JPH0534337A - Filter for separating leucocyte - Google Patents
Filter for separating leucocyteInfo
- Publication number
- JPH0534337A JPH0534337A JP3187900A JP18790091A JPH0534337A JP H0534337 A JPH0534337 A JP H0534337A JP 3187900 A JP3187900 A JP 3187900A JP 18790091 A JP18790091 A JP 18790091A JP H0534337 A JPH0534337 A JP H0534337A
- Authority
- JP
- Japan
- Prior art keywords
- porous body
- filter
- blood
- leucocytes
- leukocyte
- 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
Links
- 238000000926 separation method Methods 0.000 claims abstract description 37
- 239000011148 porous material Substances 0.000 claims abstract description 36
- 229920002554 vinyl polymer Polymers 0.000 claims abstract description 8
- 229920005749 polyurethane resin Polymers 0.000 claims abstract description 7
- 210000000265 leukocyte Anatomy 0.000 claims description 65
- 210000004369 blood Anatomy 0.000 abstract description 33
- 239000008280 blood Substances 0.000 abstract description 33
- 239000000463 material Substances 0.000 abstract description 12
- 239000002504 physiological saline solution Substances 0.000 abstract description 10
- 230000037452 priming Effects 0.000 abstract description 3
- 239000000126 substance Substances 0.000 abstract description 2
- 239000000470 constituent Substances 0.000 abstract 1
- 238000010276 construction Methods 0.000 abstract 1
- 230000014759 maintenance of location Effects 0.000 abstract 1
- 230000000717 retained effect Effects 0.000 abstract 1
- 210000000601 blood cell Anatomy 0.000 description 11
- 239000000306 component Substances 0.000 description 9
- 239000012503 blood component Substances 0.000 description 8
- 210000001772 blood platelet Anatomy 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 238000011084 recovery Methods 0.000 description 6
- 239000000835 fiber Substances 0.000 description 5
- 239000000725 suspension Substances 0.000 description 5
- 210000003743 erythrocyte Anatomy 0.000 description 4
- 239000011780 sodium chloride Substances 0.000 description 4
- 235000002639 sodium chloride Nutrition 0.000 description 4
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 239000011159 matrix material Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- FVAUCKIRQBBSSJ-UHFFFAOYSA-M sodium iodide Chemical compound [Na+].[I-] FVAUCKIRQBBSSJ-UHFFFAOYSA-M 0.000 description 3
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- 238000004820 blood count Methods 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229920002635 polyurethane Polymers 0.000 description 2
- 239000004814 polyurethane Substances 0.000 description 2
- 229920003002 synthetic resin Polymers 0.000 description 2
- 239000000057 synthetic resin Substances 0.000 description 2
- 229920000856 Amylose Polymers 0.000 description 1
- 229920001353 Dextrin Polymers 0.000 description 1
- 239000004375 Dextrin Substances 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 238000006359 acetalization reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003377 acid catalyst Substances 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 1
- 235000011130 ammonium sulphate Nutrition 0.000 description 1
- 239000003945 anionic surfactant Substances 0.000 description 1
- 239000010836 blood and blood product Substances 0.000 description 1
- 230000017531 blood circulation Effects 0.000 description 1
- 229940125691 blood product Drugs 0.000 description 1
- 230000005465 channeling Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 235000019425 dextrin Nutrition 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 238000001802 infusion Methods 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000002736 nonionic surfactant Substances 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- OTYBMLCTZGSZBG-UHFFFAOYSA-L potassium sulfate Chemical compound [K+].[K+].[O-]S([O-])(=O)=O OTYBMLCTZGSZBG-UHFFFAOYSA-L 0.000 description 1
- 229910052939 potassium sulfate Inorganic materials 0.000 description 1
- 235000011151 potassium sulphates Nutrition 0.000 description 1
- 235000009518 sodium iodide Nutrition 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
Landscapes
- External Artificial Organs (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Filtering Materials (AREA)
- Investigating Or Analysing Biological Materials (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、白血球分離用フィルタ
ーに関するものである。詳しく述べると本発明は白血球
に対して安定した捕捉能を示し、かつ異物の混入の恐れ
のない白血球分離用フィルターに関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a leukocyte separating filter. More specifically, the present invention relates to a leukocyte separation filter which has a stable capturing ability for leukocytes and which is free from the possibility of contamination by foreign matter.
