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JPS6252620B2 - - Google Patents
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JPS6252620B2 - - Google Patents

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Publication number
JPS6252620B2
JPS6252620B2 JP55040154A JP4015480A JPS6252620B2 JP S6252620 B2 JPS6252620 B2 JP S6252620B2 JP 55040154 A JP55040154 A JP 55040154A JP 4015480 A JP4015480 A JP 4015480A JP S6252620 B2 JPS6252620 B2 JP S6252620B2
Authority
JP
Japan
Prior art keywords
lymphocytes
separation
acidic functional
wet
monocytes
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.)
Expired
Application number
JP55040154A
Other languages
Japanese (ja)
Other versions
JPS56152740A (en
Inventor
Setsutaka Kanejima
Tsutae Akao
Tadaaki Furuta
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 Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry 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 Chemical Industry Co Ltd filed Critical Asahi Chemical Industry Co Ltd
Priority to JP4015480A priority Critical patent/JPS56152740A/en
Publication of JPS56152740A publication Critical patent/JPS56152740A/en
Publication of JPS6252620B2 publication Critical patent/JPS6252620B2/ja
Granted legal-status Critical Current

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  • External Artificial Organs (AREA)
  • Medicines Containing Material From Animals Or Micro-Organisms (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Description

【発明の詳现な説明】[Detailed description of the invention]

