TW200306349A - The cell culture method using a porous membrane - Google Patents
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200306349 五、發明說明(1) 一 一、 【發明所屬之技術領域】 本發明與細胞培養技術有關。詳言之,特別與在再生 醫療等領域有用之使用多孔膜為細胞增殖時之立足點之名 胞培養技術有關。 _ ^ 二、 【先前技術】 細胞培養技術為利用被移植於培養哭旦之w — μ 〃上 货时… < 既疋培蚕處 所之細胞’依據該細胞之趨化性’將細胞緩緩移動至i'周 邊區域而進行增殖之性質之技術。 〃 ^200306349 V. Description of the invention (1) 1 1. [Technical field to which the invention belongs] The present invention relates to cell culture technology. Specifically, it is particularly related to the cell culture technology, which is useful in the fields of regenerative medicine and the like, when using porous membranes as a foothold in cell proliferation. _ ^ 2. [Previous technology] Cell culture technology is to use the w-μ 被 which is transplanted to culture crying when the goods are delivered ... < The cells of the silkworm premises are 'slowly slowed down according to the chemotaxis of the cells' A technique that moves to the area around i 'to perform proliferation. 〃 ^
細胞增殖依賴細胞之移動性甚大,故最初被移入 胞如不能確實緊貼、固定在培養處所,則不能巧妙的: 細胞之移動性,而無法進行旺盛的細胞增殖。因此,1 細胞之立足點(scaffold),為細胞培養技術之一重要保 題。 坏1 在此,專利文獻1提示不愛西各与处 一 而要乳軋供給裝置,而铢私 經常且充分供給細胞代謝必要笺 月匕夠 戈之虱軋寺虱體,益細晌、、亡 染,運送簡便,且容器之至少_ # Α ώ、# γ ω ‘…、、田胞/可 邻刀由透氣性塑膠材料形 先前之細胞培養,通常使 等器具進行,其後研發塑膠製 實施親水處理,或以膠原蛋白 或聚離胺酸等實施覆蓋處理, 細胞培養效率,並增加培養細 如此,於先前之細胞培養 尚移入細胞對培養處所表面之 根據此想法,研發各種培養專 用玻璃製之皿、碟、三角瓶 培養器具,並再對器具表面 或纖維黏連蛋白等細胞間質 使細胞更容易附著,而提升 胞種類。 技術,其改進要點專注於提 附著性以確保其立足點,而 用器具。Cell proliferation depends on the mobility of the cells. Therefore, if the cells are initially moved in, they cannot be cleverly fixed in the culture place. They cannot be clever: the mobility of the cells cannot be used for vigorous cell proliferation. Therefore, the scaffold of 1 cell is an important guarantee for cell culture technology. Bad 1 Here, Patent Document 1 suggests that a milk supply device is needed instead of the West, and that the supply of cell metabolism is often and adequately necessary for the cell metabolism. Dyeing, easy transportation, and at least the container _ # Αώ, # γ ω '... ,, field cells / knockable knives are made of air-permeable plastic materials, which are previously cultured in cells, and are usually performed by instruments, and then developed by plastics. Hydrophilic treatment, or covering treatment with collagen or polyamic acid, etc., cell culture efficiency, and increase the culture. In the previous cell culture, the cells were moved to the surface of the culture place. Based on this idea, various glass special culture systems were developed. Dish, dish, Erlenmeyer flask culture equipment, and then the surface of the equipment or intercellular substance such as fibronectin makes cells more easily attached, and enhances the cell type. Technology, the main points of its improvement focus on improving adhesion to ensure its foothold, and using appliances.
200306349 五、發明說明(2) 成之細胞培養用容器。 專利文獻1 ·日本專利特開平i丨—〇 2 8 〇 8 3號。 三、【發明内容】 然而,生體内之細胞,其周圍被細胞及細胞間質所包 圍,通常在細胞全體表面進行營養補給、舊廢物排出、信 號傳達等。 ° 亦即,在生體内環境,對細胞增殖之方向幾無物理障 礙,但在生體外進行之先前細胞培養,在物質完全不能移 動之玻璃製或塑膠製培養器具之硬質表面上進行細胞培 養,因此有對細胞增痩之方向或細胞增殖之形態必然加以 限制之技術性課題。 因此,本發明使用可功用為細胞增殖時之立足點,且 物質可能移動之「多孔膜」,提供能夠簡便實現高密度細 胞培養之細胞培養方法為主要目的。 為解決上述技術性課題,首先,本發明提供設法以浸 潰於培養基之多孔膜進行細胞培養之細胞培養方法 於本發明可能採用之多孔膜,廣汎包含具備均勻微細 孔’並具備透氣性及物質通過功能(過濾功能)之膜體,不200306349 V. Description of the invention (2) Container for cell culture. Patent Document 1 Japanese Patent Laid-Open Publication No. Hei 08-083. 3. [Summary of the Invention] However, the cells in the living body are surrounded by cells and interstitial cells. Usually, the entire surface of the cells is supplemented with nutrients, discharged from old wastes, and transmitted signals. ° That is, in the living body environment, there is almost no physical obstacle to the direction of cell proliferation, but the previous cell culture performed outside the living body, the cell culture is performed on the hard surface of glass or plastic culture equipment that cannot move material at all Therefore, there are technical issues that necessarily limit the direction of cell proliferation or the form of cell proliferation. Therefore, the present invention uses a "porous membrane" that can function as a foothold during cell proliferation and can move materials, and provides a cell culture method capable of easily realizing high-density cell culture. In order to solve the above technical problems, first, the present invention provides a cell culture method that seeks to perform cell culture with a porous membrane immersed in a culture medium. The porous membrane that may be used in the present invention includes a wide range of porous membranes with uniform and fine pores. Membrane body for substance passing function (filter function), not
:,義解釋。「多孔膜」之代表例,可舉例如通常稱為過 履膜(memb]:ane filter)之高分子合成膜。 因在多孔膜形 盛。又與在玻 時’細胞增殖 細胞如同在生 依據使用多孔膜之上述細胞培養方法, 成堅固立足點,故促進細胞移動性而增殖旺 ㈤製或塑膠製培養器具表面之細胞培養比較 方向性之限制緩和,細胞容易重疊。亦即,:, Meaning explained. A representative example of the "porous membrane" is a polymer synthetic membrane generally called a membrane: an ane filter. Because in the porous membrane shape Sheng. Compared with the above-mentioned cell culture method in which cell proliferation is based on the use of porous membranes in glass, it has a strong foothold, so it promotes cell mobility and proliferates cell culture on the surface of culture equipment made of plastic or plastic. Restriction eases and cells easily overlap. that is,