【0002】[0002]
【従来の技術】輸血の形態が従来の全血輸血から、患者
が必要としている成分のみを輸血する成分輸血へと変化
して久しいが、この成分輸血においては、分画した血液
成分の純度をいかに高くするかが課題となっている。従
来、献血によって得られた血液は、遠心操作によって赤
血球濃厚液(CRC)、濃縮血小板血漿(PC)および
乏血小板血漿(PPP)に分離される。このようにして
分離された血球製剤は、赤血球あるいは血小板を必要と
する患者への成分輸血に広く用いられているが、各血球
製剤は、多くの白血球を含んでおり、輸血により多量の
白血球が輸注されていることが問題視されている。血球
製剤に含まれる白血球は、輸血後の副作用を防止する上
からも極力除去する必要があり、このために従来より多
くの工夫がなされている。その方法としては、血球の比
重差を利用した重力遠心分離法、白血球の粘着ないしは
付着等の作用を利用した捕捉材利用の方法等が使用され
ている。2. Description of the Related Art The form of blood transfusion has long changed from conventional whole blood transfusion to component transfusion in which only the components required by the patient are transfused. In this component transfusion, the purity of the fractionated blood components is changed. The issue is how to raise it. Conventionally, blood obtained by donating blood is separated into concentrated red blood cell liquid (CRC), concentrated platelet plasma (PC) and platelet poor plasma (PPP) by centrifugation. The blood cell preparation thus separated is widely used for component transfusion to patients who need red blood cells or platelets, but each blood cell preparation contains many white blood cells, and a large amount of white blood cells is produced by the blood transfusion. It is regarded as a problem that it is infused. Leukocytes contained in blood cell preparations need to be removed as much as possible in order to prevent side effects after blood transfusion, and for this reason, many innovations have been made in the past. As the method, there are used a gravity centrifugation method utilizing a difference in specific gravity of blood cells, a method utilizing a capturing material utilizing an action such as adhesion or adhesion of leukocytes, and the like.
【0003】これらの方法の中で、捕捉材利用の方法が
白血球除去効率の良さ、手技の簡便なことなどから広く
用いられており、天然繊維、合成繊維等の捕捉材がある
が繊維径の非常に小さな繊維をカラム内にそのまま詰め
たものや不織布等に二次加工したものが多くの場合用い
られている。しかしながら、この様な繊維を用いる場合
においては操作中に繊維の脱落の危険性は免れず、異物
流出の恐れがあった。Among these methods, the method of using a capturing material is widely used because of its excellent leukocyte removal efficiency and simple procedure, and there are capturing materials such as natural fibers and synthetic fibers, which have a large fiber diameter. In many cases, very small fibers packed in the column as they are or secondary processed into a non-woven fabric are used. However, when such a fiber is used, there is an unavoidable risk of the fiber falling off during the operation, and there is a risk of foreign matter outflow.
【0004】[0004]
【発明が解決しようとする問題点】したがって、本発明
は新規な白血球分離用フィルターを提供することを目的
とする。本発明はまた、白血球に対して高くかつ安定し
た捕捉能を有し、血液中より効率よく白血球を分離し得
る白血球分離用フィルターを提供することを目的とす
る。本発明はさらに操作時における異物の流出の恐れが
なく、安全に白血球分離操作を行ない得る白血球分離用
フィルターを提供することを目的とする。本発明はまた
フィルターの製造工程を簡易なものとし、かつ製品の性
能のバラツキの少ない白血球分離用フィルターを提供す
ることを目的とする。SUMMARY OF THE INVENTION Therefore, an object of the present invention is to provide a novel leukocyte separation filter. Another object of the present invention is to provide a leukocyte separation filter that has a high and stable capturing ability for leukocytes and that can efficiently separate leukocytes from blood. A further object of the present invention is to provide a leukocyte separation filter that can safely perform leukocyte separation operation without the risk of foreign matter flowing out during operation. Another object of the present invention is to provide a filter for separating leukocytes, which simplifies the manufacturing process of the filter and has less variation in product performance.
【0005】[0005]
【問題点を解決するための手段】上記諸目的は、最頻
(最多)気孔径1〜5μmの連続開放気孔を有する三次
元網目状連続組織の多孔体からなる白血球分離用フィル
ターにより達成される。[Means for Solving the Problems] The above-described objects are achieved by a leukocyte separation filter comprising a porous body having a three-dimensional reticulated continuous tissue having continuous open pores having a most frequent (most) pore diameter of 1 to 5 μm. .
【0006】本発明は、多孔体がビニルホルマールまた
はポリウレタン樹脂からなる白血球分離用フィルターで
ある。The present invention is a leukocyte separating filter in which a porous body is made of vinyl formal or polyurethane resin.