本発明は、癜血球浮遊液から顆粒球、単球を粘
着し、リンパ球を分離する分離材に関するもの
で、さらに詳しくは、酞性官胜基を含有する合成
暹脂性ゲル型粒状疎氎性固䜓物質であ぀お、酞性
官胜基濃床が湿䜓ml容積圓たり1.2圓量ミ
リ化孊圓量以䞊で、か぀湿䜓の粒埄が30Ό以䞊
350Ό以䞋よりなる分離材に関するものである。 埓来、癜血球浮遊液から顆粒球、単球を陀去し
おリンパ球を分離する方法ずしおは、䞡现胞間の
密床、倧きさ、圢態の違い、顆粒球、単球の貧食
胜、粘着胜の性状を利甚する方法、およびこれら
を組合せお分離する方法が知られおいる。 䞀方、最近の现胞性免疫孊の目ざたしい発展に
䌎ない、リンパ球を、その亜分画である现胞
胞腺由来リンパ球や现胞骚髄由来リンパ
球の比率にできるだけ圱響を䞎えるこずなく、
しかも定量的に、すなわち高収率で高玔床に、さ
らにリンパ球機胜を損なうこずなく癜血球浮遊液
から分離するこずの必芁性がたすたす増倧しおき
おいる。 しかしながら、埓来の分離方法では、リンパ球
矀ず顆粒球、単球矀ずの間で重なる分画があるた
めに定量性に乏しく、たた现胞障害を起こすこず
が倚い。䟋えば、最も䞀般的に䜿われおいる゜デ
むりムメトリゟ゚むトフむコヌルを䜿぀おの比重
遠心法によ぀おリンパ球を分離する方法にしお
も、顆粒球は陀去できおも、リンパ球ず同じ単栞
现胞である単球は混入しおくる。たた癌患者癜血
球を䜿぀た堎合には、顆粒球も密床が倉わり混入
しおくるこずが倚い。これらの混入しおくる単
球、顆粒球を陀去するために、ダむアむオン゚ナ
カルボニル粒子やラテツクス粒子を貧食させお陀
去する方法を組合せるこずも行なわれおいるが、
リンパ球ぞの现胞障害が避けられず、たたリンパ
球の亜分画である现胞の䞀郚を倱なうこずが倚
い。たた繊維に察する粘着性の違いを利甚しお分
離する方法は、繊維間隔、繊維充填密床によ぀お
性胜が倧きく巊右され、安定した性胜が埗にくい
ばかりでなく、倚くの堎合、玔床の高いリンパ球
を埗ようずすれば、粘着性のある䞀郚の现胞、
さらには䞀郚の现胞亜分画が倱なわれがちであ
る。たた䞀定の粒埄を持぀た倚糖類、䟋えばアガ
ロヌスゲルやデキストランゲルに察する粘着性の
違いを利甚しお分離する方法は、ゲルが匷床、
熱、化孊的安定性に欠け、たた埮生物繁殖が起こ
りやすく、分離性胜の維持が困難であり、さらに
ゲル自䜓䞀郚の现胞を粘着する傟向にある。 以䞊蚘したこずから明らかなように、癜血球浮
遊液を怜䜓に䜿぀お、リンパ球を簡䟿な操䜜によ
り、玔床も回収率も高く、しかも、现胞障害を䞎
えるこずなく分離するこずが、现胞性免疫孊を䞭
心ずする医孊、生物孊の分野で広く期埅されおい
るにもかゝわらず、その達成がなされおいない珟
状である。 本発明者らは、癜血球浮遊液を甚いお、リンパ
球を现胞膜および现胞機胜を損なうこずなく、玔
床も回収率も高く簡䟿に分離するこずを目的にし
お、遞択特異的な现胞分離材に぀いお鋭意研究を
重ねた結果、酞性官胜基濃床が湿䜓ml容積圓た
り1.2圓量以䞊で、か぀湿䜓の粒埄が30Ό以䞊
350Ό以䞋である酞性官胜基を含有する合成暹脂
補ゲル型粒状疎氎性固䜓物質ず癜血球浮遊液ず
を、蛋癜含有液䞭で接觊させるこずにより、該物
質以䞋、本発明の分離材ず略すがリンパ球を
吞着しないこずを芋い出し、本発明を完成するに
至぀た。 すなわち、本発明の分離材ず癜血球浮遊液ずを
蛋癜含有液䞭で接觊させるこずにより、现胞膜の
陰性荷電がリンパ球の方が顆粒球、単球よりも倧
きいこず、および现胞の粘着性が顆粒球、単球の
方がリンパ球よりも匷いこずの盞加効果が充分に
発揮できるため、本発明の分離材にリンパ球が粘
着せずに、顆粒球、単球のみが粘着するこずにな
り、分離可胜ずなる。 したが぀お、液の出入口ず぀以䞊のフむルタ
ヌを有するカラムを䜜補し、dl以䞊の蛋癜
を含む液に浞挬した本発明の分離材を充填し、血
液たたは血液から分離した癜血球をdl以䞊
の蛋癜を含む液に浮遊させた液を前蚘カラムに泚
入し、掗浄液により掗い出す操䜜を行なえば、遞
択的にリンパ球だけが浮遊した液を埗るこずがで
きる。 本発明においお、酞性官胜基を含有する粒状疎
氎性固䜓物質ずは、粒状の疎氎性固䜓物質に酞性
官胜基、すなわち匷酞性官胜基たたは匱酞性官胜
基が存圚しおいるものずしお定矩できる。匷酞性
官胜基ずは、䟋えば、スルホン基であり、匱酞性
官胜基ずは、䟋えば、カルボキシル基、ホスホン
基、プノヌル基などである。 具䜓的には、䞊蚘各酞性官胜基を盎接結合した
スチレンずゞビニルベンれンの共重合䜓、䟋ずし
おは、スチレンに〜12のゞビニルベンれンを
加え、その混合物に重合の觊媒ずしお少量の過酞
化ベンゟむルず氎を加え、ベントナむトやアルギ
ン酞などの懞濁剀を加えお懞濁重合を行ない、䜜
成した重合䜓を濃硫酞たたはクロルスルホン酞で
凊理しお埗られたものなどである。たた、プノ
ヌルスルホン酞ずホルムアルデヒドずプノヌル
ずの瞮合䜓、ビニルスルホン酞の重合䜓、アクリ
ル酞重合䜓、メタクリル酞重合䜓、むタコン酞重
合䜓、マレむン酞重合䜓、フマル酞重合䜓、ブタ
ゞ゚ン−−カルボン酞重合䜓、むミノゞ酢酞型
スチレン重合䜓、・・−レゟルシン酞ずホ
ルムアルデヒドずの瞮合䜓、ゞアリルホスホン酞
重合䜓、プノヌルずホルムアルデヒドずの瞮合
䜓などがある。 本発明における酞性官胜基の濃床ずしおは、湿
䜓ml容積圓たり1.2圓量以䞊であるこずが性
胜を発揮するのに適しおおり、1.2圓量未満の
堎合は、分離材ぞのリンパ球吞着率が増加する傟
向にある。酞性官胜基の濃床の䞊限は特に制限は
ないが、過倧の酞性官胜基濃床を有するものは、
匷床劣化をきたし甚いられない。酞性官胜基は
型䟋えば−SO3Hあるいは塩圢〔䟋えば−
SO3Na、−SO3K、−SO32Ca、−SO32Mgな
ど〕いずれでも䜿甚できるが、塩圢の方が浮遊液
のPH調敎が容易であるために䜿甚䞊奜たしい。 本発明における粒埄ずしおは、実際に䜿甚する
湿最状態で、すなわち湿䜓で、350Ό以䞋、極め
お望たしくは200Ό以䞋であるこずが性胜を発揮
するのに適しおおり、350Όよりも倧きい堎合
は、分離材ぞの顆粒球、単球の吞着率が枛少する
傟向にある。湿䜓粒埄ずしおは、正芏分垃をなし
おいるずみなせる粒床分垃においお、分離材の90
以䞊のものを含む有効埄ずしお30Ό以䞊350ÎŒ
以䞋の粒埄範囲、望たしくは70Ό以䞊200Ό以䞋
の粒埄範囲にあるものが䜿甚でき、有効埄がこの
範囲にあるものを適圓に混ぜ合わせお䜿甚しおも
よい。 本発明に甚いるリンパ球を分離するための分離
噚の䟋を図面により説明するず、现胞浮遊液お
よび掗浄液を泚入する入口ず、现胞浮遊液およ
び掗浄液を流出させる出口ずを持぀たカラム
に、出口の所に分離材が流出しない皋床の孔埄を
持぀たフむルタヌを取り付け、カラム内に前
蚘した分離材が充填されおいる。 分離噚を甚いお、癜血球からリンパ球を分離す
るには、血液たたは血液から遠心法、比重遠心法
などの方法により分離した癜血球を蛋癜含有液に
浮遊させた液を、あらかじめ蛋癜含有液で掗浄し
た分離噚に泚入し、浮遊液が本発明の分離材に浞
透し終぀た時点で、掗浄液を流しお未吞収着现胞
を掗い出すこずにより行なう。以䞊の方法により
掗い出した掗浄液䞭には、リンパ球が含たれるこ
ずになる。 本発明の分離材ず癜血球ずを接觊させる際に䜿
甚する蛋癜含有液ずしおは、dl以䞊の蛋癜
を含む液、望たしくは自己血枅たたは動物血枅、
䟋えば牛胎児血枅や子牛血枅を30以䞊含む培逊
液たたは緩衝液、さらに望たしくは100血枅が
甚いられる。dl未満の蛋癜を含む液を甚い
た堎合、䟋えば血枅10を含む緩衝液を甚いた堎
合は、分離材ぞのリンパ球吞着率が増加する傟向
にある。たた分離材を、dl以䞊の蛋癜を含
む液であらかじめコヌテむング凊理を行な぀おお
けば、分離操䜜の際、あらかじめ分離噚を蛋癜含
有液で掗浄する必芁がなく、分離操䜜が簡単にな
り䟿利である。 分離操䜜の際の枩床は、现胞障害を䞎えない枩
床であればいずれでもよいが、宀枩18〜25℃
から䜓枩37℃近蟺ぐらいの枩床が奜たしい。 このようにしお埗られたリンパ球に぀いお、幌
若化胜、抗䜓産生調節䜜甚、现胞障害胜、抗䜓産
生胜などの免疫孊的機胜怜査を行な぀た結果、分
離噚に泚入する前のリンパ球の機胜ず倉わらない
皋床に機胜を保持しおいた。 さらに、リンパ球を溶出させた埌、分離噚に
dl以䞊の分離に際しお甚いたず同様の蛋癜を
含む液を加えながら、おだやかに分離材を撹拌す
るこずにより、䞀たん吞着した癜血球を溶離さ
せ、回収するこずができる。このようにしお埗ら
れた癜血球は、バむアビリテむヌにすぐれ、免疫
孊的機胜怜査においおも機胜の䜎䞋は特に認めら
れないものである。 以䞊、酞性官胜基を含有する粒状疎氎性固䜓物
質であ぀お、酞性官胜基濃床が湿䜓ml容積圓た
り1.2圓量以䞊で、か぀湿䜓の粒埄が30Ό以䞊
350Ό以䞋であるこずを特城ずする、癜血球浮遊
液から顆粒球、単球を吞着し、リンパ球を分離す
る分離材、および該分離材ず癜血球浮遊液ずを
dl以䞊の蛋癜を含む液䞭で接觊させるこずに
より癜血球浮遊液からリンパ球を分離する本発明
は、埓来のリンパ球分離甚詊料およびそれらの方
法ず比べお、䞋蚘の効果がある。 (1) 癜血球からリンパ球を分離するたでの操䜜が
簡単で、しかも䞀段階で枈む。すなわち、癜血
球浮遊液を本発明の分離材を充填した容噚に泚
入し、掗浄液を流すだけの操䜜で枈む。 (2) 分離する際に、癜血球の酵玠凊理や薬剀凊理
などをする必芁がなく、たた分離埌も元のリン
パ球性状ず異なるこずもないので、リンパ球の
機胜倉化、䜎䞋が起こらない。したが぀お、リ
ンパ球に぀いおの免疫孊的機胜怜査にも䜿え
る。 (3) 分離噚の䜜補が埓来のリンパ球分離甚詊料お
よび分離機噚の䜜補に比べお容易で、しかも安
䟡である。 (4) 分離材は高分子合成物質であるので、䞀定の
掻性を持぀分離材の䜜補および掻性の維持が容
易にでき、しかも滅菌操䜜が簡単にできる。さ
らに物理的、化孊的、生物的安定性にすぐれ、
経時的劣化もない。 次に実斜䟋によ぀お本発明をさらに詳现に説明
する。 実斜䟋  分離噚の䜜補ゲル型粒状スルホン化ポリスチレ
ン−ゞビニルベンれン暹脂のNaむオン型酞
性官胜基濃床湿䜓ml容積圓たり1.5圓
量、湿䜓の粒埄有効埄100〜350Όmlを燐
酞緩衝液に充分に浞し、掗浄埌、この暹脂を、
底面に50Όメツシナのナむロンネツトのフむ
ルタヌを匕いた液入口ず出口ずを持぀た内埄10
mmのアクリル補プラスチツクのカラム図面参
照に、気泡が入らないように泚意しながら充
填するこずにより䜜補した。 分離操䜜ヘパリン加ヒト末梢血から゜デむりム
メトリゟ゚むト−フむコヌル混液
1.077、20℃を䜿぀お、比重遠心法により分
離し、燐酞緩衝液で掗浄した癜血球分画を×
106mlの濃床に、100牛胎児血枅蛋癜含有
量4.5dlに浮遊させた液0.5mlを、前も぀
お100牛胎児血枅mlで掗浄した分離噚の入
口より静かに流し蟌み、浮遊液が充分に分離材
に浞透し終぀た時点で、たゞちに掗浄液ずしお
牛胎児血枅mlをカラム入口から流し蟌み、自
然萜䞋の流速で、分離材に吞着しおいない现胞
を掗い出しお回収した。 分析結果党现胞回収率は、自動血球蚈数噚たた
は血球蚈算盀を䜿぀おの顕埮鏡芳察により求め
た。たた怜䜓および回収液䞭のリンパ球は、亜
分画である现胞をノむラミニダヌれ凊理矊赀
血球ずのロれツト反応により、现胞を衚面免
疫グロブリンに察する螢光抗䜓法により分析
し、现胞ず现胞ずの和によ぀お算出した。
䞀方、怜䜓および回収液䞭の顆粒球、単球矀
は、ペルオキシダヌれ染色法により分析した。
さらに党现胞回収率ず怜䜓および回収液䞭の各
組成割合ずを䜿぀お、各組成の回収率を算出し
た。結果は、现胞、现胞に぀いおのデヌタ
も含めお衚に瀺す。 実斜䟋 〜 実斜䟋ず同様な方法により、ゲル型粒状スル
ホン化ポリスチレン−ゞビニルベンれン暹脂の
Naむオン型酞性官胜基濃床湿䜓ml容積圓
たり2.0圓量、湿䜓の粒埄有効埄70〜300Ό
−実斜䟋−、ゲル型粒状メタクリル酞−ゞビニ
ルベンれン暹脂のNaむオン型酞性官胜基濃
床湿䜓ml容積圓たり2.5圓量、湿䜓の粒
埄有効埄100〜350Ό−実斜䟋−、ゲル型粒
状アクリル酞−ゞビニルベンれン暹脂のNaむオ
ン型酞性官胜基濃床湿䜓ml容積圓たり3.5
圓量、湿䜓の粒埄有効埄70〜350Ό−実斜䟋
−、ゲル型粒状カルボキシル化ポリスチレン−
ゞビニルベンれン暹脂のNaむオン型酞性官胜
