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CN102631722B - Blood plasma separation adsorber capable of blood purification - Google Patents

Blood plasma separation adsorber capable of blood purification Download PDF

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CN102631722B
CN102631722B CN201210126708.2A CN201210126708A CN102631722B CN 102631722 B CN102631722 B CN 102631722B CN 201210126708 A CN201210126708 A CN 201210126708A CN 102631722 B CN102631722 B CN 102631722B
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董凡
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Jafron Biomedical Co Ltd
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Abstract

本发明公开一种血浆分离吸附器,包括:壳体,内部设有入口缓冲腔、出口缓冲腔及血液净化腔,在入口缓冲腔的壁部设有血液入口,在出口缓冲腔的壁部设有血液出口,在血液净化腔的壁部设有血浆出口;至少一种空心纤维膜,安装在血液净化腔中,其中每根空心纤维膜的两端均分别与入口缓冲腔和出口缓冲腔相连通;至少一种纤维状吸附剂,安装在血液净化腔中。具有血浆分离和血浆吸附是同时进行,可使血浆吸附流程缩短,减少体外循环的血液量,从而降低患者的负担和血液不相容的风险等优点。

The invention discloses a plasma separation adsorber, which comprises: a shell, which is provided with an inlet buffer chamber, an outlet buffer chamber and a blood purification chamber, a blood inlet is arranged on the wall of the inlet buffer chamber, and a blood inlet is arranged on the wall of the outlet buffer chamber. There is a blood outlet, and a plasma outlet is provided on the wall of the blood purification chamber; at least one hollow fiber membrane is installed in the blood purification chamber, and the two ends of each hollow fiber membrane are respectively connected with the inlet buffer chamber and the outlet buffer chamber pass; at least one fibrous adsorbent installed in the blood purification cavity. It has the advantages of simultaneous plasma separation and plasma adsorption, which can shorten the plasma adsorption process and reduce the amount of blood in extracorporeal circulation, thereby reducing the burden on patients and the risk of blood incompatibility.

Description

一种可进行血液净化的血浆分离吸附器A plasma separation adsorber capable of purifying blood

技术领域 technical field

本发明涉及一种血液净化装置,特别是一种可同时进行血浆分离和血浆吸附的血浆分离吸附器。 The invention relates to a blood purification device, in particular to a plasma separation adsorber capable of simultaneously performing plasma separation and plasma adsorption.

背景技术 Background technique

血浆吸附疗法对血细胞损伤小,对人体内环境影响小,在血液净化领域得到广泛应用。血浆吸附疗法的基本原理是将患者体内血液引到体外,通过先将血浆与血细胞分离,再针对性的将血浆中的致病物质吸附除去,以达到治疗疾病的目的。根据所选择吸附剂的不同,该治疗方式可用于治疗人体自身免疫疾病、代谢性疾病、内外源性中毒。 Plasma adsorption therapy has little damage to blood cells and has little impact on the internal environment of the human body, and has been widely used in the field of blood purification. The basic principle of plasma adsorption therapy is to introduce blood from the patient's body to the outside of the body, firstly separate the plasma from blood cells, and then specifically adsorb and remove the pathogenic substances in the plasma to achieve the purpose of treating diseases. Depending on the selected adsorbent, this treatment method can be used to treat human autoimmune diseases, metabolic diseases, and endogenous poisoning.

图1是目前常见的血浆吸附疗法的流程图。如图1所示,从人体动脉流出的血液沿箭头所示方向,先经血泵100进入到血浆分离器200内,通过血浆分离器200的筛分作用将血浆与血细胞分离开,然后将分离出的血浆通过血泵300再引入到血浆吸附柱400内,利用血浆吸附柱400内装载的吸附剂的吸附作用针对性的清除血浆中的各种致病物质。其中,血浆分离器200中充填的是空心纤维膜。这个过程中串联的设备较多,医护人员的操作难度较大,并且体外循环的血液量较大,接触的医疗器械较多,这在增加了患者的身体负担的同时也使溶血、凝血等问题出现的概率增大,增大了治疗时的安全风险。另外,全套血浆吸附器材成本也比较高。上述这些问题导致血浆吸附治疗模式难以在国内广泛推广。 Figure 1 is a flow chart of the current common plasma adsorption therapy. As shown in Figure 1, the blood flowing out from the human artery enters the plasma separator 200 through the blood pump 100 along the direction indicated by the arrow, and the plasma and blood cells are separated by the sieving function of the plasma separator 200, and then the separated The blood plasma is reintroduced into the plasma adsorption column 400 through the blood pump 300, and various pathogenic substances in the plasma are targetedly removed by the adsorption effect of the adsorbent loaded in the plasma adsorption column 400. Wherein, the plasma separator 200 is filled with hollow fiber membranes. In this process, there are many devices connected in series, the operation of medical staff is difficult, and the amount of blood in extracorporeal circulation is large, and there are many medical devices in contact, which not only increases the physical burden of patients, but also causes problems such as hemolysis and coagulation. The probability of occurrence increases, which increases the safety risk during treatment. In addition, the cost of a complete set of plasma adsorption equipment is relatively high. The above-mentioned problems make it difficult for the plasma adsorption therapy mode to be widely promoted in China.