【0007】[0007]
【作用】本発明の白血球分離用フィルターは、最頻(最
多)気孔径1〜5μmの連続開放気孔を有する三次元網
目状連続組織の多孔体からなることを特徴とするもので
ある。The white blood cell separation filter of the present invention is characterized by comprising a porous body having a three-dimensional network continuous structure having continuous open pores having a most frequent (most frequent) pore diameter of 1 to 5 μm.
【0008】この様にマトリックスが3次元網目状連続
組織である上記の如き一定の範囲の気孔径を有する多孔
体で血液等の白血球懸濁液を処理すると、懸濁液中に含
まれる白血球は、多孔体のマトリックス間に形成される
連続開放気孔よりなる複雑な流路を通過する間に効率よ
く捕捉されるものである。さらに、フィルターの流路
は、多孔体の三次元網目状連続組織、すなわち、多孔体
のマトリックスにより形成される連続開放気孔であるた
め、フィルターの流路は多孔体の成型時に形成されるこ
ととなるゆえ、該多孔体を用いて白血球分離フィルター
を製造する際の製造工程は極めて簡易なもので、また製
品の性能のバラツキは連続組織であるために安定したも
のであり、操作時における該多孔体からの異物の流出あ
るいは流路のチャンネリングなどの問題も本質的に生じ
ないものである。When a leukocyte suspension such as blood is treated with a porous body having a pore size within a certain range as described above in which the matrix is a three-dimensional network continuous tissue, leukocytes contained in the suspension are treated. , Is efficiently trapped while passing through a complicated flow path composed of continuous open pores formed between the matrices of the porous body. Furthermore, since the flow path of the filter is a three-dimensional network continuous structure of the porous body, that is, continuous open pores formed by the matrix of the porous body, the flow path of the filter is formed during the molding of the porous body. Therefore, the production process for producing a leukocyte separation filter using the porous body is extremely simple, and the variation in product performance is stable because it is a continuous structure, and Problems such as the outflow of foreign matter from the body and channel channeling do not essentially occur.
【0009】以下、本発明を実施態様に基づきより詳細
に説明する。Hereinafter, the present invention will be described in more detail based on the embodiments.
【0010】本発明の白血球分離用フィルターは、連続
開放気孔を有する三次元網目状連続組織の多孔体からな
るものであり、さらに多孔体の材質がポリビニルホルマ
ールまたはポリウレタン樹脂からなるものである。The leukocyte separating filter of the present invention comprises a porous body having a continuous three-dimensional network structure having continuous open pores, and the material of the porous body is polyvinyl formal or polyurethane resin.
【0011】本発明に関わる上記の如き構造を有する多
孔体において連続開放気孔の最頻(最多)気孔径は1〜
5μm、好ましくは2〜4μmであることが望ましい。
すなわち、気孔径が1μm未満であると白血球除去操作
時において、処理される血液あるいは白血球懸濁液中に
含まれる他の血球までもが捕捉されてしまい、目詰まり
を引き起こす恐れがある。一方、気孔径が5μmを越え
るものであると、処理される白血球懸濁液との接触頻度
が低下するために白血球の補捉率が低下してしまう恐れ
があるためである。In the porous body having the above-mentioned structure according to the present invention, the most frequent (most) pore size of continuous open pores is 1 to.
It is desirable that the thickness is 5 μm, preferably 2 to 4 μm.
That is, if the pore diameter is less than 1 μm, the blood to be treated or other blood cells contained in the leukocyte suspension may be captured during the leukocyte removal operation, which may cause clogging. On the other hand, when the pore diameter is more than 5 μm, the frequency of contact with the leukocyte suspension to be treated is reduced, which may reduce the leukocyte capture rate.
【0012】なお、本発明における「最頻(最多)気孔
径」とは、多孔体を任意に切断し、断面全体に分散して
いる細孔の各々について面積を測定して円に換算した直
径を求め、直径と細孔の数との関係を調べたときに、円
に換算した直径が最も数の多いところを表すものであ
る。すなわち、多孔体の任意の切断面に分散する細孔は
色々な形で、その直径も様々であるが、個々の細孔をそ
の細孔の断面積と同じ面積の円に換算し、その直径を1
μm間隔で横軸にとり、縦軸にその区間の(1μmごと
の)細孔数をそれぞれとってグラフに曲線を描いたとき
に、その曲線のピークに当る直径が本明細書でいう最頻
(最多)気孔径である。この時細孔はランダムに2,0
00個以上数えるのが好ましい。したがって、最頻(最
多)直径以上の細孔は数が少なくなることを表すもので
あって、これ以上の直径の粒子は通過しないというもの
ではない。The "most frequent (most) pore diameter" in the present invention is a diameter obtained by cutting a porous body arbitrarily, measuring the area of each of the pores dispersed in the entire cross section, and converting it into a circle. When the relationship between the diameter and the number of pores is determined by finding the value, the diameter converted into a circle represents the most number. That is, the pores dispersed on any cut surface of the porous body have various shapes and have various diameters, but each pore is converted into a circle having the same area as the cross-sectional area of the pore, and its diameter is 1
When a curve is drawn on a graph with the horizontal axis at μm intervals and the number of pores (every 1 μm) in that section on the vertical axis, the diameter at the peak of the curve is the mode ( (Most) pore size. At this time, the pores are randomly set to 2,0
It is preferable to count 00 or more. Therefore, the number of pores having the most frequent (most) diameter or more means that the number is small, and it does not mean that particles having a diameter larger than this do not pass through.
