリンパ球、Bリンパ球、NK細胞、NKT細胞、単
球、マクロファージ、樹状細胞、造血幹細胞、破骨細
胞、骨芽細胞、骨細胞、繊維芽細胞、軟骨芽細胞等があ
げられる。また、本発明で言う有核細胞含有液とは前記
有核細胞を含有する液体のことであり、例えば末梢血、
リンパ球、骨髄液、臍帯血、あるいはこれらに何らかの
処理を施した液体等があげられる。
In the method for separating and recovering cells according to the present invention, the cell-containing solution is stored at a cell storage temperature A. A is usually higher than 0 ° C. and lower than 30 ° C., preferably 2 ° C. or higher and 2 ° C. or lower.
The temperature is 5 ° C or less, and still more preferably 3 ° C or more and 25 ° C or less. If A is 0 ° C or lower or 30 ° C or higher, cell functions may be damaged, which is not preferable. In the method for separating and collecting cells according to the present invention, the cell-containing liquid is introduced into the cell capturing means at the cell separation temperature B. B is usually higher than 0 ° C and lower than 30 ° C, preferably 2 ° C or higher and 2 ° C or higher.
The temperature is 5 ° C or less, and still more preferably 3 ° C or more and 25 ° C or less. If B is 0 ° C. or lower or 30 ° C. or higher, cell functions may be damaged, which is not preferable. In the present invention, the absolute value of the difference between the cell storage temperature A and the cell separation temperature B |
AB | is less than 15 ° C, preferably less than 10 ° C,
Even more preferably, it is below 5 ° C. At 15 ° C. or higher, an increase in cell treatment time and a decrease in cell recovery rate are observed, which is not preferable. The reason why the cell treatment time increases and / or the cell recovery rate decreases when | AB | is 15 ° C or higher is not clear, but the present inventors consider as follows. It is considered that the cell is trapped by the cell capturing means to a considerable extent, causing stress. At that time, the large difference between the cell storage temperature and the cell separation temperature means that stress due to environmental changes around the cells will also be applied,
In the worst case, cells are destroyed and sticky substances such as DNA are released, or even if it is not reached, activation of the coagulation system due to stress stimulation (precipitation of fibrin),
It is considered that an increase in the adhesion ability of the cells themselves is caused. It is presumed that these results lead to an increase in cell treatment time and a decrease in cell recovery rate. The cell separation and collection method according to the present invention is suitably used when the cells requiring collection are nucleated cells. A nucleated cell refers to a cell having a nucleus in the cell, for example, leukocyte, granulocyte, neutrophil, eosinophil, basophil, myelocyte, erythroblast, lymphocyte, T lymphocyte, helper T lymphocytes, suppressor T lymphocytes, cytotoxic T lymphocytes, B lymphocytes, NK cells, NKT cells, monocytes, macrophages, dendritic cells, hematopoietic stem cells, osteoclasts, osteoblasts, bone cells, fibers Blasts, chondroblasts and the like. Further, the nucleated cell-containing liquid in the present invention is a liquid containing the nucleated cells, for example, peripheral blood,
Examples include lymphocytes, bone marrow fluid, umbilical cord blood, and liquids obtained by subjecting these to some treatment.

【0007】[0007]

【実施例】以下に実施例により本発明をより詳細に説明
するが、本発明はこれらにより限定されるものではな
い。
EXAMPLES The present invention will be described in more detail with reference to the following Examples, but it should not be construed that the invention is limited thereto.