200306349 五、發明說明(3) 體内環境,能夠立體增 增大,可增加細胞之膠 透氣性外亦具備物質通 其次,於本發明, 設法重疊使用多數之多 孔膜間形成逢隙狀態, 時,能夠確保在多層化 行物質(營養、舊廢物) 細胞培養條件,成為適 依據此多孔膜多層 能。亦即,可提供細胞 膜之使用牧數,而可能 質生產量之優點。又亦 培養基採樣等之培養哭、 (Hollow f iber )培養法 養法,乃捆紮空心纖維 在纖維表面或進入續# 特徵。 其次,於本發明, 面,由其反面以負墨口及 基流’設法'一面由上述 產生之舊廢物一面進行 又於此構成之細胞 〜1.0/zm範園特 殖之結 原蛋白 過性, 設法層 孔膜單 再設法 各多孔 之自由 合細胞 化方法 培養用 控制細 可能設 具,可 所無之 製成管 間增殖 果,每 等蛋白 適合細 疊使用 體。尤 使該多 膜上培 移動及 高密度 ,細胞 生物反 胞密度 計可能 獲得現 優點。 柱,在 ,而培 單位面 質生產 胞之高 上述多 其,以 孔膜層 養之細 氣體之 培養之 高密度 應器。 ,並可 觀察多 為主流 又所謂 其中培 養液連 f之細胞密度 ί。多孔《除 费度培養。 孔臈。亦即, 適宜方法在多 疊(多層化) 胞週園容易進 供給或交換等 方法。 培養成為可 Φ 又依單位多孔 預測計算蛋白 孔膜上細胞或 之空心纖維式 空心纖維式培 養細胞,細胞 續性迴流為其 k供附著細胞於上述多孔膜之一 弓丨或由細胞增殖面加壓而形成培養 多孔膜之細胞增殖面去除上述細胞 細胞培養之細胞培養方法。 培養方法,多孔膜微細孔之直徑以 別適合。其理由為小於〇 ·丨# m時, 〇200306349 V. Description of the invention (3) The internal environment can be increased three-dimensionally, which can increase the permeability of the gel of cells. It also has a second material. In the present invention, it is managed to overlap and use a majority of porous membranes to form a gap state. It can ensure that cell culture conditions (nutrient, old waste) in multi-layered cell culture conditions become suitable for multi-layered energy based on this porous membrane. That is, it can provide the advantage of using cell membranes, and possibly the quality of production. In addition, the culture method of culture medium sampling (Hollow fiber) culture method is to bundle hollow fibers on the fiber surface or enter the continuation # feature. Secondly, in the present invention, from the opposite side, the negative ink port and the base stream are used to 'try' while the old waste generated above is carried out and the cells formed there are ~ 1.0 / zm. Try to layer the pore membrane and then try to use the various porous free synthesizing methods for cultivation. The control device may be used to make interstitial proliferation fruits, and each protein is suitable for thin stacks. Especially with the multi-membrane culture and high density, the cell biological densitometer may obtain the current advantages. Columns, while the culture unit per unit of production is as high as the above, and the high-density reactor is cultivated with a fine gas cultured in a porous membrane layer. It can be observed that most of the so-called cell density of culture medium and f. Porous "except costly culture. Kong Yan. That is, a suitable method is easy to supply or exchange in a multi-layered (multi-layered) cell garden. The culture becomes a hollow fiber-type hollow fiber type culture cell that can be calculated on the basis of the prediction of the unit porosity of the protein, and the cells continue to flow back to allow them to attach cells to one of the above porous membranes or add from the cell proliferation surface The cell culture method for removing the above-mentioned cell cell culture by pressing the cell proliferation surface of the culture porous membrane. For the culture method, the diameter of the micropores of the porous membrane is not suitable. The reason is that when it is less than 〇 ##, 〇
第7頁 200306349 五、發明說明(4)Page 7 200306349 V. Description of the invention (4)
如不提鬲負壓吸引或加壓時之壓力,則較難形成通過夕 膜之適當培養基流,故需要一定之高壓條件,但因施力古 壓致使培養細胞引起損傷故不適合’而另一方面,如大= 時,產生之蛋白質與舊廢物一起被去除。細胞產生 之蛋白質,與同樣產生之胜肽及蛋白多醣等結合而表面分 子量變大,故1 · 〇 /z m以下之孔徑被阻塞而難以通過。 刀 於此細胞培養 用該多孔膜具有之 尿酸、過氧化脂質 反向對面,介微細 舊廢物。其結果細 孔膜孔控等,有控 與本發明有關 進行細胞增殖,有 技術,即組合細胞 内外再生(再構築) 四、【實施方式】 為驗註與本發 下之實驗1〜5。 <實驗1 > 方法,導 過濾功能 等舊廢物 孔通過, 胞壽命延 制去除物 之細胞培 用於廣汎 、細胞立 組織或臟 入培養 ,將細 ,由多 而可能 長,容 質之優 養方法 生化學 足點、 器之技 基於多 跑產生 孔膜之 由細胞 易連續 點。 ,能夠 領域, 細胞增 術,具 之低分子尿素, 細胞增殖面向4 增殖面去除上土 培養。又選擇^ 高密度且連續七 尤其於再生醫邊 殖因子,在生骨 有技術性意義。Without mentioning the pressure during suction or pressurization with negative pressure, it is more difficult to form a proper medium flow through the membrane, so a certain high pressure condition is required, but it is not suitable because of the damage caused by the application of ancient pressure to the cultured cells. In aspects, such as large =, the produced protein is removed along with the old waste. The protein produced by the cell is bound to the peptides and proteoglycans produced by the same, and the amount of surface molecules becomes large. Therefore, the pore diameter below 1 · / z m is blocked and difficult to pass. For this cell culture, the porous membrane has the uric acid and lipid peroxides opposite to each other, and the fine old waste is introduced. As a result, the pore membrane and pore control are related to the present invention. For cell proliferation, there is a technique, which is to combine the regeneration inside and outside the cell (reconstruction). 4. [Embodiment] For the test and experiment 1 ~ 5 of this issue. < Experiment 1 > Method, the passage of old waste wells such as the filtration function, and cell culture with extended cell life removal are used for extensive, cell standing tissue or dirty culture. The best method of biochemical biochemical foot and organ technology is based on multiple running to produce a continuous membrane of the cell membrane. It can be used in the field of cell proliferation, with low-molecular urea, and the cell proliferation surface is removed from the 4 proliferation surface to remove the soil culture. Also choose ^ high-density and continuous seven, especially the regenerative medicine collateral factor, has technical significance in bone formation.