【0013】また、この様な多孔体の空孔率は、最頻
(最多)気孔径等によっても左右されるが、75〜95
%、より望ましくは80〜95%であることが好まし
い。すなわち、空孔率が75%以上であると白血球除去
処理操作をより短時間で行うことができ、一方、空孔率
が95%以下であるとフィルターとしての強度の点で優
れるためである。さらに、この様な多孔体の厚さは、最
頻(最多)気孔径、気孔率およびマトリックスである三
次元網目状連続組織の微細構造等によっても左右される
が0.1〜10mm、より望ましくは0.5〜3mm程
度であることが好ましい。すなわち、多孔体の厚さが
0.1mm以上であるとフィルターの強度の点で優れ、
10mm以下であると濾過層長が長くなり過ぎず、目詰
まりの可能性が低くなるためである。The porosity of such a porous material depends on the most frequent (most) pore diameter and the like, but is 75 to 95.
%, And more preferably 80 to 95%. That is, when the porosity is 75% or more, the leukocyte removal treatment operation can be performed in a shorter time, while when the porosity is 95% or less, the strength of the filter is excellent. Further, the thickness of such a porous body depends on the most frequent (most) pore diameter, the porosity, the fine structure of the three-dimensional network continuous structure which is a matrix, and the like, but is more preferably 0.1 to 10 mm. Is preferably about 0.5 to 3 mm. That is, when the thickness of the porous body is 0.1 mm or more, the strength of the filter is excellent,
This is because if the thickness is 10 mm or less, the length of the filtration layer does not become too long and the possibility of clogging decreases.
【0014】本発明に係わる多孔体は、所望の構造を有
するものであれば、特にその材質を限定されるものでは
ないが、血球に損傷を与えにくいものであることが望ま
れる。また、フィルターで処理する血液製剤等の種類に
より、例えば、赤血球濃厚液を処理する場合は血小板が
付着し易い材質であることが望まれ、濃縮血小板血漿を
処理する場合は血小板が付着しにくい材質であることが
望まれる。The porous material according to the present invention is not particularly limited in its material as long as it has a desired structure, but it is desired that it is less likely to damage blood cells. Further, depending on the type of blood product or the like to be treated with a filter, for example, when processing a concentrated red blood cell, it is desired that the material to which platelets are likely to adhere is desired, and when treating concentrated platelet plasma, the material to which platelets are unlikely to be adhered. Is desired.
【0015】本発明に係わるポリビニルホルマールは、
所望の構造を有するものであれば、いかなる方法によっ
て得られたものであってもよいが、澱粉、デキストリン
等のアミローズを含有する多糖類およびその誘導体、耐
酸性を有するアニオン型界面活性剤、および非イオン型
界面活性剤などの気孔生成剤を含有するポリビニルアル
コール水溶液に、必要に応じて硫酸ナトリウム、塩化ナ
トリウム、硫酸アンモニウム、塩化アンモニウム、硫酸
カリウム、ヨウ化ナトリウム等の無機塩を存在させ、ホ
ルムアルデヒドおよび酸触媒を作用させてアセタール化
反応を行なう溶出法(特公昭47−46455号、特公
昭48−20019号)により得られたものが所望の構
造を有することから特に好ましい。The polyvinyl formal according to the present invention is
It may be obtained by any method as long as it has a desired structure, but starch, polysaccharides containing amylose such as dextrin and derivatives thereof, anionic surfactant having acid resistance, and If necessary, an inorganic salt such as sodium sulfate, sodium chloride, ammonium sulfate, ammonium chloride, potassium sulfate, or sodium iodide is present in an aqueous polyvinyl alcohol solution containing a pore-forming agent such as a nonionic surfactant, and formaldehyde and Those obtained by the elution method (Japanese Patent Publication No. 47-46455 and Japanese Patent Publication No. 48-20019) in which an acetalization reaction is performed by using an acid catalyst are particularly preferable because they have a desired structure.