基濃床湿䜓ml容積圓たり4.1圓量、湿䜓の
粒埄有効埄70〜350Ό−実斜䟋−をそれぞれ
分離材に甚いお実隓した結果を衚にたずめお瀺
す。
The present invention relates to a separation material that adheres to granulocytes and monocytes and separates lymphocytes from a leukocyte suspension. More specifically, the present invention relates to a separation material that is a synthetic resin gel-type granular hydrophobic solid material containing an acidic functional group. The concentration of acidic functional groups is 1.2 m equivalent (millichemical equivalent) per 1 ml volume of the wet material, and the particle size of the wet material is 30 Ό or more.
This relates to a separation material made of 350Ό or less. Conventionally, methods for removing granulocytes and monocytes from leukocyte suspensions and isolating lymphocytes are based on the differences in density, size, and morphology between the two cells, as well as the phagocytosis and adhesive ability of granulocytes and monocytes. Methods that utilize properties and methods that combine and separate these are known. On the other hand, with recent remarkable developments in cellular immunology, it is important to influence as much as possible the ratio of lymphocytes to their sub-fractions, T cells (thymus-derived lymphocytes) and B cells (bone marrow-derived lymphocytes). Without,
Moreover, there is an increasing need to quantitatively separate leukocytes from leukocyte suspensions, ie, with high yield and high purity, and without impairing lymphocyte function. However, in conventional separation methods, there are overlapping fractions between lymphocytes, granulocytes, and monocytes, resulting in poor quantitative performance and often causing cell damage. For example, even if lymphocytes are separated by specific gravity centrifugation using sodium metrizoate ficoll, which is the most commonly used method, although granulocytes can be removed, the same molecule as lymphocytes may be removed. Monocytes, which are nuclear cells, are mixed in. Furthermore, when leukocytes from cancer patients are used, granulocytes often change in density and become contaminated. In order to remove these contaminating monocytes and granulocytes, a combination of methods has been used to remove them by feeding them with Diaionenacarbonyl particles and latex particles.
Cell damage to lymphocytes is unavoidable, and some B cells, a sub-fraction of lymphocytes, are often lost. Furthermore, the performance of separation methods that utilize differences in adhesion to fibers is greatly affected by fiber spacing and fiber packing density, and not only is it difficult to obtain stable performance, but in many cases it is difficult to obtain highly pure lymphocytes. If you try to get some sticky B cells,
Furthermore, some T cell subfractions tend to be lost. In addition, methods for separating polysaccharides with a certain particle size, such as agarose gel or dextran gel, using differences in their adhesion to gels,
It lacks thermal and chemical stability, is prone to microbial growth, has difficulty maintaining separation performance, and furthermore, the gel itself tends to stick to some B cells. As is clear from the above, it is possible to isolate lymphocytes using a leukocyte suspension as a specimen with simple manipulations, with high purity and recovery rate, and without causing cell damage. Although it is widely expected in the fields of medicine and biology, with a focus on science, the current situation is that it has not been achieved. The present inventors have made extensive efforts to develop selection-specific cell separation materials with the aim of easily separating lymphocytes with high purity and recovery rate without damaging cell membranes and cell functions using a leukocyte suspension. As a result of repeated research, we found that the concentration of acidic functional groups is 1.2 m equivalent or more per 1 ml volume of wet material, and the particle size of wet material is 30 Ό or more.
By contacting a gel-type particulate hydrophobic solid substance made of a synthetic resin containing an acidic functional group with a size of 350Ό or less and a white blood cell suspension in a protein-containing liquid, the substance (hereinafter abbreviated as the separation material of the present invention) is produced. The present invention was completed based on the discovery that the present invention does not adsorb lymphocytes. That is, by contacting the separation material of the present invention with a leukocyte suspension in a protein-containing solution, it was found that the negative charge on the cell membrane of lymphocytes is greater than that of granulocytes and monocytes, and that the adhesiveness of the cells is reduced to granulocytes. Since the additive effect of globules and monocytes being stronger than lymphocytes can be fully exerted, lymphocytes do not adhere to the separation material of the present invention, and only granulocytes and monocytes adhere. , becomes separable. Therefore, a column having a liquid inlet/outlet and one or more filters is prepared, filled with the separation material of the present invention immersed in a liquid containing 1 g/dl or more of protein, and 1 g of blood or leukocytes separated from blood is prepared. By injecting a suspension of protein into the column and washing it out with a washing solution, a solution in which only