还有,目前市场上普遍采用球形大孔树脂作为血浆吸附柱的吸附剂载体,通过在树脂微孔内接枝功能性配基得到大分子吸附剂,但球形吸附树脂为了保持一定的强度,孔径就无法过大,并且大孔的数量也不可能很多,这就提高了球形树脂接枝功能基团的难度,同时也使大分子物质无法快速扩散到微孔中,这导致球形树脂吸附剂对大分子物质的有效吸附面积远小于测得的实际表面积。 In addition, spherical macroporous resins are generally used as the adsorbent carrier of plasma adsorption columns in the market at present, and macromolecular adsorbents are obtained by grafting functional ligands in the resin micropores. It cannot be too large, and the number of macropores cannot be too large, which increases the difficulty of grafting functional groups on spherical resins, and also prevents macromolecular substances from quickly diffusing into micropores, which leads to spherical resin adsorbents. The effective adsorption area of macromolecular substances is much smaller than the measured actual surface area.

发明内容 Contents of the invention

本发明要解决的技术问题是提供一种可同时进行血浆分离和血浆吸附的血浆分离吸附器,不但可减少血浆吸附疗法所使用的设备,减少体外循环的血液量,而且结构简单。 The technical problem to be solved by the present invention is to provide a plasma separation adsorber that can simultaneously perform plasma separation and plasma adsorption, which can not only reduce the equipment used in plasma adsorption therapy, reduce the amount of blood in extracorporeal circulation, but also has a simple structure.

为解决上述技术问题,本发明提供的技术方案为:血浆分离吸附器,其特征在于:包括:壳体,内部设有入口缓冲腔、出口缓冲腔及血液净化腔,在入口缓冲腔的壁部设有血液入口,在出口缓冲腔的壁部设有血液出口,在血液净化腔的壁部设有血浆出口;至少一种空心纤维膜,安装在血液净化腔中,其中每根空心纤维膜的两端均分别与入口缓冲腔和出口缓冲腔相连通;至少一种纤维状吸附剂,安装在血液净化腔中。 In order to solve the above technical problems, the technical solution provided by the present invention is: a plasma separation adsorber, which is characterized in that it includes: a shell, which is provided with an inlet buffer chamber, an outlet buffer chamber and a blood purification chamber inside, and on the wall of the inlet buffer chamber A blood inlet is provided, a blood outlet is provided on the wall of the outlet buffer chamber, and a plasma outlet is provided on the wall of the blood purification chamber; at least one hollow fiber membrane is installed in the blood purification chamber, wherein each hollow fiber membrane Both ends are respectively connected with the inlet buffer chamber and the outlet buffer chamber; at least one kind of fibrous adsorbent is installed in the blood purification chamber.