【0016】本発明に係わるポリウレタン樹脂としては
ポリウレタンの合成樹脂発泡体、あるいは合成樹脂多孔
質体の表面にセグメント化ポリウレタン等の血球の付着
しにくい材料等をコーティングしたものが好ましい。The polyurethane resin according to the present invention is preferably a synthetic resin foam of polyurethane, or a synthetic resin porous body coated with a material such as segmented polyurethane which does not easily adhere to blood cells.
【0017】本発明の白血球分離用フィルターの一実施
態様を図を用いて説明する。図1は本発明の白血球分離
用フィルターの一実施態様を示す断面図である。本実施
態様において白血球分離用フィルター1は、血液流入口
2と血液流出口3とを備えてなるハウジング4内に上記
したような構成を有するポリビニルホルマールまたはポ
リウレタン樹脂製の多孔体5がハウジング4の内部空間
を横切って設けられているものである。なおこのような
白血球分離用フィルター1において、多孔体5をハウジ
ング4内に保持するために、例えば、多孔体5の前後に
通液性の支持材6a 、6b を設け、該支持材6a 、6b
により多孔体5を挟持することは任意である。この白血
球分離用フィルター1は、例えば図2に示されるような
回路中に組入れられて実際に使用される。図2に示され
る回路において、処理しようとする血液成分を入れた血
液バッグ7および生理食塩水を入れた生理食塩水バッグ
8が白血球分離用フィルター1より上方に位置させら
れ、それぞれクレンメ9a 、9b を具備してなる導液チ
ューブ10a 、10b により白血球分離用フィルター1
の血液流入口2に連通されており、一方、白血球分離用
フィルター1の下方には生理食塩水回収用バッグ11と
処理された血液成分を回収するための血液回収用バッグ
12が位置させられ、それぞれクレンメ9c 、9d を具
備してなる導液チューブ10c 、10d により白血球分
離用フィルター1の血液流出口3に連通されている。白
血球分離操作はまずクレンメ9b 、9c を開き、クレン
メ9a 、9d を閉じた状態で生理食塩水バッグ8より生
理食塩水を白血球分離用フィルター1に流し、白血球分
離用フィルター1内をプライミングする。なおプライミ
ングに用いられた生理食塩水は生理食塩水回収バッグ1
0に回収される。プライミングを行なった後に今度はク
レンメ9a、9d を開き、クレンメ9b 、9c を閉じて
血液バッグ7より血液成分を白血球分離用フィルター1
に流す。白血球分離用フィルター1内において血液成分
は上記のごとき構成を有する多孔体5を通過する際に該
多孔体5により白血球成分を吸着捕捉され、白血球を分
離されたものとなる。このように白血球成分を除去され
た血液成分は連通する血液回収バッグ12に回収され
る。血液バッグ7より血液成分を流し終わったなら、白
血球分離用フィルター1内に残った血液を回収するため
に、さらにクレンメ9bを開き白血球分離用フィルター
1内に再び生理食塩水を流して白血球分離用フィルター
1内に残存する血液を押し出して血液回収用バッグ12
に回収し、ほぼ血液成分を回収し終えた時点でクレンメ
9d を閉じクレンメ9c を開いて血液回収に用いた生理
食塩水を生理食塩水回収用バッグ11内に回収して、白
血球分離操作を終える。One embodiment of the leukocyte separation filter of the present invention will be described with reference to the drawings. FIG. 1 is a sectional view showing an embodiment of the leukocyte separation filter of the present invention. In the present embodiment, the leukocyte separation filter 1 has a porous body 5 made of polyvinyl formal or polyurethane resin having the above-described structure in a housing 4 having a blood inlet 2 and a blood outlet 3. It is provided across the internal space. In order to hold the porous body 5 in the housing 4 in such a leukocyte separation filter 1, for example, liquid-permeable support materials 6a and 6b are provided before and after the porous body 5, and the support materials 6a and 6b are provided.