【実施例1】細胞分離器 容器外寸(縦×横×厚み)41×41×18mmで液体
流出口と液体流入口を対角線上にもつポリカーボネート
製容器の入口側に平均繊維径2.3μmのポリエステル
不織布18枚を、出口側に平均繊維径12μmのポリエ
ステル不織布16枚を充填し細胞分離器とした。なお、
充填密度は0.2g/cm3、有効濾過面積12.25
cm2、有効濾過長12.4mmであった。また、この
細胞分離器に血小板通過性を付与する目的で、親水性ポ
リマーのコーティングを行った。即ち、ヒドロキシエチ
ルメタクリレート・ジメチルアミノエチルメタクリレー
ト共重合体(ヒドロキシエチルメタクリレートとジメチ
ルアミノエチルメタクリレートのモル比=97:3)の
1%エタノール溶液を該フィルターの入口側から通液し
た後、窒素ガスを通して乾燥させた。 細胞分離操作 娩出後の胎盤及び臍帯から50mLディスポーザブルシ
リンジ(18ゲージ針付き)を用いて、臍帯血を予めC
PD1.5mLが入っている10mL採血管10本に採
取した。採取した臍帯血は200mLの血液バッグに移
した。この血液バッグを22℃の恒温器にて24時間保
存した。24時間後、恒温器から血液バッグ2を取り出
し、すみやかに細胞分離操作を行った。即ち、この血液
バッグを途中に細胞回収用バッグ5が接続した三方活栓
4とメッシュチャンバー3を有するチューブで、で作
製した細胞分離器1の入口側に接続した。細胞分離器1
の出口側は途中に回収用シリンジ接続用の三方活栓6を
有するチューブでドレーンバッグ7を接続した。原料血
液バッグ2中の有核細胞含有液を約60cmの落差で細
胞分離器に通液し、細胞分離器1から流出する赤血球含
有液をドレーンバッグ7に排液した。次に、三方活栓6
に市販のデキストラン40生理食塩水溶液(ヒト血清ア
ルブミンを4%含む)25mLを入れた30mLディス
ポーザブルシリンジを接続し、三方活栓6をシリンジと
細胞分離器のみが連通する方向に回し、また三方活栓4
を細胞分離器1と細胞回収用バッグ5のみが連通する方
向に回した後、シリンジを押して細胞分離器内に捕捉さ
れている細胞を細胞回収用バッグ5に回収した。 分析 有核細胞数、赤血球数、血小板数は自動血球計算機にて
測定、有核細胞中のCD34陽性率はFITC標識抗C
D34抗体を用い、SSC−FITCに展開するフロー
サイトメトリー法(宮崎、他:日常診療と血液、第5巻
2号、21〜24ページ、1995年)を用いて測定し
た。なお、回収率、除去率の算出方法は以下のとおりで
ある。 回収率(%)=100×(回収後細胞数/原料血液中の
細胞数) 除去率(%)=100−100×(回収後細胞数/原料
血液中の細胞数) また、濾過開始から濾過終了までを細胞分離時間とし、
ストップウォッチで計測した。 結果 結果のまとめを表1に示す。回収した細胞液中には有核
細胞、CD34陽性細胞が高率に回収できており、細胞
分離時間も短いことが分かる。
Example 1 Cell Separator The outer dimensions of the container (length × width × thickness) were 41 × 41 × 18 mm, and the average fiber diameter was 2.3 μm on the inlet side of a polycarbonate container having a liquid outlet and a liquid inlet on a diagonal line. Eighteen polyester non-woven fabrics were filled on the outlet side with 16 polyester non-woven fabrics having an average fiber diameter of 12 μm to prepare a cell separator. In addition,
The packing density is 0.2 g / cm 3 and the effective filtration area is 12.25.
cm 2 and an effective filtration length of 12.4 mm. Further, in order to impart platelet permeability to the cell separator, coating with a hydrophilic polymer was performed. That is, after passing a 1% ethanol solution of a hydroxyethyl methacrylate / dimethylaminoethyl methacrylate copolymer (molar ratio of hydroxyethyl methacrylate to dimethylaminoethyl methacrylate = 97: 3) from the inlet side of the filter, nitrogen gas was passed. Let dry. Cell Separation Procedure Umbilical cord blood was previously collected from the placenta and umbilical cord after delivery using a 50 mL disposable syringe (with an 18 gauge needle).
The blood was collected in 10 10 mL blood collection tubes containing 1.5 mL of PD. The collected cord blood was transferred to a 200 mL blood bag. This blood bag was stored in a thermostat at 22 ° C. for 24 hours. Twenty-four hours later, the blood bag 2 was taken out of the incubator, and the cell separation operation was immediately performed. That is, this blood bag was connected to the inlet side of the cell separator 1 prepared by using a tube having the three-way cock 4 and the mesh chamber 3 to which the cell collection bag 5 was connected in the middle. Cell separator 1
Was connected to a drain bag 7 with a tube having a three-way cock 6 for connecting a syringe for recovery. The nucleated cell-containing liquid in the source blood bag 2 was passed through the cell separator with a head of about 60 cm, and the erythrocyte-containing liquid flowing out of the cell separator 1 was drained into the drain bag 7. Next, three-way cock 6
A 30 mL disposable syringe containing 25 mL of a commercially available dextran 40 physiological saline solution (containing 4% of human serum albumin) is connected thereto, and the three-way cock 6 is turned in a direction in which only the syringe and the cell separator communicate with each other.
Was turned in a direction in which only the cell separator 1 and the cell collection bag 5 communicated with each other, and then the syringe was pushed to collect the cells captured in the cell separator into the cell collection bag 5. Analysis The number of nucleated cells, the number of erythrocytes and the number of platelets were measured by an automatic hemocytometer, and the CD34 positive rate in nucleated cells was determined by FITC-labeled anti-C.
The measurement was performed using the D34 antibody by a flow cytometry method developed on SSC-FITC (Miyazaki, et al .: Daily Practice and Blood, Vol. 5, No. 2, 21-24, 1995). The method of calculating the recovery rate and the removal rate is as follows. Recovery rate (%) = 100 × (number of cells after collection / number of cells in source blood) Removal rate (%) = 100−100 × (number of cells after collection / number of cells in source blood) The time until the end is the cell separation time,
It was measured with a stopwatch. Results Table 1 summarizes the results. It can be seen that nucleated cells and CD34-positive cells were recovered at a high rate in the recovered cell solution, and that the cell separation time was short.

