TWI233943B - Method for forming scaffold - Google Patents
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- TWI233943B TWI233943B TW092136088A TW92136088A TWI233943B TW I233943 B TWI233943 B TW I233943B TW 092136088 A TW092136088 A TW 092136088A TW 92136088 A TW92136088 A TW 92136088A TW I233943 B TWI233943 B TW I233943B
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Abstract
Description
1233943 玖、發明說明: , 【發明所屬之技術領域】 本發明係有關於一種生物基材之形成方法,特別是 有關於一種於低溫條件下進行固定製程的生物基材形成 方法。 【先前技術】 組織工程是近年來蓬勃發展的領域之一,其著名的 應用方式之一係植入細胞於生物可降解春 (biodegradable )的材料内,待細胞生長形成具有功 能的新組織或器官的雛形後,再植入至人體内,組織工 私已成為治療器官功能短缺或組織壞死的熱門方法。關 於組織工程的研究,大致可分為三個部分:細胞 (cells )、具有生物相容性的基材(scaffolds,簡稱生 物基材)與刺激細胞表現出特定行為的訊號(signals ), 三者之間彼此影響並共同調節組織的分化與表現,其馨 中’生物基材在組織工程中所扮演的角色包括: 1 ·運送細胞或經過初步培養的組織至身體的特定部位, 避免所培養的細胞或組織過早遭到免疫作用或身體中 其他物理作用的破壞。 2 ·使新生成的組織或器官具有符合要求的立體型態,並 給予它們支持及提供保護。 · 13 1233943 3.刺激細胞或組織表現出特定的行為,例如在生物基材 表面塗布可產生訊號的物質以達到所需效果。 製造生物基材的方式一般可分為相分離法與非相分 離法别I疋|曰5周整局分子溶液的狀態,纟溶液位置在 熱力學相圖中的位置發生改變,進人相分離( separation)的區域,達到製備孔洞的效製造方法 包括溫度誘導(therinally_induced phase separation )、加入非溶劑與改變溶液的組成。常見的非籲 相分離程序製造方法包括微粒溶濾(丨㈡仏比。 of pore former)、立體印刷(3D printing)、高壓氣體 或超臨界流體穿孔(gas foaming)與燒結(s — g) 半熔融態高分子顆粒。 一般而言,上述以相分離法製造生物基材中最常見 的方法係為冷;東乾燥法,冷;東乾燥法大致可分為兩個步 驟:即冷〉東與乾燥’首先將配製好的高分子溶液降低溫_ 度,使其由原先的均一(homogeneous )變成非均一相 (heter〇geneous ),此情形稱之為相分離,高分子溶液 刀成间分子貧相與高分子富相,當溶劑被移除之後,高 貧相开> 成孔,同,而南分子富相形成孔壁。也就是說, · 巧分子溶液於冷凍(相分離)時,其實基材的多孔結構、 即已生成,故高分子富相型態為決定生物基材結構的因 _ 14 1233943 素之 。如前所述,冷束乾燥、本+ ^ τ μ 之所以廣以心、组織 工私基材製備的原因,便在於 n十 在匕疋在低溫的情況之下(低 ?冷/之熔點),對系統加以真空 ^ 卞,合劑是在被凍結的 情形下,直接變成氣體而移除,如 ★此原先的膜結構即不 又:響。但冷凌乾燥有其先天的條件限制如下: 1 ·溶劑限制··溶劑最好選用揮 平4度季乂冋者,否則在低溫1233943 发明 Description of the invention: [Technical field to which the invention belongs] The present invention relates to a method for forming a biological substrate, and more particularly, to a method for forming a biological substrate under a low temperature condition. [Previous technology] Tissue engineering is one of the fields that have flourished in recent years. One of its famous application methods is to implant cells into biodegradable materials and wait for the cells to grow into functional new tissues or organs. After being implanted into the human body, tissue workers have become a popular method for treating organ function shortage or tissue necrosis. The research on tissue engineering can be roughly divided into three parts: cells, biocompatible substrates (scaffolds), and signals that stimulate cells to show specific behaviors. They influence each other and jointly regulate the differentiation and performance of tissues. The role of 'biological substrates' in tissue engineering includes: 1. Transporting cells or tissues that have been initially cultured to specific parts of the body, avoiding cultivated Cells or tissues are prematurely damaged by immune or other physical effects in the body. 2 · Make the newly generated tissues or organs have a three-dimensional shape that meets the requirements, and give them support and protection. · 13 1233943 3. Stimulate cells or tissues to show specific behaviors, such as coating the surface of a biological substrate with a substance that can produce a signal to achieve the desired effect. The