It is optional to sandwich the porous body 5 with. The white blood cell separation filter 1 is actually used by being incorporated in a circuit as shown in FIG. 2, for example. In the circuit shown in FIG. 2, a blood bag 7 containing a blood component to be processed and a physiological saline bag 8 containing physiological saline are positioned above the leukocyte separation filter 1 and are respectively clamps 9a and 9b. Filter 1 for separating white blood cells by liquid guiding tubes 10a and 10b equipped with
, Which is in communication with the blood inlet port 2, while a physiological saline solution collection bag 11 and a blood collection bag 12 for collecting the treated blood component are positioned below the white blood cell separation filter 1. The blood flow outlets 3 of the leukocyte separation filter 1 are communicated with the liquid guide tubes 10c and 10d, which are provided with clamps 9c and 9d, respectively. In the white blood cell separation operation, first, with the clamps 9b and 9c opened and the clamps 9a and 9d closed, physiological saline is flown from the physiological saline bag 8 to the leukocyte separation filter 1 to prime the inside of the leukocyte separation filter 1. The physiological saline used for priming is the saline recovery bag 1
Recovered to 0. After the priming, this time, the clamps 9a and 9d are opened, the clamps 9b and 9c are closed, and blood components are separated from the blood bag 7 by the white blood cell separation filter 1.
Shed on. In the white blood cell separation filter 1, when the blood component passes through the porous body 5 having the above-mentioned configuration, the white blood cell component is adsorbed and captured by the porous body 5 to separate the white blood cells. The blood component from which the white blood cell component has been removed in this manner is recovered in the blood recovery bag 12 in communication therewith. After the blood components have been flushed from the blood bag 7, in order to collect the blood remaining in the leukocyte separation filter 1, the clamp 9b is further opened and physiological saline is again poured into the leukocyte separation filter 1 for leukocyte separation. Blood collection bag 12 that pushes out the blood remaining in the filter 1
And when almost all blood components have been collected, the clamp 9d is closed and the clamp 9c is opened to recover the physiological saline used for blood recovery in the physiological saline recovery bag 11 to complete the leukocyte separation operation. .
【0018】[0018]
【実施例】以下、本発明を実施例によりさらに具体的に
説明する。EXAMPLES The present invention will be described in more detail below with reference to examples.
【0019】実施例1
最頻(最多)気孔径2〜3μm、気孔率86%のポリビ
ニルホルマール製多孔体を厚さ1.3mm、濾過面積1
00cm2のものとして図1に示すような白血球分離用
フィルターを作製し、さらに図2に示すような回路を用
いて該白血球分離用フィルターに400ml採血して得
られたCPD加ヒト赤血球濃厚液(CRC)1単位を自
然落差で流した。この結果、処理に要する時間は6分で
あり、また処理前後のCRC中の血球数を自動血球算定
装置(Sysmex NE−6000、東亜医用電子(株)
製)を用いて算定の後、液量に基づいて各血球成分の絶
対数を求め、これより白血球除去率を求めたところ99
%であり、また赤血球の回収率は98%であり、さらに
血小板除去率は90%であった。Example 1 A polyvinyl formal porous body having a most frequent (most) pore diameter of 2 to 3 μm and a porosity of 86% had a thickness of 1.3 mm and a filtration area of 1
A white blood cell separation filter as shown in FIG. 1 having a size of 00 cm 2 was prepared, and 400 ml of blood was collected on the white blood cell separation filter using the circuit shown in FIG. (CRC) 1 unit was run by natural head. As a result, the time required for the treatment is 6 minutes, and the blood cell count in the CRC before and after the treatment is automatically measured by a blood cell counter (Sysmex NE-6000, Toa Medical Electronics Co., Ltd.).
After the calculation, the absolute number of each blood cell component was calculated based on the liquid volume, and the leukocyte removal rate was calculated from this.
%, The recovery rate of red blood cells was 98%, and the platelet removal rate was 90%.
【0020】実施例2
最頻(最多)気孔径2〜3μm、気孔率82%のポリウ
レタン樹脂製多孔体を厚さ1.0mm、濾過面積50c
m2のものとして図1に示すような白血球分離用フィル
ターを作製し、さらに図2に示すような回路を用いて該
白血球分離用フィルターに200ml採血して得られた
CPD加ヒト濃縮血小板血漿(PC)10単位を点滴速
度(約4ml/min.)で流した。この結果、滴下速
度が遅くなることもなく、また処理前後のPC中の血球
数を自動血球算定装置(SysmexNE−6000、東亜医
用電子(株)製)とフローサイトメーター(Cyto-ACE1
50、日本分光(株)製)を用いて算定の後、液量に基
づいて各血球成分の絶対数を求め、これより白血球除去
率を求めたところ99.9%であり、また血小板回収率
は95%であった。Example 2 A polyurethane resin porous body having a most frequent (most) pore diameter of 2 to 3 μm and a porosity of 82% had a thickness of 1.0 mm and a filtration area of 50 c.