具有上述结构的血浆分离吸附器,用于血浆分离的空心纤维膜和进行血浆吸附的纤维状吸附剂安装在同一壳体内,血液经入口缓冲腔进入空心纤维膜内,在跨膜压的作用下,血浆通过空心纤维膜侧壁上的微孔渗出,进入到血液净化腔。在血液净化腔内,分离出的血浆与纤维状吸附剂的表面充分接触,并使血浆中的致病物质被吸附。这个过程中,血浆分离和血浆吸附是同时进行的。籍此,可使血浆吸附流程缩短,减少了体外循环的血液量,从而降低了患者的负担和血液不相容的风险。另外,本发明的血浆分离吸附器不但结构简单,部件少,而且操作容易。此外,用于血浆分离的空心纤维膜和进行血浆吸附的纤维状吸附剂都比较容易取得,且价格较为便宜,因此本发明的血浆分离吸附器还具有制造容易、成本低等优点。 In the plasma separation adsorber with the above structure, the hollow fiber membrane used for plasma separation and the fibrous adsorbent for plasma adsorption are installed in the same housing, the blood enters the hollow fiber membrane through the inlet buffer chamber, and under the action of transmembrane pressure , the blood plasma seeps out through the micropores on the side wall of the hollow fiber membrane and enters the blood purification cavity. In the blood purification chamber, the separated plasma is in full contact with the surface of the fibrous adsorbent, and the pathogenic substances in the plasma are adsorbed. In this process, plasma separation and plasma adsorption are carried out simultaneously. Thereby, the process of plasma adsorption can be shortened, the blood volume of extracorporeal circulation can be reduced, thereby reducing the burden on patients and the risk of blood incompatibility. In addition, the plasma separation adsorber of the present invention not only has a simple structure, fewer parts, but also is easy to operate. In addition, the hollow fiber membrane used for plasma separation and the fibrous adsorbent for plasma adsorption are relatively easy to obtain and relatively cheap, so the plasma separation adsorber of the present invention also has the advantages of easy manufacture and low cost.

优选的方案之一为纤维状吸附剂与空心纤维膜在血液净化腔内呈混合均匀状。籍此,可使分离出的血浆与吸附剂表面能够充分接触,并使血浆中的致病物质被充分吸附。 One of the preferred schemes is that the fibrous adsorbent and the hollow fiber membrane are uniformly mixed in the blood purification cavity. Thereby, the separated plasma can be fully contacted with the surface of the adsorbent, and the pathogenic substances in the plasma can be fully adsorbed.

优选的方案之一是纤维状吸附剂的比表面积在0.05-100m2/g之间,更为优选的是在0.1-20m2/g之间。籍此,可以根据目标吸附物质分子量的大小而选择比表面积不同的吸附剂种类及数量,以获得最佳的吸附性能和安全性能。 One of the preferred schemes is that the specific surface area of the fibrous adsorbent is between 0.05-100m 2 /g, more preferably between 0.1-20m 2 /g. In this way, the types and quantities of adsorbents with different specific surface areas can be selected according to the molecular weight of the target adsorbed substance, so as to obtain the best adsorption performance and safety performance.

优选的方案之一是空心纤维膜的表面积在0.05-0.8m2之间。籍此,可在确保血浆分离量和分离速度的情况下,有效控制生产成本,确保血浆分离的效果。 One of the preferred schemes is that the surface area of the hollow fiber membrane is between 0.05-0.8m 2 . In this way, the production cost can be effectively controlled and the effect of plasma separation can be ensured under the condition of ensuring the plasma separation volume and separation speed.

优选的方案之一是纤维状吸附剂和空心纤维膜的截面积之和与所述壳体的截面积的比为0.1-0.65,以获得优异的血浆分离效果及吸附剂对致病物质的吸附性能。 One of the preferred schemes is that the ratio of the sum of the cross-sectional area of the fibrous adsorbent and the hollow fiber membrane to the cross-sectional area of the housing is 0.1-0.65, so as to obtain excellent plasma separation effect and the adsorption of the adsorbent to the pathogenic substance performance.

本发明血浆分离吸附器内的空心纤维膜可以直接采用市售的血浆分离膜,如聚醚砜、聚砜、聚丙烯等材质的血浆分离膜等,但并不局限于上述材质。优选生物相容性较好的聚醚砜、聚砜材质的血浆分离膜。 The hollow fiber membranes in the plasma separation adsorber of the present invention can directly use commercially available plasma separation membranes, such as plasma separation membranes made of polyethersulfone, polysulfone, polypropylene, etc., but are not limited to the above materials. Polyethersulfone and polysulfone plasma separation membranes with better biocompatibility are preferred.