明有關之細胞培養方法之效果,進行Clarify the effects of the relevant cell culture methods,
、 •、丨1湖肥儿疋點L比較塑 導致蛋土質生產量之差異而進行實驗;。 於貫驗1之蛋白質定量,將回 孔微量板之孔井中,加等量 之培養上清液放可馬斯蛋白質檢測試劑SExperiments were performed on the comparison of the fertilization point L of the lake fertilization, which caused differences in egg soil quality. For the protein quantification of Test 1, add the same amount of culture supernatant to the wells of the microtiter plate and place the Coomassie protein detection reagent S.
200306349 五、發明說明(5) (Coomassie Protein Assay Reagent Kit 、PIERCE 製 品),以布雷德福(Bradford)法進行。對照使用BSA (Bovine Serum Albumin、牛血清蛋白)。所得蛋白質以 SDS — PAGE(硫酸十二酯鈉-聚丙烯醯胺凝膠電泳)及使用抗 膠原蛋白抗體之免疫點潰法(immunob lot ting)定性分析, 確認此蛋白質大部分為膠原蛋白。 (比較例1 ) 接種人初級纖維芽細胞於φ 6 0匪塑膠製培養皿(含1 〇 % 牛胎兒血清(以下簡寫為rFBS」)之DMEM、日本製藥股份 有限公司製品)’在3 7 °C培養器中培養。亦即不使用多孔 膜進行細胞培養。到達(細胞)融合(c 〇 n f 1 u e n t )狀態時, 用及引為吸引去除培養上清液,將細胞培養基更換為無血 清培養基(nonFBS-DMEM)。每週回收如上述之培養上清 液,進行蛋白質定量。此時細胞培養基每次均更換為 清培養基,並均添加抗生素。又「DEME」#Dulbe(;^〇,;200306349 V. Description of the invention (5) (Coomassie Protein Assay Reagent Kit, PIERCE product), carried out by Bradford method. As a control, BSA (Bovine Serum Albumin, bovine serum albumin) was used. The obtained protein was qualitatively analyzed by SDS-PAGE (sodium lauryl sulfate-polyacrylamide gel electrophoresis) and immunooblot ting method using an anti-collagen antibody, and it was confirmed that most of the protein was collagen. (Comparative Example 1) Inoculation of human primary fibroblasts in a φ 60-band plastic petri dish (containing 10% bovine fetal serum (hereinafter abbreviated as rFBS) in DMEM, Japan Pharmaceutical Co., Ltd.) at 3 7 ° C incubator. That is, cell culture is performed without using a porous membrane. When reaching the (cell) confluent (conn f 1 u e n t) state, the culture supernatant was removed by suction, and the cell culture medium was replaced with a non-blood culture medium (nonFBS-DMEM). The culture supernatant as described above was recovered every week for protein quantification. At this time, the cell culture medium was replaced with a clear medium every time, and antibiotics were added. Also "DEME" #Dulbe (; ^ 〇 ,;
Modefied Eagle Medium 之一般簡稱。 (實施例1〜4 ) f亩用過慮膜(以下簡寫為「MF」)之培養為預先固定評 (直住13_或47_)於M〇cm培養皿底部,與上述比較例工 以下,ΓΛ接:V刀級原發纖維芽細胞(含1 °%牛胎兒血 =口mi I之_、曰本製藥股份有限公司 二I广立 養器中培養。接種之上述細胞在MOcm 支口養皿底部均勻附著、增殖時, 合狀態,A可推讀上之細胞 :=底°卩細胞為融 I邳為融合狀態。此培養後之Modefied Eagle Medium (Examples 1 to 4) The cultivation of f acres of used membranes (hereinafter abbreviated as "MF") was fixed in advance (straight 13_ or 47_) at the bottom of the Mocm petri dish, which is the same as the above comparative example, ΓΛ Connection: V knife-grade primary fibroblasts (containing 1 °% bovine fetal blood = mouth mi I, _, Yueben Pharmaceutical Co., Ltd. II I wide stand, cultured. The inoculated cells are cultured in MOcm oral culture dishes When the bottom is uniformly attached and proliferated, the confluent state, A can be deduced on the cells: = Bottom ° 为 cells are fused I 邳 fused state. After this culture
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更換為無血清培養基。並每 MF移至新的φ 1 〇cm培養皿後 5曰更換1次無血清培養基。 在細胞培養用培養皿(培養面積:2〇· 〇cm2)中 級原發纖維芽細胞培養至融合狀態後,更換為無血清培刀 基,分別測定比較該無血清培養基中之蛋白質量與放入 著細胞之直徑47onnMF(培養面積:173cm2)無血清培寸 中之蛋白質量。 土 此時MF之材質使用A〜D之4種。盯種類以抓―A、肿一 B、MF-C、MF-D簡寫。MF-A(實施例1)為親水性聚四氟乙 (孔徑·· 〇· 5 //m),MF-B(實施例2)為親水性聚亞乙烯二氟 (孔徑1· 45 //m),MF-C(實施例3)為無親水處理聚四氟乙 烯(孔徑:0· 5 #m),MF~D(實施例4)為聚碳酸酯(孔徑: 0.4/zm)。其結果示如下表1。 【表1】— 冗"養器具- 培養期間7?^ 全蛋白Ϊ量Ug> 蛋白質量/面積/曰^ (Mg/cm2/曰;μ 比較例 培養皿P 7^ 2L:! 0.15. 實施例 MF 二 Α» 405^ 4 7^ 實施例厶 MF 二Bo 5^ 285一 3·3ρ 實施例1 MF 二Ο 5,^ 63, 0.73。 實施例‘ MF - D 一 5^· —60。 0.69,; 由上示表1得知,在MF上進行細胞培養時,產生之蛋 白質量增加,每單位面積蛋白質生產量亦增加故每單位面 積細胞密度增多。尤其使用MF-A 、MF-B為多孔膜時,與 使用培養皿比車父’蛋白質生產量顯然增多,能夠以更高密 度培養細胞。