lymphocytes are selectively suspended can be obtained. In the present invention, a particulate hydrophobic solid material containing an acidic functional group can be defined as a particulate hydrophobic solid material in which an acidic functional group, that is, a strongly acidic functional group or a weakly acidic functional group, is present. The strong acidic functional group is, for example, a sulfone group, and the weakly acidic functional group is, for example, a carboxyl group, a phosphonic group, a phenol group, etc. Specifically, a copolymer of styrene and divinylbenzene with each of the above acidic functional groups directly bonded, for example, 4 to 12% divinylbenzene is added to styrene, and a small amount of peroxide is added to the mixture as a polymerization catalyst. It is obtained by adding benzoyl and water, adding a suspending agent such as bentonite or alginic acid to carry out suspension polymerization, and treating the resulting polymer with concentrated sulfuric acid or chlorosulfonic acid. In addition, condensates of phenolsulfonic acid, formaldehyde, and phenol, vinylsulfonic acid polymers, acrylic acid polymers, methacrylic acid polymers, itaconic acid polymers, maleic acid polymers, fumaric acid polymers, butadiene-1- Examples include carboxylic acid polymers, iminodiacetic acid type styrene polymers, condensates of 1,3,5-resorcinic acid and formaldehyde, diallylphosphonic acid polymers, and condensates of phenol and formaldehyde. The concentration of acidic functional groups in the present invention is suitable for exhibiting performance if it is 1.2 m equivalent or more per 1 ml of wet volume, and if it is less than 1.2 m equivalent, the lymphocyte adsorption rate to the separation material will decrease. is on the rise. There is no particular upper limit to the concentration of acidic functional groups, but those with an excessive concentration of acidic functional groups are
Cannot be used due to strength deterioration. The acidic functional group is H
form (e.g. -SO 3 H) or salt form [e.g. -
[SO 3 Na, −SO 3 K, (−SO 3 ) 2 Ca, (−SO 3 ) 2 Mg, etc.] can be used, but the salt form is preferred because it is easier to adjust the pH of the suspended liquid. preferable. The particle size in the present invention is suitably 350ÎŒ or less, preferably 200ÎŒ or less, in order to exhibit its performance in the wet state of actual use, that is, in a wet state, and if it is larger than 350ÎŒ, The adsorption rate of granulocytes and monocytes to the separation material tends to decrease. In terms of wet particle size, in a particle size distribution that can be considered to be a normal distribution, the separation material has a particle size of 90%.
30Ό or more 350Ό as effective diameter including % or more
Particles within the following particle size range, preferably from 70Ό to 200Ό, can be used, and particles having an effective diameter within this range may be appropriately mixed and used. An example of a separator for separating lymphocytes used in the present invention will be described with reference to a drawing. A column 3 has an inlet 1 for injecting a cell suspension and a washing solution, and an outlet 2 for draining the cell suspension and washing solution.
At the outlet, a filter 4 having a pore size large enough to prevent the separation material from flowing out is attached, and the column 3 is filled with the separation material 5 described above. To separate lymphocytes from white blood cells using a separator, white blood cells separated from blood or blood by a method such as centrifugation or specific gravity centrifugation are suspended in a protein-containing solution and then washed with a protein-containing solution in advance. When the suspension liquid has permeated into the separation material of the present invention, a washing liquid is poured to wash out unabsorbed cells. The washing liquid washed out by the above method contains lymphocytes. The protein-containing liquid used when bringing the separation material of the present invention into contact with leukocytes includes a liquid containing 1 g/dl or more of protein, preferably autologous serum or animal serum.
For example, a culture solution or buffer containing 30% or more fetal bovine serum or calf serum, more preferably 100% serum, is used. When a solution containing less than 1 g/dl of protein is used, for example when a buffer solution containing 10% serum is used, the rate of adsorption of lymphocytes to the separation material tends to increase. In addition, if the separation material is coated in advance with a solution containing 1 g/dl or more of protein, there is no need to wash the separator with a protein-containing solution beforehand, making the separation process easier. It's convenient. The temperature during the separation operation may be any temperature as long as it does not cause cell damage, but room temperature (18-25℃) is acceptable.
The preferred temperature is from to body temperature (around 37 degrees Celsius). The lymphocytes obtained in this way were subjected to immunological function tests such as blastogenesis ability, antibody production regulation effect, cytotoxicity ability, and antibody production ability. The function was maintained to the same extent as the function of . Furthermore, after eluating the lymphocytes, 1