纤维状吸附剂是以纤维为载体固载功能配基的吸附剂,优选中心部位不存在连续空腔的实心纤维。海岛型纤维是一种表面含有较多凹面和微孔的纤维,以其为载体制备的纤维状吸附剂,比普通纤维状吸附剂具有更大的有效吸附面积,对小分子和大分子物质均有较好的吸附能力。以海岛型纤维为载体的纤维状吸附剂,可以通过在海岛型纤维上固载功能配基自行制备。如,可用30-40μm的苯乙烯-聚丙烯共混海岛型纤维作为载体,在浓硫酸作用下接枝手臂,在氧化镁作用下固载多粘菌是通过素B配基,得到针对内毒素的纤维状吸附剂,具体制备方法可参考日本东丽(toray)公司专利US4661260。海岛型纤维可以是聚苯乙烯-聚丙烯共混物、聚砜、聚醚砜、聚乙烯-乙烯醇共聚物等不同材质,但并不局限于上述材质。目前,海岛型纤维的生产技术已经比较成熟,均可以通过商业途径购买到。 The fibrous adsorbent is an adsorbent in which functional ligands are immobilized on the fiber as a carrier, preferably a solid fiber with no continuous cavity in the center. The sea-island fiber is a kind of fiber with more concave surfaces and micropores on the surface. The fibrous adsorbent prepared by using it as a carrier has a larger effective adsorption area than ordinary fibrous adsorbents, and is suitable for small molecules and macromolecules. It has better adsorption capacity. The fibrous adsorbent with sea-island fibers as the carrier can be prepared by immobilizing functional ligands on the sea-island fibers. For example, 30-40 μm styrene-polypropylene blended island-in-the-sea fibers can be used as a carrier, and the arms are grafted under the action of concentrated sulfuric acid, and polymyxa is immobilized under the action of magnesium oxide. The specific preparation method of the fibrous adsorbent can refer to the patent US4661260 of Toray Corporation of Japan. The sea-island fibers can be made of different materials such as polystyrene-polypropylene blends, polysulfone, polyethersulfone, polyethylene-vinyl alcohol copolymer, but are not limited to the above materials. At present, the production technology of island-in-the-sea fibers is relatively mature, and all of them can be purchased through commercial channels.

本发明的血浆分离吸附器,针对不同致病物质,可选择固载有相应配基的纤维状吸附剂,以适应不同疾病的治疗。 In the plasma separation adsorber of the present invention, for different pathogenic substances, fibrous adsorbents immobilized with corresponding ligands can be selected to adapt to the treatment of different diseases.

本发明的血浆分离吸附器,用于血浆分离的空心纤维膜和用于血浆吸附的纤维状吸附剂的选择及其用量比,可以根据不同的用途,通过计算得出,这与现有技术中确定血浆分离器中空心纤维的数量及血浆吸附柱内吸附剂的量的方法基本相同,为节省起见,此处不再赘述。 The plasma separation adsorber of the present invention, the hollow fiber membrane used for plasma separation and the selection and dosage ratio of the fibrous adsorbent used for plasma adsorption can be obtained by calculation according to different purposes, which is different from that in the prior art The methods for determining the number of hollow fibers in the plasma separator and the amount of adsorbent in the plasma adsorption column are basically the same, and will not be described here for the sake of saving.

本发明的血浆分离吸附器,用于血浆分离的空心纤维膜和用于血浆吸附的纤维状吸附剂在血液净化腔内可以相互平行排列,亦可以相互交叉。可以相互混合后形成纤维束,亦可以形成网状。 In the plasma separation adsorber of the present invention, the hollow fiber membranes used for plasma separation and the fibrous adsorbents used for plasma adsorption can be arranged parallel to each other in the blood purification chamber, or can cross each other. They can be mixed together to form fiber bundles or to form a network.

附图说明 Description of drawings

图1为现有技术血浆吸附过程的流程图; Fig. 1 is the flowchart of prior art plasma adsorption process;

图2为本发明可进行血浆分离的血浆分离吸附器的截面图; Fig. 2 is a sectional view of the plasma separation adsorber capable of plasma separation in the present invention;

图3为本发明血浆分离吸附器的结构示意图; Fig. 3 is the structural representation of the plasma separation adsorber of the present invention;

图4为使用本发明可进行血浆分离的血浆分离吸附器的流程图。 Fig. 4 is a flow chart of the plasma separation adsorber capable of plasma separation using the present invention.

下面结合附图和具体实施方式对本发明予以进一步说明。 The present invention will be further described below in conjunction with the accompanying drawings and specific embodiments.

 具体实施方式 Detailed ways

实施例1Example 1

结合参考图2和图3,血浆分离吸附器A包括:壳体1、空心纤维膜21和以海岛形纤维为载体的纤维状吸附剂31、密封胶层一14、密封胶层二15。 Referring to FIG. 2 and FIG. 3 , the plasma separation adsorber A includes: a housing 1 , a hollow fiber membrane 21 , a fibrous adsorbent 31 with island-in-the-sea fibers as carriers, a sealant layer 14 , and a sealant layer 2 15 .