【0008】[0008]

【比較例1】細胞分離器 実施例1と同様の細胞分離器を用いた。 細胞分離操作 22℃の恒温器の代わりに4℃の冷蔵庫を用いて臍帯血
を保存すること、及びすみやかに細胞分離を行う代わり
に室温(24℃)で1時間放置した後に細胞分離を行う
こと以外は実施例1と同様の操作を行った。 分析 実施例1と同様の方法で分析した。 結果 結果のまとめを表2に示す。有核細胞、CD34陽性細
胞の回収率は実施例1と比べて低値であり、細胞分離時
間が長く、実施例1の約3倍要した。
Comparative Example 1 Cell Separator The same cell separator as in Example 1 was used. Cell separation operation Preservation of umbilical cord blood using a 4 ° C refrigerator instead of a 22 ° C incubator, and cell separation after leaving at room temperature (24 ° C) for 1 hour instead of promptly performing cell separation Except for the above, the same operation as in Example 1 was performed. Analysis was analyzed in the same manner as in Example 1. Results Table 2 summarizes the results. The recovery rate of nucleated cells and CD34-positive cells was lower than that of Example 1, and the cell separation time was longer, and required about three times that of Example 1.

【0009】[0009]

【実施例2】細胞分離器 実施例1と同様の細胞分離器を用いた。 細胞分離操作 22℃の恒温器の代わりに4℃の冷蔵庫を用いて臍帯血
を保存すること以外は実施例1と同様の操作を行った。 分析 実施例1と同様の分析を行った。 結果 結果のまとめを表3に示す。回収した細胞液中には有核
細胞、CD34陽性細胞が高率に回収できており、細胞
分離時間も短いことが分かる。
Example 2 Cell Separator The same cell separator as in Example 1 was used. Cell Separation Operation The same operation as in Example 1 was performed except that cord blood was stored using a refrigerator at 4 ° C. instead of a thermostat at 22 ° C. Analysis The same analysis as in Example 1 was performed. Results Table 3 summarizes the results. It can be seen that nucleated cells and CD34-positive cells were recovered at a high rate in the recovered cell solution, and that the cell separation time was short.

【0010】[0010]

【比較例2】細胞分離器 実施例1と同様の細胞分離器を用いた。 細胞分離操作 臍帯血を恒温器から出してすみやかに細胞分離を行う代
わりに22℃で保存した臍帯血を4℃の冷蔵庫で1時間
冷蔵した後に細胞分離を行うこと以外は実施例1と同様
の操作を行った。 分析 実施例1と同様の方法で分析した。 結果 結果のまとめを表4に示す。有核細胞、CD34陽性細
胞の回収率は実施例1と比べて低値であり、細胞分離時
間が長く、実施例1の約3倍要した。
Comparative Example 2 Cell Separator The same cell separator as in Example 1 was used. Cell Separation Operation Same as Example 1 except that the cord blood stored at 22 ° C. is refrigerated in a refrigerator at 4 ° C. for 1 hour and then subjected to cell separation instead of taking out the cord blood from the incubator and immediately performing cell separation. The operation was performed. Analysis was analyzed in the same manner as in Example 1. Results Table 4 summarizes the results. The recovery rate of nucleated cells and CD34-positive cells was lower than that of Example 1, and the cell separation time was longer, and required about three times that of Example 1.