By gently stirring the separation material while adding a solution containing the same protein used in the separation of g/dl or more, the once adsorbed leukocytes can be eluted and recovered. The leukocytes thus obtained have excellent viability, and no particular decrease in function is observed in immunological function tests. The above is a particulate hydrophobic solid substance containing an acidic functional group, in which the concentration of the acidic functional group is 1.2 m equivalent or more per 1 ml volume of the wet material, and the particle size of the wet material is 30 Ό or more.
A separation material for adsorbing granulocytes and monocytes from a leukocyte suspension and separating lymphocytes, which is characterized by a particle size of 350 Ό or less, and a separation material for separating lymphocytes from a leukocyte suspension;
The present invention, which separates lymphocytes from a leukocyte suspension by contacting them in a solution containing protein of g/dl or higher, has the following effects compared to conventional lymphocyte separation samples and methods thereof. (1) The procedure for separating lymphocytes from white blood cells is simple and can be completed in one step. That is, all that is required is to inject the leukocyte suspension into a container filled with the separation material of the present invention and to drain the washing liquid. (2) There is no need for enzymatic or drug treatment of leukocytes during separation, and the properties of the lymphocytes do not differ from the original lymphocytes even after separation, so no functional changes or declines in lymphocytes occur. Therefore, it can also be used for immunological function tests on lymphocytes. (3) The production of the separator is easier and cheaper than the production of conventional lymphocyte separation samples and separation equipment. (4) Since the separating material is a polymeric synthetic material, it is easy to produce a separating material with a certain level of activity and maintain the activity, and the sterilization process can be easily performed. Furthermore, it has excellent physical, chemical, and biological stability,
There is no deterioration over time. Next, the present invention will be explained in more detail with reference to Examples. Example 1 Preparation of separator: 2 ml of gel-type granular sulfonated polystyrene-divinylbenzene resin of Na ion type (acidic functional group concentration: 1.5 m equivalent per 1 ml volume of wet material, particle size of wet material: effective diameter 100 to 350 Ό) After thoroughly immersing the resin in phosphate buffer and washing, the resin is
Inner diameter 10 with a liquid inlet and outlet with a 50 ÎŒm mesh nylon net filter on the bottom.
It was prepared by filling a 2 mm acrylic plastic column (see drawing), taking care not to introduce air bubbles. Separation procedure: Sodium metrizoate-ficoll mixture (d=
1.077, 20°C), the leukocyte fraction was separated by specific gravity centrifugation and washed with phosphate buffer.
Gently add 0.5 ml of a solution suspended in 100% fetal bovine serum (protein content: 4.5 g/dl) to a concentration of 10 6 /ml from the inlet of a separator that was previously washed with 4 ml of 100% fetal bovine serum. When the floating liquid has sufficiently permeated the separation material, immediately pour 4 ml of fetal bovine serum from the inlet of the column as a washing solution to wash out cells that are not adsorbed to the separation material at a flow rate of gravity. Recovered. Analysis results: Total cell recovery rate was determined by microscopic observation using an automatic hemocytometer or hemocytometer. In addition, the lymphocytes in the specimen and collected solution were analyzed by analyzing the sub-fractions T cells by rosette reaction with neuraminidase-treated sheep red blood cells, and B cells by fluorescent antibody method against surface immunoglobulin. Calculated by the sum of
On the other hand, granulocytes and monocytes in the specimen and recovered solution were analyzed by peroxidase staining.
Furthermore, the recovery rate of each composition was calculated using the total cell recovery rate and the proportion of each composition in the specimen and recovery solution. The results are shown in Table 1, including data on T cells and B cells. Examples 2 to 5 By the same method as in Example 1, gel-type granular sulfonated polystyrene-divinylbenzene resin was prepared.
Na ion type (acidic functional group concentration: 2.0 m equivalent per 1 ml wet volume, wet particle size: effective diameter 70 to 300Ό)
-Example 2-, Na ion type of gel-type granular methacrylic acid-divinylbenzene resin (acidic functional group concentration: 2.5 m equivalent per 1 ml volume of wet body, particle size of wet body: effective diameter 100 to 350Ό) - Example 3 -, Na ion type of gel type granular acrylic acid-divinylbenzene resin (acidic functional group concentration: 3.5 per ml wet volume)
m equivalent, wet particle size; effective diameter 70 to 350Ό) - Example 4 - Gel type granular carboxylated polystyrene -
The results of experiments using Na ion type divinylbenzene resin (acidic functional group concentration: 4.1 m equivalent per 1 ml wet volume, wet particle size: effective diameter 70 to 350Ό) - Example 5) are shown below. They are summarized in Table 1.