本实施例血浆分离吸附器A为立式的,壳体1包括顶盖11、底盖12和柱体13。由顶盖11、底盖12和柱体13围成的壳体内部空间通过密封胶层一14和密封胶层二15被分隔成三个腔室。该部分结构与图1中血浆分离器的结构基本相同,为节省起见,此处不赘述。 The plasma separation adsorber A in this embodiment is vertical, and the housing 1 includes a top cover 11 , a bottom cover 12 and a cylinder 13 . The inner space of the housing surrounded by the top cover 11 , the bottom cover 12 and the cylinder 13 is divided into three chambers by the first sealant layer 14 and the second sealant layer 15 . The structure of this part is basically the same as that of the plasma separator in Fig. 1, and for the sake of saving, details are not described here.

本实施例中,壳体1内部的三个腔室从上到下依次为入口缓冲腔16、血液净化腔17及出口缓冲腔18。在入口缓冲腔16的壁部设有血液入口161,在出口缓冲腔18的壁部设有血液出口181,在血液净化腔17的壁部设有二个出口171、172,其中出口172可作为血浆出口,另一个出口171可用于安装检测用的仪表。 In this embodiment, the three chambers inside the housing 1 are an inlet buffer chamber 16 , a blood purification chamber 17 and an outlet buffer chamber 18 from top to bottom. The wall of the inlet buffer chamber 16 is provided with a blood inlet 161, the wall of the outlet buffer chamber 18 is provided with a blood outlet 181, and the wall of the blood purification chamber 17 is provided with two outlets 171, 172, wherein the outlet 172 can be used as Plasma outlet, another outlet 171 can be used to install the instrument used for detection.

由多根空心纤维膜21和纤维状吸附剂31相互平行排列并均匀混合后形成的纤维束平行于壳体1的轴向安装在血液净化腔中。在血浆分离吸附器的横截方向上,空心纤维膜21与纤维状吸附剂31呈均匀分布。在安装固定后,对每根空心纤维膜21而言,均是一端穿过密封胶层一与入口缓冲腔161相连通,另一端穿过密封胶层二与血液出口缓冲腔171相连通。 A fiber bundle formed by a plurality of hollow fiber membranes 21 and fibrous adsorbent 31 arranged parallel to each other and uniformly mixed is installed in the blood purification chamber parallel to the axial direction of the casing 1 . In the transverse direction of the plasma separation adsorber, the hollow fiber membrane 21 and the fibrous adsorbent 31 are evenly distributed. After being installed and fixed, for each hollow fiber membrane 21 , one end passes through the sealant layer one to communicate with the inlet buffer chamber 161 , and the other end passes through the sealant layer two to communicate with the blood outlet buffer chamber 171 .

本实施例中,壳体1的内径约为44mm,空心纤维膜21选择外径500μm、内径为300μm的血浆分离用聚醚砜空心纤维膜,数量为2210根,长度约为240mm。纤维状吸附剂31是以聚苯乙烯-聚丙烯共混材质的海岛型纤维作为载体,表面接枝羧基和磺酸基的纤维状LDL吸附剂,有效长度约为240mm,直径为100μm,数量为53000根,重约36 g。 In this embodiment, the inner diameter of the housing 1 is about 44 mm, and the hollow fiber membranes 21 are polyethersulfone hollow fiber membranes for plasma separation with an outer diameter of 500 μm and an inner diameter of 300 μm, the number is 2210, and the length is about 240 mm. The fibrous adsorbent 31 is a fibrous LDL adsorbent with sea-island fibers made of polystyrene-polypropylene blended material as a carrier, and carboxyl groups and sulfonic acid groups grafted on the surface. The effective length is about 240 mm, the diameter is 100 μm, and the number is 53,000 pieces, weighing about 36 g.

本实施例血浆分离吸附器A在装配过程中,可先将空心纤维膜21和纤维状吸附剂31均匀混合形成纤维束,然后可参照现有技术中的血浆分离器的生产方法,通过聚氨酯密封胶浇注将纤维束固定在壳体1中,经过切胶处理后形成密封胶层一14和密封胶层二15,得到血浆分离吸附器。 In the assembly process of the plasma separation adsorber A of this embodiment, the hollow fiber membrane 21 and the fibrous adsorbent 31 can be evenly mixed to form a fiber bundle, and then the plasma separator can be sealed by polyurethane according to the production method of the plasma separator in the prior art. Glue casting fixes the fiber bundles in the housing 1, and after glue cutting, a sealant layer 1 14 and a sealant layer 2 15 are formed to obtain a plasma separation adsorber.