【0011】[0011]

【実施例3】細胞分離器 実施例1と同様の細胞分離器を用いた。 細胞分離操作 22℃の恒温器の代わりに15℃の恒温器を使用したこ
と、すみやかに細胞分離を行う代わりに15℃で保存し
た臍帯血を室温(24℃)で1時間放置した後に細胞分
離を行う以外は実施例1と同様の操作を行った。 分析 実施例1と同様の分析を行った。 結果 結果のまとめを表5に示す。回収した細胞液中には有核
細胞、CD34陽性細胞が高率に回収できており、細胞
分離時間も短いことが分かる。
Example 3 Cell Separator The same cell separator as in Example 1 was used. Cell separation operation A 15 ° C incubator was used instead of a 22 ° C incubator, and cord blood stored at 15 ° C was left at room temperature (24 ° C) for 1 hour instead of immediately performing cell separation. The same operation as in Example 1 was performed except that the above operation was performed. Analysis The same analysis as in Example 1 was performed. Results Table 5 summarizes the results. It can be seen that nucleated cells and CD34-positive cells were recovered at a high rate in the recovered cell solution, and that the cell separation time was short.

【0012】[0012]

【実施例4】細胞分離器 実施例1と同様の細胞分離器を用いた。 細胞分離操作 臍帯血を冷蔵庫から出してすみやかに細胞分離を行う代
わりに4℃で保存した臍帯血を15℃の恒温器で1時間
放置した後に細胞分離を行う以外は実施例2と同様の操
作を行った。 分析 実施例1と同様の分析を行った。 結果 結果のまとめを表6に示す。回収した細胞液中には有核
細胞、CD34陽性細胞が高率に回収できており、細胞
分離時間も短いことが分かる。
Example 4 Cell Separator The same cell separator as in Example 1 was used. Cell Separation Operation The same operation as in Example 2 except that the cord blood stored at 4 ° C. is left for 1 hour in a 15 ° C. incubator for 1 hour instead of removing the cord blood from the refrigerator and immediately performing cell separation, and then performing cell separation. Was done. Analysis The same analysis as in Example 1 was performed. Results Table 6 summarizes the results. It can be seen that nucleated cells and CD34-positive cells were recovered at a high rate in the recovered cell solution, and that the cell separation time was short.

【0013】[0013]

【比較例3】細胞分離器 実施例1と同様の細胞分離器を用いた。 細胞分離操作 15℃の恒温器の代わりに20℃の恒温器を用いる以外
は実施例4と同様の操作を行った。 分析 実施例1と同様の方法で分析した。 結果 結果のまとめを表7に示す。有核細胞、CD34陽性細
胞の回収率は実施例4と比べて低値であり、細胞分離時
間も実施例4の約3倍要した。 以上の実施例及び比較例のまとめを表8に示す。
Comparative Example 3 Cell Separator The same cell separator as in Example 1 was used. Cell Separation Operation The same operation as in Example 4 was performed except that a thermostat at 20 ° C. was used instead of a thermostat at 15 ° C. Analysis was analyzed in the same manner as in Example 1. Results Table 7 summarizes the results. The recovery rate of nucleated cells and CD34-positive cells was lower than in Example 4, and the cell separation time was about three times as long as in Example 4. Table 8 summarizes the above Examples and Comparative Examples.

【0014】[0014]

【発明の効果】以上示したように、本発明によれば安価
でかつ簡便・短時間操作で、造血幹細胞等、有核細胞が
高率に回収できる有核細胞分離回収方法を提供すること
ができるので臨床現場での省力化に貢献するところ大で
ある。
As described above, according to the present invention, it is possible to provide a method for separating and recovering nucleated cells, which can recover nucleated cells such as hematopoietic stem cells at a high rate at a low cost, with simple and easy operation. It is a great way to contribute to labor savings in clinical settings.

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

【図1】実施例1で用いた細胞分離回路システムの模式
図である。
FIG. 1 is a schematic diagram of a cell separation circuit system used in Example 1.

【符号の説明】[Explanation of symbols]

1 細胞分離器 2 血液バッグ 3 メッシュチャンバー 4 三方活栓 5 細胞回収用バッグ 6 三方活栓 7 ドレーンバッグ Reference Signs List 1 cell separator 2 blood bag 3 mesh chamber 4 three-way cock 5 cell collection bag 6 three-way cock 7 drain bag

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4B029 AA09 BB11 CC01 HA02 HA06 HA09 4B065 AA93X AA94X BD18 4C087 AA04 AA10 BB34 BB43 BB44 BB58 BB59 CA21 DA02 DA03 DA14 DA17 DA21 ZA51  ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 4B029 AA09 BB11 CC01 HA02 HA06 HA09 4B065 AA93X AA94X BD18 4C087 AA04 AA10 BB34 BB43 BB44 BB58 BB59 CA21 DA02 DA03 DA14 DA17 DA21 ZA51