亦即’親水性多孔膜之親水性聚四氟乙烯、Replace with serum-free medium. And every MF was moved to a new φ10 cm petri dish and the serum-free medium was changed once every 5 days. After the medium-grade primary fibroblasts were cultured to a confluent state in a culture dish for cell culture (culture area: 2.0 cm2), they were replaced with serum-free culturing substrates, and the quality of the protein in the serum-free medium was measured and compared. The diameter of the cells was 47onnMF (culture area: 173cm2) and the protein mass in serum-free culture. Soil At this time, four types of materials A to D are used. Stare at the type to abbreviate ―A, swollen B, MF-C, MF-D. MF-A (Example 1) is a hydrophilic polytetrafluoroethylene (pore diameter ···· 5 // m), and MF-B (Example 2) is a hydrophilic polyvinylidene difluoride (pore diameter 1.45 // m), MF-C (Example 3) is a non-hydrophilic polytetrafluoroethylene (pore size: 0.5 #m), and MF to D (Example 4) is polycarbonate (pore size: 0.4 / zm). The results are shown in Table 1 below. [Table 1] — redundant " cultivation equipment-7? ^ Total protein amount Ug during culture> protein mass / area / say ^ (Mg / cm2 / say; μ Comparative Example Petri dish P 7 ^ 2L :! 0.15. Implementation Example MF II A »405 ^ 4 7 ^ Example MF MF Bo 5 ^ 285-3 · 3ρ Example 1 MF 205 5, ^ 63, 0.73. Example 'MF-D-5 ^ -60 — 0.69 From Table 1 shown above, it is known that when cell culture is performed on MF, the amount of protein produced increases, and the protein production per unit area also increases, so the cell density per unit area increases. In particular, the use of MF-A and MF-B is When using a porous membrane, compared with the use of a petri dish, the production of protein is significantly increased, and cells can be cultured at a higher density. That is, the hydrophilic polytetrafluoroethylene of the hydrophilic porous membrane,
200306349 五、發明說明(7) 親水性聚亞乙烯二氟當做多孔膜材料特別適合。 <實驗2 > 為驗^正不同細胞立足點(比較塑膠製培養JDI與過濾膜) 導致細胞壽命之差異而進行實驗2。 u字,初、、及原發纖維芽細胞以塑膠製培養皿(F a 1 c ο η公 1 ^ b養皿)培養時當做『比較例2』,而在過濾膜上培養 士 :&例5』。兩者比較細胞由底部剝離至浮游之 間立、,此日守在細胞融合狀態後以無血清培養’每隔1週留 ΪΛ2} 血清200306349 V. Description of the invention (7) Hydrophilic polyvinylidene difluoride is particularly suitable as a porous membrane material. < Experiment 2 > Experiment 2 was performed to verify that different cell footholds (comparing plastic culture JDI with filter membranes) caused differences in cell life. U-shaped, primary, and primary fibroblasts are cultured in plastic petri dishes (F a 1 c ο η male 1 ^ b petri dishes) as "Comparative Example 2", and cultured on a filter membrane: & Example 5 ”. Comparing the two, the cells were separated from the bottom to the planktonic position. After that, the cells were kept in a confluent state and cultured in serum-free.
3 0%培養上清液而更換培養基。實驗2之結果示如表2。 培養 ia > 狀態p 70# 7〇曰後薄片狀細胞由底面剥離。 142. 「薄片狀細胞未由MF剥離^ 細胞以MF L之細胞培 得知使用MF之細胞培養,適合 為立足點而增飱辟成 ^ ^ ^ ° 、 .r . .. 7日殖旺盛,其細胞哥命較使用培養 養(比較例2)較長。亦即 細胞之連續培養。30% of the culture supernatant was replaced with medium. The results of Experiment 2 are shown in Table 2. After culture ia > state p 70 # 70, the lamellar cells were detached from the bottom surface. 142. "Sheet cells have not been peeled off by MF cells. Cell culture using MF L has shown that cell culture using MF is suitable for increasing footholds to ^ ^ ^ °, .r... Its cell life is longer than that of culture (Comparative Example 2), that is, continuous culture of cells.
在此,管, A , 、π 之〜果由一般初級細胞培養之壽命觀 維芽1月可視為異常。但如考慮到在生體内皮膚纖 佟杜、、、^以〜6年週期進行新陳代謝,則實施例5之培養 條件,可視為近似生體内環境。 結,又此結ί,應視為細胞不是以融合狀態停止細胞增 而以重豐化繼續細胞增殖較無矛盾。$時,聯結成薄 片狀、、、田胞未由MF剝離,故雖然各個細胞死亡,但如同在生Here, the tube, A, and π are regarded as abnormal from the perspective of life expectancy of ordinary primary cell culture in January. However, in consideration of the metabolism of the skin fibers in the living body at a period of ~ 6 years, the culture conditions of Example 5 can be regarded as approximate the living body environment. This, again, should be considered that the cells do not stop cell proliferation in a fused state and continue cell proliferation with heavy abundance. When it is connected, the cells are connected into a thin sheet, and the field cells are not stripped by MF. Therefore, although each cell died, it was as if it were living.