A white blood cell separation filter as shown in FIG. 1 was prepared for m 2 and further 200 ml of blood was collected on the white blood cell separation filter using the circuit as shown in FIG. 10 units of PC) was flown at an infusion rate (about 4 ml / min.). As a result, the dropping rate does not slow down, and the blood cell counts in the PC before and after the treatment are automatically measured with a blood cell counter (Sysmex NE-6000, manufactured by Toa Medical Electronics Co., Ltd.) and a flow cytometer (Cyto-ACE1).
50, manufactured by JASCO Corporation, the absolute number of each blood cell component was calculated based on the liquid volume, and the leukocyte removal rate was calculated from the absolute number, which was 99.9%, and the platelet recovery rate was also calculated. Was 95%.
【0021】[0021]
【発明の効果】以上、述べたように、本発明は最頻(最
多)気孔径1〜5μmの連続開放気孔を有する三次元網
目状連続組織の多孔体からなる白血球分離用フィルター
であるから、白血球に対して高く安定した捕捉能を有
し、血液等の白血球懸濁液より白血球成分を効率よく分
離し得るものであり、また、操作時における濾材の脱落
による異物の混入の恐れもなく、安全に白血球除去操作
を行い得るものである。As described above, the present invention is a leukocyte separation filter comprising a porous body having a three-dimensional reticulated continuous tissue having continuous open pores having a most frequent (most) pore diameter of 1 to 5 μm. It has a high and stable capturing ability for leukocytes, and can efficiently separate leukocyte components from leukocyte suspensions such as blood, and there is no fear of contamination by foreign substances due to the dropping of the filter medium during operation, It is possible to safely perform leukocyte removal operation.
【図1】本発明の白血球分離用フィルターの一実施態様
を示す断面図である。FIG. 1 is a cross-sectional view showing an embodiment of a leukocyte separation filter of the present invention.
【図2】本発明の白血球分離用フィルターの一実施態様
を組込んだ血液処理回路を示す回路図である。FIG. 2 is a circuit diagram showing a blood processing circuit incorporating an embodiment of the leukocyte separation filter of the present invention.
1…白血球分離用フィルター、2…血液流入口、3…血
液流出口、4…ハウジング、5…ポリビニルホルマール
多孔体、6a ,6b …支持材、7…血液バッグ、8…生
理食塩水バッグ、9a ,9b ,9c ,9d …クレンメ、
10a ,10b ,10c ,10d …導液チューブ、11
…生理食塩水回収用バッグ、12…血液回収用バッグ。1 ... Leukocyte separation filter, 2 ... Blood inlet, 3 ... Blood outlet, 4 ... Housing, 5 ... Polyvinyl formal porous body, 6a, 6b ... Support material, 7 ... Blood bag, 8 ... Saline solution bag, 9a , 9b, 9c, 9d ... Clemme,
10a, 10b, 10c, 10d ... Liquid conducting tube, 11
... Saline saline bag, 12 ... Blood bag.
Claims (3)
放気孔を有する三次元網目状連続組織の多孔体からなる
白血球分離用フィルター1. A filter for separating leukocytes comprising a porous body having a continuous three-dimensional network structure having continuous open pores having a most frequent (most frequent) pore diameter of 1 to 5 μm.
請求項1に記載の白血球分離用フィルター2. The leukocyte separation filter according to claim 1, wherein the porous body is made of polyvinyl formal.