【衚】 比范䟋 、 実斜䟋ず同じ濃床および組成の癜血球浮遊液
を䜿぀お、ゲル型粒状スルホン化ポリスチレン−
ゞビニルベンれン暹脂のNaむオン型酞性官胜
基濃床湿䜓ml容積圓たり1.0圓量、湿䜓の
粒埄有効埄70〜350Ό−比范䟋−、ゲル型粒
状スルホン化ポリスチレン−ゞビニルベンれン暹
脂のNaむオン型酞性官胜基濃床湿䜓ml容
積圓たり2.0圓量、湿䜓の粒埄有効埄380〜
550Ό−比范䟋−をそれぞれ分離材に甚いお、
実斜䟋ず同様の分離操䜜を実斜した。分析結果
は衚にたずめお衚す。 比范䟋  培地を100牛胎児血枅の代わりに10牛胎児
血枅−燐酞緩衝液蛋癜含有量0.44dlを甚
いた以倖は、実斜䟋ず同じ濃床および組成の癜
血球浮遊液を䜿぀お、実斜䟋ず同様の方法によ
り実斜した。分析結果は衚に瀺す。
[Table] Comparative Examples 1 and 2 Using a leukocyte suspension with the same concentration and composition as in Example 2, gel-type granular sulfonated polystyrene
Na ion type of divinylbenzene resin (acidic functional group concentration: 1.0 m equivalent per 1 ml wet volume, wet particle size: effective diameter 70 to 350Ό) - Comparative Example 1 - Gel type granular sulfonated polystyrene - divinylbenzene resin Na ion type (acidic functional group concentration: 2.0 m equivalent per 1 ml wet volume, wet particle size: effective diameter 380 ~
550Ό) - Comparative Example 2 - were used as separation materials, respectively.
The same separation operation as in Example 1 was carried out. The analysis results are summarized in Table 2. Comparative Example 3 A leukocyte suspension with the same concentration and composition as in Example 2 was used, except that 10% fetal bovine serum-phosphate buffer (protein content 0.44 g/dl) was used instead of 100% fetal bovine serum. The experiment was carried out in the same manner as in Example 1. The analysis results are shown in Table 2.