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五、發明說明(8) 體内,新的細胞相繼增殖,以填充發生細胞死亡之空間。 將MF配置成多層化,似可能以高密度培養細胞:進行 高密度培養之系統,稱為動物細胞培養用生物反應器(反 應器),動物細胞由於其增殖形態分成兩類,故上述反應 器亦一般大別為2種。5. Description of the invention (8) In vivo, new cells proliferate one after another to fill the space where cell death occurs. MF is configured in multiple layers, and it is possible to culture cells at high density: a system for high density culture is called a bioreactor (reactor) for animal cell culture. Animal cells are divided into two types due to their proliferation patterns, so the above reactor There are generally two types.
首先,細胞有浮游在培養基中可增殖之浮游細胞與不 附著立足點則不能增殖之附著細胞。反應器須要為操作上 述附著細胞設法,故研發增加附著面積之水平滾筒式 (Roller bottle),或附著細胞於微粒載體(Microcar r i e r ) 表 面後將 該球粒 懸浮反 應器中 之方法 (懸 浮擾掉 法、氣升式、細胞浮升式等)。再者,於高密度培養則研 發空心纖維式(Hoi low fiber)及陶瓷基質式(Ceramic matrix) 〇 如此,細胞密度雖然有飛躍的增加,但亦發生不能為 擴大細胞培養或監測細胞壤境而進行採樣之問題。此監測 在管理細胞生產物而使細胞環境均勻時為必須之方法。 <實驗3 > 為驗証在MF上培養之細胞形態而進行「實驗3」。 將人原發纖維芽細胞,在M F上培養1〜2個月後,用立 體顯微鏡觀察染色細胞。其結果,觀察到細胞重疊化而其 一部份表現立體構造。圖1表示上述顯微鏡照像。又於圖1 所示照片,其臺盼藍(or錐蟲藍、trypan b 1 ue )染色較深 部分,為細胞密度較高部分。 使用一般塑膠培養器具之細胞培養方法,因其器具表First, the cells have planktonic cells that can proliferate in the culture medium and adherent cells that cannot proliferate without a foothold. The reactor needs to work for the above-mentioned attachment cells, so a horizontal roller type (roller bottle) that increases the attachment area, or a method of suspending the pellets in the reactor after attaching the cells to the surface of a microcar rier (suspension suspension) Method, air lift, cell lift, etc.). In addition, in the high-density culture, the development of the hollow fiber (Hoi low fiber) and ceramic matrix (Ceramic matrix) 〇 In this way, although the cell density has increased dramatically, it also occurs that can not be used to expand cell culture or monitor cell soil environment Problems with sampling. This monitoring is necessary when managing cell production to homogenize the cell environment. < Experiment 3 > "Experiment 3" was performed to verify the morphology of cells cultured on MF. After human primary fibroblasts were cultured on MF for 1 to 2 months, the stained cells were observed with a stereo microscope. As a result, overlapping of cells was observed, and a part of them showed a three-dimensional structure. FIG. 1 shows the above-mentioned microscope photograph. In the photo shown in Fig. 1, the trypan blue (or trypan blue, trypan b 1 ue) stains the darker part, which is the part with higher cell density. Cell culture methods using general plastic culture instruments
第12頁 200306349 五、發明說明(9) 面為硬質而非多孔質’故不能形成具有此種立體構造之細 胞,因此該立體性細胞增殖,可認為以MF為立足點時之一 大特徵。又MF多層化之結果,每單位面積之細胞數增加, 可維持蛋白質之高生產量(可由後述實驗4驗証)。照片中 顏色較深部分,表示細胞密度較高。 又於上述實施例,採用過濾膜(MF)為多孔膜,但不限 疋於此,在與本發明有關之細胞培養方法,至少具有均勻 微細孔之膜體,且適合細胞培養之多孔膜均可採用,如可 多層化則更適合採用。Page 12 200306349 V. Description of the invention (9) The surface is hard but not porous', so cells with this three-dimensional structure cannot be formed. Therefore, the proliferation of this three-dimensional cell can be considered as one of the major characteristics when MF is the foothold. As a result of multi-layered MF, the number of cells per unit area is increased, and a high protein production amount can be maintained (verified by Experiment 4 described later). Darker parts of the photo indicate higher cell density. In the above embodiment, the filtration membrane (MF) is used as a porous membrane, but it is not limited to this. In the cell culture method related to the present invention, the membrane body has at least a uniform fine pore membrane, and the porous membrane suitable for cell culture is uniform. Can be used, if it can be multi-layered, it is more suitable for use.
在此,根據圖2說明與本發明有關之細胞培養方法之 適合發展形態。圖2為簡單表示上述發展形態之概念圖。 於圖2,將細胞2附著於多孔膜1之一面1〇ι,由其另一 面之反面102用負壓吸引,形成通過多孔膜i之培養基流 F,而可設法一面由多孔膜}之細胞增殖面1〇1去除上述細 胞2產生之老舊廢物3,一面進行細胞培養。 又亦可採用由多孔膜1之細胞增殖面丨〇 i方加壓,使細 胞2產生之老舊廢物3,由細胞增殖面1〇1隨培養基流f向其 反面1 0 2流出,以去除之方法。Here, a suitable development form of the cell culture method related to the present invention will be described with reference to FIG. 2. FIG. 2 is a conceptual diagram briefly showing the above development form. In FIG. 2, the cell 2 is attached to one side 10m of the porous membrane 1, and the opposite side 102 of the other side is attracted with negative pressure to form a medium flow F through the porous membrane i. The proliferation surface 101 removes the old waste 3 produced by the cells 2 and performs cell culture. Alternatively, the cell proliferation surface of the porous membrane 1 can be pressurized to make the old waste 3 produced by the cell 2 flow from the cell proliferation surface 101 to the opposite surface 102 with the medium flow f to remove it. Method.