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 細胞保存温度Aで保存された回収必要細
胞と除去対象細胞を含む細胞含有液を、該回収必要細胞
を実質的に捕捉し該除去対象細胞を実質的に通過させる
細胞捕捉手段に細胞分離温度Bで導入し、除去対象細胞
含有液を該細胞捕捉手段から導出させ、次に該細胞捕捉
手段に液体を導入して該細胞捕捉手段に捕捉されている
該回収必要細胞を該細胞捕捉手段から回収する細胞分離
方法において、細胞保存温度Aと細胞分離温度Bが、0
℃<A<30℃且つ0℃<B<30℃且つ|A−B|<
15℃であることを特徴とする細胞分離回収方法。
1. A cell capturing means for substantially capturing a cell containing a cell containing a cell to be recovered and a cell to be removed stored at a cell storage temperature A, and substantially passing the cell to be removed. At a cell separation temperature B, and a liquid containing the cells to be removed is led out from the cell capturing means. Then, a liquid is introduced into the cell capturing means to collect the cells to be collected which have been captured by the cell capturing means. In the cell separation method of recovering from the cell capturing means, the cell storage temperature A and the cell separation temperature B are 0
<A <30 ° C. and 0 ° C. <B <30 ° C. and | AB | <
A method for separating and collecting cells, wherein the temperature is 15 ° C.
【請求項2】 細胞保存温度Aで保存された回収必要細
胞と除去対象細胞を含む細胞含有液を、該回収必要細胞
を実質的に捕捉し該除去対象細胞を実質的に通過させる
細胞捕捉手段に細胞分離温度Bで導入し、除去対象細胞
含有液を該細胞捕捉手段から導出させ、次に該細胞捕捉
手段に液体を導入して該細胞捕捉手段に捕捉されている
該回収必要細胞を該細胞捕捉手段から回収する細胞分離
方法により得られた実質的に除去対象細胞を含まない細
胞含有液であって、細胞保存温度Aと細胞分離温度B
が、0℃<A<30℃且つ0℃<B<30℃且つ|A−
B|<15℃である回収必要細胞含有液。
2. A cell capturing means for substantially capturing a cell containing a cell containing a cell to be recovered and a cell to be removed stored at a cell storage temperature A, and substantially passing the cell to be removed. At a cell separation temperature B, and a liquid containing the cells to be removed is led out from the cell capturing means. Then, a liquid is introduced into the cell capturing means to collect the cells to be collected which have been captured by the cell capturing means. A cell-containing liquid substantially free of cells to be removed, obtained by the cell separation method recovered from the cell capturing means, comprising a cell storage temperature A and a cell separation temperature B
Is 0 ° C <A <30 ° C and 0 ° C <B <30 ° C and | A−
B | A solution containing cells requiring recovery that is <15 ° C.
JP10327539A 1998-11-04 1998-11-04 Separation and recovery of cell and recovery required cell-containing liquid Pending JP2000139454A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10327539A JP2000139454A (en) 1998-11-04 1998-11-04 Separation and recovery of cell and recovery required cell-containing liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10327539A JP2000139454A (en) 1998-11-04 1998-11-04 Separation and recovery of cell and recovery required cell-containing liquid

Publications (1)

Publication Number Publication Date
JP2000139454A true JP2000139454A (en) 2000-05-23

Family

ID=18200230

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10327539A Pending JP2000139454A (en) 1998-11-04 1998-11-04 Separation and recovery of cell and recovery required cell-containing liquid

Country Status (1)

Country Link
JP (1) JP2000139454A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004058936A1 (en) * 2002-12-25 2004-07-15 National Institute Of Advanced Industrial Science And Technology Cell separation and collection apparatus and separation and collection method
US7939323B2 (en) 2003-06-27 2011-05-10 Universite Laval Method of isolating cells from umbilical cord
CN102242054A (en) * 2011-05-11 2011-11-16 浙江星月生物科技股份有限公司 Totally-enclosed cell and cell factor preparation device and preparation method thereof
JP2013123385A (en) * 2011-12-13 2013-06-24 Kaneka Corp Method for treating bone marrow aspirate

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004058936A1 (en) * 2002-12-25 2004-07-15 National Institute Of Advanced Industrial Science And Technology Cell separation and collection apparatus and separation and collection method
US7939323B2 (en) 2003-06-27 2011-05-10 Universite Laval Method of isolating cells from umbilical cord
CN102242054A (en) * 2011-05-11 2011-11-16 浙江星月生物科技股份有限公司 Totally-enclosed cell and cell factor preparation device and preparation method thereof
JP2013123385A (en) * 2011-12-13 2013-06-24 Kaneka Corp Method for treating bone marrow aspirate

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