項1に記載の白血球分離用フィルター3. The leukocyte separation filter according to claim 1, wherein the porous body is made of a polyurethane resin.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3187900A JPH0534337A (en) | 1991-07-26 | 1991-07-26 | Filter for separating leucocyte |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3187900A JPH0534337A (en) | 1991-07-26 | 1991-07-26 | Filter for separating leucocyte |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0534337A true JPH0534337A (en) | 1993-02-09 |
Family
ID=16214165
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3187900A Pending JPH0534337A (en) | 1991-07-26 | 1991-07-26 | Filter for separating leucocyte |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0534337A (en) |
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0630675A1 (en) * | 1993-06-27 | 1994-12-28 | Terumo Kabushiki Kaisha | Leukocyte or leukocyte/platelet remover and filter therefor |
US5647985A (en) * | 1994-10-17 | 1997-07-15 | Baxter International Inc. | Whole blood leukodepletion and platelet filter |
US5728306A (en) * | 1994-12-23 | 1998-03-17 | Baxter International Inc. | Leukodepletion filter and method for filtering leukocytes from freshly drawn blood |
US5972217A (en) * | 1994-10-17 | 1999-10-26 | Baxter International Inc. | Blood cell separation devices having a membrane with particular coating |
US6045701A (en) * | 1994-10-17 | 2000-04-04 | Baxter International Inc. | Method of filtering a fluid suspension with a membrane having a particular coating |
US6648922B2 (en) | 1994-10-17 | 2003-11-18 | Baxter International Inc. | Method for producing improved medical devices and devices so produced |
US6746482B2 (en) | 1994-10-17 | 2004-06-08 | Baxter International Inc. | Method for producing medical devices and devices so produced |
JP2008540108A (en) * | 2005-05-20 | 2008-11-20 | アクアポリン エーピーエス | Membrane to filter water |
JP2010275401A (en) * | 2009-05-27 | 2010-12-09 | Nikkiso Co Ltd | Porous beads |
US8999167B2 (en) | 2003-08-07 | 2015-04-07 | Asahi Kasei Medical Co., Ltd. | Composite porous membrane and process for producing the same |
KR101540620B1 (en) * | 2014-05-19 | 2015-07-31 | 진화메디칼 주식회사 | Filter |
US9205432B2 (en) | 2012-04-30 | 2015-12-08 | Korea Institute Of Machinery & Materials | Apparatus for self-extracting cells using magnetic field and method for self-extracting cells using the same |
JP2020072752A (en) * | 2016-03-18 | 2020-05-14 | 株式会社村田製作所 | Filter for filtering nucleated cells and filtering method using the same |
US12018277B2 (en) | 2017-04-26 | 2024-06-25 | Murata Manufacturing Co., Ltd. | Filter for filtering nucleated cells and filtering method using the same |
-
1991
- 1991-07-26 JP JP3187900A patent/JPH0534337A/en active Pending
Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0630675A1 (en) * | 1993-06-27 | 1994-12-28 | Terumo Kabushiki Kaisha | Leukocyte or leukocyte/platelet remover and filter therefor |
US6746482B2 (en) | 1994-10-17 | 2004-06-08 | Baxter International Inc. | Method for producing medical devices and devices so produced |
US5647985A (en) * | 1994-10-17 | 1997-07-15 | Baxter International Inc. | Whole blood leukodepletion and platelet filter |
US7422606B2 (en) | 1994-10-17 | 2008-09-09 | Edwards Lifesciences Corporation | Medical devices and products having coatings applied thereto |
US5795483A (en) * | 1994-10-17 | 1998-08-18 | Baxter International Inc. | Method of separating leukocytes from blood cells using a leukodepletion filter |
US5972217A (en) * | 1994-10-17 | 1999-10-26 | Baxter International Inc. | Blood cell separation devices having a membrane with particular coating |
US6045701A (en) * | 1994-10-17 | 2000-04-04 | Baxter International Inc. | Method of filtering a fluid suspension with a membrane having a particular coating |
US6648922B2 (en) | 1994-10-17 | 2003-11-18 | Baxter International Inc. | Method for producing improved medical devices and devices so produced |
US5885457A (en) * | 1994-12-23 | 1999-03-23 | Baxter International Inc. | Filtration media for filtering leukocytes from freshly drawn blood |
US5728306A (en) * | 1994-12-23 | 1998-03-17 | Baxter International Inc. | Leukodepletion filter and method for filtering leukocytes from freshly drawn blood |
US8999167B2 (en) | 2003-08-07 | 2015-04-07 | Asahi Kasei Medical Co., Ltd. | Composite porous membrane and process for producing the same |
JP2008540108A (en) * | 2005-05-20 | 2008-11-20 | アクアポリン エーピーエス | Membrane to filter water |
JP2010275401A (en) * | 2009-05-27 | 2010-12-09 | Nikkiso Co Ltd | Porous beads |
US9205432B2 (en) | 2012-04-30 | 2015-12-08 | Korea Institute Of Machinery & Materials | Apparatus for self-extracting cells using magnetic field and method for self-extracting cells using the same |
KR101540620B1 (en) * | 2014-05-19 | 2015-07-31 | 진화메디칼 주식회사 | Filter |
JP2020072752A (en) * | 2016-03-18 | 2020-05-14 | 株式会社村田製作所 | Filter for filtering nucleated cells and filtering method using the same |
US11485951B2 (en) | 2016-03-18 | 2022-11-01 | Murata Manufacturing Co., Ltd. | Filter for filtration of nucleated cells and filtration method using the same |
US12018277B2 (en) | 2017-04-26 | 2024-06-25 | Murata Manufacturing Co., Ltd. | Filter for filtering nucleated cells and filtering method using the same |
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