負壓吸引或加壓之方法,只要能夠形成符合本發明 目的程度之培養基4之流動(培養基流F)之方法, 細胞4 ’只將老舊廢物3向反面1〇2方去除之方法均可、 用’又此等方法亦適用於MF多声介眭—夕a 培養基流F。 夕層化¥,在多層化之MF形 又於圖2 元件符號21以模式表示 被移植細胞2在多The method of suction or pressurization by negative pressure may be a method of forming the flow of the culture medium 4 (medium flow F) that meets the purpose of the present invention, and the method of removing only the old waste 3 to the opposite side by 102 cells 4 Using these methods is also applicable to MF polyphonic media-Xi a medium flow F. Even layered ¥, in a multi-layered MF shape. Also shown in Figure 2 is the symbol 21 for the pattern.
200306349 五、發明說明(ίο) 孔膜1上進行立體增殖。 <實驗4〉 驗4 為驗証將多孔臈多層化時之細胞培養效果 而進行「實200306349 V. Description of the Invention (ίο) Three-dimensional proliferation is performed on the pore membrane 1. < Experiment 4> Experiment 4
首先二為使MF容易多们匕,製作具備可夾持固定直徑 4 7mm圓形薄膜狀MF用多數個突起部位之框架。此垂 使用框架’設計成當重疊該框架本身日寺,各二 相固定。重疊框架之結果,能夠以確保細間之=(空 間)狀態,將被各框架失持固定之評重疊(多層化)。 、其次,準備圓筒形容器以收容重疊之MF及固定該肝之 亡述框架’此圓筒形容器選用透氣性高之材質(聚甲基戊 烯或聚碳酸酯)。再者,此圓筒形容器之蓋子,亦選定透 氣性之上述材質。 (實驗4相關之比較例3及實施例6〜9 ) 首先’為附著細胞於MF上,將直徑47匪之MF(MF-A或 MF-B)+用白色凡士林固定於直徑6〇mm培養皿,接種人初級 纖維芽細胞(含1 〇%FBS之DMEM培養基),以37 °C培養器培 養。MF預先以1 cm間隔之十字形狀做成9個直徑〗min小孔,First, in order to make the MF easier, a frame having a large number of protrusions for holding and fixing a circular film-shaped MF with a diameter of 47 mm was produced. This vertical frame is designed so that when the frame itself is overlapped, the two phases are fixed. As a result of overlapping frames, it is possible to overlap (multi-layer) the evaluations that are fixed by the failure of each frame in order to ensure that the detail is equal to (space). Secondly, prepare a cylindrical container to house the overlapping MF and fix the liver's frame. This cylindrical container is made of a material with high air permeability (polymethylpentene or polycarbonate). In addition, the lid of this cylindrical container is also selected from the above-mentioned materials having air permeability. (Comparative Example 3 and Examples 6 to 9 related to Experiment 4) First, to attach cells to MF, a MF (MF-A or MF-B) with a diameter of 47 bands + fixed with white vaseline at 60 mm in diameter and cultured Dish, inoculated with human primary fibroblasts (DMEM medium containing 10% FBS), and cultured in a 37 ° C incubator. MF made 9 small holes with a diameter of 1 cm in a cross shape in advance,
田細胞增殖至此等小孔,即判定評上之細胞到達融合狀 恶:將此附著細胞之MF以凡士林直接固定於新的直徑6 0mm 培養皿者當做「比較例3」。 又將MF以每1牧固定於上述框架,放入上述圓筒形容 器。1枚MF者為「實施例6」,2枚MF者為「實施例7」,5 枚MF者為「實施例8」,6牧MF者為「實施例9」,。比較The proliferation of field cells to these small holes means that the evaluated cells have reached a confluent state. Evil: The MF of this attached cell was directly fixed to a new 60 mm diameter petri dish with Vaseline as "Comparative Example 3". The MF was fixed to the above frame at a time, and placed in the above-mentioned cylindrical container. One MF is "Example 6", two MFs are "Example 7", 5 MFs are "Example 8", and 6 MFs are "Example 9". Compare
200306349 五、發明說明(11) 例3及實施例6〜9分別以含10%FBS之DMEM培養基培養,1週 後洗清並更換為無血清(DMEM)培養基。其後之第10日測定 培養上清液中之蛋白質量。測定結果如下「表3」所示。 【表 有無框架# i枚數y 蛋白質量/面積(仁g/cm2> 比較例3· 無ρ 1(單層> 5.6^ 實施例& 有- 1(單層> 19.2= 實施例7。 有 2(多層> 19 4. 實施例心 有p 5(多層> 12.5, 實施例〜 有。 6(多層> 12.6·: 首先,比較上示「表3」之比較例3與實施例6之結 果,闡明使用框架在MF與容器底面間形成間隙(空間),提 升蛋白質之生產性。其原因可能為形成上述間隙,容易在 細胞週圍自由進行物質(營養、舊廢物)之移動或氣體之供 給或交換。 其次,如實施例6〜9所示,可知重疊固定MF之框架, 多層化MF時,較比較例3維持蛋白質之高生產性。亦即, 闡明多層化MF之構成亦有效。 枚MF時(實施例6)與2枚MF時(實施例7) 又 -------- V月,/ 议d双 MF時(實施例8)或6枚MF時(實施例9),約有35%程度之蛋白 質生產量差異。此表示能夠預估計算擴大生產或蛋白質總 生產量。 、〜 如上所述,於本發明,以MF為細胞立足點可能以高宓 度及良好效率進行細胞培養。再者,在腳與訂間形成二 之多層化,而非密接MF與MF之多層化,改善先前認為最有200306349 V. Description of the invention (11) Example 3 and Examples 6-9 were cultured in 10% FBS-containing DMEM medium, washed one week later and replaced with serum-free (DMEM) medium. The amount of protein in the culture supernatant was measured on the 10th day thereafter. The measurement results are shown in "Table 3" below. [表 有 有 FRAME # #number of y protein mass / area (ren g / cm2)> Comparative Example 3 · No ρ 1 (single layer) 5.6 ^ Example & yes-1 (single layer) 19.2 = Example 7 Yes 2 (multi-layer) 19 4. Examples are p 5 (multi-layer> 12.5, examples ~ yes. 6 (multi-layer) 12.6 ·: First, compare the comparative example 3 shown in Table 3 above with the implementation The result of Example 6 clarifies the use of the frame to form a gap (space) between the MF and the bottom surface of the container to improve the productivity of the protein. The reason may be that the above gap is formed, and it is easy to freely move materials (nutrition, old waste) around the cell