【衚】 実斜䟋  ゲル型粒状スルホン化ポリスチレン−ゞビニル
ベンれン暹脂のNaむオン型酞性官胜基濃床
湿䜓ml容積圓たり1.8圓量、湿䜓の粒埄有
効埄70〜200Όを分離材ずしお䜿甚し、ヘパリ
ン加ヒト末梢血から遠心法によりバツフむヌコヌ
トを分離し、燐酞緩衝液で充分に掗浄した癜血球
分画を×107mlの濃床に100牛胎児血枅に浮
遊させた液、0.5mlを怜䜓液ずしお䜿甚し、実斜
䟋ず同様の方法により実斜した。 分析の結果、怜䜓液䞭の組成割合は、リンパ球
38.535.2、3.3、顆粒・単球
61.3であ぀たのに察しお、回収液䞭の組成割
合は、リンパ球79.172.4、6.7
、顆粒・単球19.1であり、回収率は、党
现胞45.5、リンパ球93.593.6、
92.4、顆粒・単球14.2であ぀た。 実斜䟋  実斜䟋ず同じ分離材を䜿甚しお、癜血球を
7.86×106mlの濃床で含むヘパリン加ヒト末梢
血0.5mlをそのたた怜䜓液ずしお䜿぀お、実斜䟋
ず同様の方法により実斜した。 分析の結果、怜䜓液䞭の組成割合は、リンパ球
37.127.5、9.6、顆粒・単球
62.0であ぀たのに察しお、回収液䞭の組成割
合は、リンパ球85.264.8、20.4
、顆粒・単球12.6であり、回収率は、党
现胞36.3、リンパ球83.485.5、
77.1、顆粒・単球7.4であ぀た。な
お、回収液䞭には、血球ずしお赀血球、血小板も
含たれおいるため、これらを陀去したい堎合は、
さらに溶血操䜜や遠心操䜜が必芁である。 実斜䟋  実斜䟋ず同様にしお分離噚を䜜成し、同様の
分離操䜜にお、吞着しおいない现胞を掗い出した
埌、10牛胎児血枅含有リン酞緩衝液mlをカラ
ム入口から流し蟌み、自然萜䞋の流速で流䞋させ
ながら、パスツヌルピペツトにおピペツテむング
を行なうこずにより、おだやかに分離材をかきた
ぜ、分離した癜血球を溶出させる。 埗られた癜血球は、実斜䟋ず同様にしお分析
した結果、組成割合はリンパ球23.6、リン
パ球10.7、顆粒、単球64.3であ぀た。
[Table] Example 6 Na ion type of gel type granular sulfonated polystyrene-divinylbenzene resin (acidic functional group concentration;
Using 1.8 m equivalent per 1 ml volume of wet fluid (particle size of wet fluid; effective diameter: 70 to 200 ÎŒ) as a separation material, the buffer coat was separated from heparinized human peripheral blood by centrifugation, and then thoroughly separated with phosphate buffer. The procedure was carried out in the same manner as in Example 1, using 0.5 ml of the washed leukocyte fraction suspended in 100% fetal bovine serum at a concentration of 1×10 7 /ml as the sample solution. As a result of the analysis, the composition ratio in the sample fluid was lymphocytes = 38.5% (T = 35.2%, B = 3.3%) and granules/monocytes = 61.3%, whereas the composition ratio in the collected fluid was Lymphocytes = 79.1% (T = 72.4%, B = 6.7
%), granules/monocytes = 19.1%, and the recovery rate was total cells = 45.5%, lymphocytes = 93.5% (T = 93.6%,
B = 92.4%), and granules/monocytes = 14.2%. Example 7 Using the same separation material as in Example 6, leukocytes were isolated.
The experiment was carried out in the same manner as in Example 1, using 0.5 ml of heparinized human peripheral blood containing a concentration of 7.86×10 6 /ml as the sample fluid. As a result of the analysis, the composition ratio in the sample fluid was lymphocytes = 37.1% (T = 27.5%, B = 9.6%) and granules/monocytes = 62.0%, whereas the composition ratio in the collected fluid was Lymphocytes = 85.2% (T = 64.8%, B = 20.4
%), granules/monocytes = 12.6%, and the recovery rate was total cells = 36.3%, lymphocytes = 83.4% (T = 85.5%,
B = 77.1%), and granules/monocytes = 7.4%. The recovered solution also contains red blood cells and platelets, so if you want to remove them,
Furthermore, hemolysis and centrifugation operations are required. Example 8 A separator was created in the same manner as in Example 1, and after washing out unadsorbed cells using the same separation procedure, 8 ml of phosphate buffer containing 10% fetal bovine serum was poured into the column from the inlet. The separation material is gently stirred by pipetting with a Pasteur pipette while flowing down at the flow rate of gravity, and the separated white blood cells are eluted. The obtained leukocytes were analyzed in the same manner as in Example 1, and the composition ratio was 23.6% T lymphocytes, 10.7% B lymphocytes, and 64.3% granules and monocytes.