methods of manufacturing biological substrates can generally be divided into phase separation methods and non-phase separation methods. The state of the molecular solution in 5 weeks, the position of the solution in the thermodynamic phase diagram changes, and it enters the phase separation ( In the region of separation), effective manufacturing methods to achieve the preparation of holes include temperature induced (thermally induced phase separation), adding a non-solvent, and changing the composition of the solution. Common methods for making non-phase separation procedures include particle filtration of pore former, 3D printing, high-pressure gas or supercritical fluid gas foaming, and sintering (s-g). Molten polymer particles. Generally speaking, the most common method in the above-mentioned phase separation method for manufacturing biological substrates is cold; Dong drying method, cold; Dong drying method can be roughly divided into two steps: cold> dong and drying ' The polymer solution reduces the temperature, so that it changes from the original homogeneous to a heterogeneous phase. This situation is called phase separation. The polymer solution is cut into a molecular poor phase and a polymer rich phase. When the solvent is removed, the high-lean phase opens pores, and the south-rich phase forms pore walls. In other words, when the molecule solution is frozen (phase separated), the porous structure of the substrate is actually formed, so the polymer-rich phase type is the factor that determines the structure of the biological substrate _ 14 1233943. As mentioned earlier, the reason for the cold beam drying and the preparation of Ben + ^ τ μ, the organization of industrial and private substrates is that n is under the condition of low temperature (low temperature / low melting point). ), Vacuum the system ^ 卞, when the mixture is frozen, it is directly changed to gas and removed, such as ★ this original membrane structure is no longer: ring. However, there are some inherent limitations of chilling drying as follows: 1. Solvent restrictions
大規模生產的門檻之 的情況下,溶劑的蒸氣壓將較常溫下更低,使得溶劑 移除困難度大幅提高,也容易有溶劑殘留的問題。 2.耗費能源:冷康系統及真空幫浦耗電量甚矩,往往是 耗費時間·由於低溫下溶劑揮發性降低,需要較長的 日守間才能移除溶劑,若為高沸點的溶劑系统,數日仍 不也保證完全除去溶劑。 4.儀器設備:需要特別的冷;東乾燥設備,價格高昂。 ,有鑑於此,仍有必要發展新的生物基材製程以符合 製造快速、節省能源與低價位的需求,並藉 :口 1> » 他製造 成本’提升生產效能。 【發明内容】 鑒於上述之發明背景中,為了克服傳統 ^ 7古的缺 發明提供一種新的生物基材之形成方法以符人制 k陕速、節省能源與低價位的需求。 、 15 43 本發明之一目的在於因應不同的高分子材質或應用 $戈,提供不同種類的固定劑於低溫條件下進行固定程 序。由於是在低溫的情形下移除高分子貧相或是固定高 分子富相,所以能夠維持高分子富相的多孔結構並藉此 %成生物基材。本發明之另一目的在於增加使用溶劑的 種类貝’例如可以使用高彿點的溶劑,或是傳統冷;東乾燥 各所無法處理的溶劑。由於使用溶劑的選擇增加,高分 子材質的選擇也隨之增加,因此能製成具有不同材^ 生物基材。 ' 根據以上所述之目的, 的形成方法,此方法步驟簡 乾燥設備,因此,本發明能 的利用性。上述之生物基材 一溶解製程、一調整溫度程 序,此固定程序更包含下列 序、一酸驗中和程序與一膠 【實施方式】 本發明揭示了 一種生物基材 單,不需要使用特別的冷凍 符合經濟上的效益與產業上 的形成方法包含下列步驟: 序、一冷凍程序與一固定程 程序之一者:一固液交換程 化程序。Under the threshold of large-scale production, the vapor pressure of the solvent will be lower than at normal temperature, which makes the difficulty of removing the solvent greatly increased, and it is also prone to the problem of solvent residue. 