or Supply or exchange of gas. Next, as shown in Examples 6 to 9, it can be seen that the frame of MF is superimposed and fixed. When multilayered MF is used, the protein is more productive than Comparative Example 3. That is, the structure of multilayered MF is also explained. Valid: When there are MFs (Embodiment 6) and when there are 2 MFs (Embodiment 7) and -------- V month, / when dual MFs (Embodiment 8) or 6 MFs (implementation) Example 9), there is a difference of approximately 35% in protein production. This means that it is possible to estimate and calculate the expanded production or the total protein production. As described above, in the present invention, using MF as the foothold of the cell may allow cell culture to be performed with a high degree of efficiency and good efficiency. Furthermore, a multi-layered structure is formed between the feet and the space, rather than a multi-layered structure that closely contacts MF and MF Improve what was previously considered the most
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效率之空心纖維式 MF枚數容易預估計 夠觀察MF上之細胞 <實驗5 > 培養法之缺點。亦 算蛋白質生產量, 或培養基採樣之培 即,根據附著細胞之 使擴大生產簡單。能 養器具亦容易設計。 =檢时收容MF之容器(圓筒形容器)之適合材質為目 的,貫施以下之「實驗5」。The efficiency of the hollow fiber type MF is easy to predict. It is possible to observe the cells on the MF < Experiment 5 > It can also be counted as the amount of protein produced, or culture medium sampling, that is, simple expansion of production based on adherent cells. Supporting appliances are also easy to design. = The suitable material of the container (cylindrical container) containing the MF during inspection is for the purpose of the following "Experiment 5".
準備3種材質之收容多層化MF用圓筒形容器。在各容 器中培養細胞,測定培養上清液中蛋白質含量,以探討細 1生產蛋白質時氣體交換性(透氣性)之有效性。容器之材 質使用〜聚丙烯(實施例丨〇 )、聚碳酸酯(實施例丨丨)、聚甲基 戊烯(實施例12)。另外再準備培養上清液中蛋白質含量^ 多之材f之圓筒形容器上部安裝具有氣體交換性(透氣性) ,過濾器以再提高氣體交換性之實施例(實施例丨3 )。又此 圓筒形谷器為旋轉蓋子關閉形式之高氣密性者,裝水倒轉 時亦不滲漏。 具體說明實驗5之方法,為附著細胞於MF上,將直# 4 7mm之MF(MF-A或MF-B)用白色凡士林固定於直徑6〇_培養Cylindrical containers for multi-layered MF were prepared in three materials. Cells were cultured in each container, and the protein content in the culture supernatant was measured to investigate the effectiveness of gas exchange (breathability) during protein production. As the material of the container, polypropylene (Example 丨 0), polycarbonate (Example 丨 丨), and polymethylpentene (Example 12) were used. In addition, an embodiment (Example 3) in which the upper part of the cylindrical container with a high protein content in the culture supernatant is provided with a gas exchange property (air permeability) and a filter to further improve the gas exchange property. In addition, the cylindrical trough is highly airtight in the form of a closed lid, and does not leak when the water is inverted. The method of Experiment 5 will be described in detail. To attach cells to MF, fix straight # 4 7mm MF (MF-A or MF-B) with white vaseline at a diameter of 60 °.
皿’接種人初級纖維芽細胞(含10%FBS2DMEM培養基),以 37 C培養斋培養。MF預先以1 cm間隔之十字形狀做成9個直 徑1 mm小孔,當細胞增殖至此等小孔,即判定肝上之細胞 到達融合狀態。將此附著細胞之MF固定於框架,收容於實 轭例1 0〜1 2之圓筒形容器,再放入附著細胞之微粒載體 1 · 5 g。培養1週後,充分去除含血清培養基,洗清並更換 為無血清培養基。其後之第1 4曰測定培養上清液中之蛋白The dish was inoculated with human primary fibroblasts (containing 10% FBS2DMEM medium) and cultured at 37 C. MF made nine small holes with a diameter of 1 mm in a cross shape with a 1 cm interval in advance. When the cells proliferated to these small holes, it was determined that the cells on the liver had reached a confluent state. The MF of this adherent cell was fixed to a frame, and it was stored in a cylindrical container of the actual yoke example 10 to 12 and then a particulate carrier 1 · 5 g of the adherent cell was placed. After 1 week of culture, the serum-containing medium was sufficiently removed, washed, and replaced with a serum-free medium. The following fourteenth: determination of protein in the culture supernatant
第16頁 200306349 五、發明說明(13) 質量。測定結果如下「表4」所示 容器之材質θ 培養基量(πύ> 蛋白質濃度(#g/ml$ 實施例1〇β 聚丙婦4 32.5^ ~~ 實施例1L· 聚碳酸酯ρ 他 36.5— 實施例12^ 聚甲基戊婦ρ 输 39.2^ ' 實施例13^ 聚!基在烯(附過濾器> 38.8, - ^ …一 p y丄✓月狀丁 之史白質濃度均南’尤其實施例12聚甲基戊婦製圓筒形容 器為最大(39.2// g/mi )。又於另外進行之材質試驗結果聚甲 基戊烯之透氣性最大。亦即,細胞之蛋白質生產性,與容钱 器之透氣性密接相關。 ^ 又比較實施例1 2與實施例1 3,只要是聚甲基戊烯之容 裔’再附加透氣性過濾器,蛋白質濃度無很大改變。由此 1果得知以透氣性高之聚甲基戊烯等材質形成圓筒形容器 ^ ’無須使用透氣性過濾器等以提高透氣性。 〆,由上述實驗5,收容多層化MF於透氣性高之聚曱基戊 稀製容器進行細胞培養,可實施高密度之細胞培養,確 馬度之蛋白質生產性。 [發明效果] /依據與本發明有關之細胞培養方法,細胞能夠在多孔讀 =形成堅固的立足點,因此促進細胞移動性而進行旺盛之 曰殖’減緩細胞增殖方向性之限制,並能重疊細胞,使細 胞之高密度培養成為可能。 