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

図面は分離噚の䟋を瀺す断面図である。   液の入口、  液の出口、  カラ
ム、  フむルタヌ、  分離材。
The drawing is a sectional view showing one example of a separator. 1...Liquid inlet, 2...Liquid outlet, 3...Column, 4...Filter, 5...Separation material.

Claims (1)

【特蚱請求の範囲】[Claims]  酞性官胜基を含有する合成暹脂補ゲル型粒状
疎氎性固䜓物質であ぀お、酞性官胜基濃床が湿䜓
ml容積圓たり1.2圓量以䞊であ぀お、か぀湿
䜓の粒埄が30Ό以䞊350Ό以䞋であるこずを特城
ずする、癜血球浮遊液から顆粒球、単球を粘着
し、リンパ球を分離する分離材。
1 Gel-type granular hydrophobic solid material made of synthetic resin containing acidic functional groups, in which the acidic functional group concentration is 1.2 m equivalent or more per 1 ml of wet material, and the particle size of the wet material is 30 Ό or more and 350 Ό or less A separation material that adheres to granulocytes and monocytes and separates lymphocytes from a leukocyte suspension.
JP4015480A 1980-03-31 1980-03-31 Lymph cell separating agent, separator and separating method Granted JPS56152740A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4015480A JPS56152740A (en) 1980-03-31 1980-03-31 Lymph cell separating agent, separator and separating method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4015480A JPS56152740A (en) 1980-03-31 1980-03-31 Lymph cell separating agent, separator and separating method

Publications (2)

Publication Number Publication Date
JPS56152740A JPS56152740A (en) 1981-11-26
JPS6252620B2 true JPS6252620B2 (en) 1987-11-06

Family

ID=12572841

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4015480A Granted JPS56152740A (en) 1980-03-31 1980-03-31 Lymph cell separating agent, separator and separating method

Country Status (1)

Country Link
JP (1) JPS56152740A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0975725A (en) 1995-09-20 1997-03-25 Kanegafuchi Chem Ind Co Ltd Bradykinin adsorbent, adsorption removal method and adsorber

Also Published As

Publication number Publication date
JPS56152740A (en) 1981-11-26

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