图4是使用本发明血浆分离吸附器A进行血液分离吸附的流程示意图。结合参考图2和图3,使用时,从患者体内引出的血液沿箭头方向流动,先经血泵100,从血浆分离吸附器A的血液入口161进入入口缓冲腔16内,然后进入空心纤维膜21。血液中的血浆穿过空心纤维膜21的膜壁,从全血中分离出来,进入血液净化腔17内。在血液净化腔17内,血浆与纤维状吸附剂31相接触,其中的致病物质被纤维状吸附剂31所吸附,血浆得以净化。经纤维状吸附剂31净化处理后血浆从血浆出口172排出后,通过血泵300,流入静脉壶500。浓缩后的血液从空心纤维膜中进入出口缓冲腔18,经血液出口181流出,亦流入静脉壶500,并在静脉壶500中与血浆混合,然后重新输回人体。 Fig. 4 is a schematic flow chart of blood separation and adsorption using the plasma separation adsorber A of the present invention. Referring to Fig. 2 and Fig. 3 together, when in use, the blood drawn from the patient flows in the direction of the arrow, first passes through the blood pump 100, enters the inlet buffer cavity 16 from the blood inlet 161 of the plasma separation adsorber A, and then enters the hollow fiber membrane 21 . Plasma in the blood passes through the membrane wall of the hollow fiber membrane 21 , is separated from the whole blood, and enters the blood purification chamber 17 . In the blood purification chamber 17, the plasma is in contact with the fibrous adsorbent 31, the pathogenic substances therein are adsorbed by the fibrous adsorbent 31, and the plasma is purified. After being purified by the fibrous adsorbent 31 , the plasma is discharged from the plasma outlet 172 , passes through the blood pump 300 , and flows into the venous pot 500 . The concentrated blood enters the outlet buffer cavity 18 from the hollow fiber membrane, flows out through the blood outlet 181, and also flows into the venous pot 500, where it is mixed with plasma and then reinfused back into the human body.

实施例2Example 2

本实施例与实施例1的结构基本相同,不同之处仅在于纤维状吸附剂不同,本实施例中是在纤维状载体上固载色氨酸后得到纤维状免疫吸附剂。 The structure of this example is basically the same as that of Example 1, except that the fibrous adsorbent is different. In this example, the fibrous immunosorbent is obtained after immobilizing tryptophan on the fibrous carrier.

本发明的技术构思并不仅限于上述实施例,还可以依据本发明的构思得到许多不同的具体方案,此等微小改变以及等效变换均应包含在权利要求所述范围之内。 The technical concept of the present invention is not limited to the above-mentioned embodiments, and many different specific solutions can be obtained according to the concept of the present invention, and such minor changes and equivalent transformations should be included within the scope of the claims.

Claims (7)

1. separating plasma adsorber, is characterized in that: comprising:
Housing, inside is provided with entrance cushion chamber, outlet cushion chamber and blood purification chamber, is provided with blood entrance in the wall portion of described entrance cushion chamber, is provided with blood outlet in the wall portion of described outlet cushion chamber, is provided with blood plasma outlet in the wall portion in described blood purification chamber;
At least one hollow-fiber film, is arranged in described blood purification chamber, and wherein the two ends of every hollow-fiber film are connected with described entrance cushion chamber and described outlet cushion chamber respectively;
At least one Fibriform adsorbents, is arranged in described blood purification chamber;
Described Fibriform adsorbents and described hollow-fiber film are and mix homogeneously shape at described blood purification intracavity.
2. separating plasma adsorber according to claim 1, is characterized in that:
The specific surface area of described Fibriform adsorbents is at 0.05-100m 2between/g.
3. separating plasma adsorber according to claim 1, is characterized in that:
The surface area of described hollow-fiber film is at 0.05-0.8m 2.
4. separating plasma adsorber according to claim 1, is characterized in that:
The sectional area sum of described Fibriform adsorbents and described hollow-fiber film is 0.1-0.65 with the ratio of the sectional area of described housing.
5. separating plasma adsorber according to claim 1, is characterized in that:
Described hollow-fiber film and described Fibriform adsorbents are arranged in parallel at described blood purification intracavity.
6. separating plasma adsorber according to claim 1, is characterized in that:
Described hollow-fiber film and described Fibriform adsorbents are in the cross arrangement of described blood purification intracavity.
7. according to the separating plasma adsorber described in claim 1 to 6 any one, it is characterized in that:
Described Fibriform adsorbents is the Fibriform adsorbents taking islands-in-sea type fibre as carrier.
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