又細胞之高密度培養成為可能之結果,能夠增加細胞Page 16 200306349 V. Description of the invention (13) Quality. The measurement results are as shown in "Table 4" below. The material of the container θ The amount of medium (πύ > Protein concentration (# g / ml $ Example 10) Polypropylene 4 32.5 ^ ~~ Example 1L · Polycarbonate β 36.5— Implementation Example 12 ^ Polymethylammonium chloride 39.2 ^ 'Example 13 ^ Poly! Based on alkenes (with filter > 38.8,-^… a py 丄The 12-polymethylpentyl cylindrical container is the largest (39.2 // g / mi). The results of the material test conducted separately are that the maximum permeability of polymethylpentene. That is, the protein productivity of cells, and The breathability of the money holder is closely related. ^ Compare Example 12 and Example 13 again, as long as it is a polymethylpentene-based container and add an air permeability filter, the protein concentration does not change much. Therefore 1 It was learned that a cylindrical container made of a material having high air permeability such as polymethylpentene was used to improve the air permeability. 〆 According to the above experiment 5, the multilayered MF is accommodated in a high air permeability. Polyfluorenyl dilute container for cell culture, can carry out high-density cell culture. [Productive effect] [Inventive effect] / According to the cell culture method related to the present invention, cells can form a strong foothold in porous readings, thus promoting cell mobility and vigorously colonizing, slowing cell proliferation. Limitation, and can overlap cells, making high-density culture of cells possible. Also, as a result of high-density culture of cells, it is possible to increase cells
—1 1丨,_ 第17頁 200306349 五、發明說明(14) 之膠原蛋白等蛋白質生產量,故可望成為再生醫療技術, 尤其使用增殖自體細胞所得自體組織之再生醫療基本技術 之細胞培養方法。 、、設法多層化使用上述多孔膜,使更高密度之細胞培養 成為可能,依單位多孔膜之使用牧數,有可能控制細胞密 度或計算蛋白質生產量,故極為方便。又亦有可能設計可 能觀察多孔膜上細胞或培養基採樣之培養器具之優點。—1 1 丨, _ Page 17 200306349 V. Description of the invention (14) The production of collagen and other proteins is expected to become a regenerative medical technology, especially a cell that uses the basic technology of regenerative medical treatment of autologous tissue obtained from the proliferation of autologous cells Training methods. It is very convenient to use the above-mentioned porous membrane in multiple layers to make higher density cell culture possible. Depending on the number of porous membranes used, it is possible to control the cell density or calculate the amount of protein produced, which is extremely convenient. It is also possible to design culture devices that can observe the sampling of cells or culture media on porous membranes.
附著細胞於多孔膜之一面,由其反面以負壓吸引或由 細胞增殖面加壓,以形成通過多孔膜之培養基流,設法去 除上述細胞產生之舊廢物,則可能由多孔膜之細胞捭 =上1效率確實去除由細胞產生之低分子尿素、尿‘、 行連舊廢物。其結果’細胞壽命延長,能夠確實進 質。、、、Λ。養。再者,選擇多孔膜孔徑等,可控制去除物 斗加如以多孔膜濃縮細胞自體分泌物、即自體作用吝斗 王理活性物哲 、, I生之 理活性物匕使低分子舊廢物通過多孔膜去除,則生 分泌物代二^給不須依賴牛胎兒血清(FBS),可用自體 增殖。θ ,,、添加無蛋白質培養液’即可維持進行細胞Cells are attached to one side of the porous membrane, and the opposite side is attracted by negative pressure or pressurized by the cell proliferation surface to form a medium flow through the porous membrane. If you try to remove the old waste generated by the cells, the cells of the porous membrane may be 捭 = The above efficiency does remove low-molecular urea, urine, and old waste produced by cells. As a result, the cell life is prolonged, and the cell can be surely improved. ,,, Λ. support. Furthermore, by selecting the pore size of the porous membrane, you can control the removal of the material, such as concentrating the cell's autocrine secretion with the porous membrane, that is, the autologous action of the active principle of the Douwangli, and the low-molecular active substance. The waste is removed through the porous membrane, and the raw secretion is replaced by bovine fetal serum (FBS), which can be used for autologous proliferation. θ ,, can be maintained by adding protein-free culture medium ’
第18頁 200306349 圖式簡單說明 五、【圖式簡單說明】 圖1為實驗3之培養細胞之立體顯微鏡放大照片。 圖2為簡單表示與本發明有關之細胞培養方法之適合 發展形態之概念圖。 元件符號說明: 5多孔膜 6細胞 7舊廢物 8培養基 F 培養基流 2 1 細胞立體增殖模式 1 0 1多孔膜1之細胞增殖面 102多孔膜1之101之反面Page 18 200306349 Simple illustration of the diagram V. [Simplified illustration of the diagram] FIG. 1 is an enlarged photo of a stereo microscope of the cultured cells of Experiment 3. FIG. Fig. 2 is a conceptual diagram briefly showing a suitable development form of a cell culture method related to the present invention. Explanation of component symbols: 5 porous membrane 6 cells 7 old waste 8 medium F medium flow 2 1 three-dimensional cell proliferation mode 1 0 1 cell proliferation surface of porous membrane 1 102 reverse side of 101 of porous membrane 1
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