2. Consumption of energy: Cold power systems and vacuum pumps consume a lot of power, which is often time-consuming. Due to the reduced volatility of the solvent at low temperatures, it requires a longer period of time to remove the solvent. If it is a high-boiling solvent system For several days, the solvent is still not completely removed. 4.Instruments and equipment: Special cooling is needed; Dong drying equipment is expensive. In view of this, it is still necessary to develop a new biological substrate process to meet the needs of rapid manufacturing, energy saving and low price, and use: 口 1 > »other manufacturing cost’ to improve production efficiency. [Summary of the Invention] In view of the above background of the invention, in order to overcome the traditional shortcomings of the invention, the invention provides a new method for forming a biological substrate to meet the needs of man-made systems, speed, energy saving and low price. 15 43 One purpose of the present invention is to provide different types of fixing agents for fixing procedures under low temperature conditions according to different polymer materials or applications. Since the polymer-depleted phase is removed or the polymer-rich phase is fixed at a low temperature, the porous structure of the polymer-rich phase can be maintained and a biological substrate can be formed therefrom. Another object of the present invention is to increase the number of solvents to be used. For example, a solvent with a high Buddha point can be used, or a solvent that can not be processed by conventional cold drying and drying. As the choice of solvents used increases, the choice of high-molecular materials also increases, so it can be made with different materials ^ biological substrates. '' According to the purpose described above, the method of forming, this method has simple steps and drying equipment, and therefore, the present invention can be used. The above-mentioned biological substrate has a dissolving process and a temperature adjustment procedure. The fixing procedure further includes the following sequence, an acid test neutralization procedure, and a glue. [Embodiment] The present invention discloses a biological substrate sheet, which does not need to use a special Freezing conforms to economic benefits and industrial formation methods including the following steps: one of a sequence, a freezing procedure and a fixed procedure: a solid-liquid exchange procedure.
m心艰成方 法。為了能徹底地瞭解本發明,將在下列心 詳盡的製程步驟或組成結構。 颂然地,本發明的施行並 未限定於生物基材領域之拮蓺土 員域技藝者所熟習的特殊細節。另 16 1233943 方面眾所周知的組成或製程步驟並未描述於細節 中以避免造成本發明不必要之限制。本發明的較佳實 施例會詳細描述如下,然而除了這些詳細描述之外,本 發明還可以廣泛地施行在其他的實施例中,且本發明的 範圍不受限定,其以之後的專利範圍為準。 參考第一圖所示,在本發明之一第一實施例中,首 先提供一高分子進料110,其中上述之高分子進料 係為下列族群之一者:聚乳酸(Polylactic acid,PLA )、 · 聚乳酸-甘醇酸【p〇ly(lactide-co-glyC〇iide),PLGA】、 PHA 【P〇ly(hydroxyalkonate)s 】、PHB【poly(3_ hydroxybutyrate)】、聚己内酉旨(p〇iyCapr〇iact〇ne, PCL )及其衍生物。聚乳酸(pla )包含左旋聚乳酸 (PLLA )、右旋聚乳酸(PDLA )與聚左旋-右旋乳酸 PDLLA,且聚乳酸(PLA)之常用溶劑為l,4-二氧陸圜 (1,4-dioxane );聚乳酸-甘醇酸(PLGA )之常用溶劑 鲁 有二甲基亞硬(Dim ethyl sulfoxide,DM SO )或乙酸乙 酯(ethyl acetate )或 1,4-二氧陸圜(1,4-dioxane ) 或二甲基甲醯胺(Dimethylformamide,DMF)或甲基 比嘻酮(N-Methyl-Pyrrolidone,NMP) ; PHA之常用 溶劑係為下列族群之一者:氣仿(chloroform )、乙腈 (acetonitrile )、苯(benzene )、環己烧 17 1233943 (cyclohexane)、1,4-二氧陸圜(l,4-dioxane)與二 甲基亞砜(Dimethylsulfoxide,DMSO ) ; PHB 之常 用溶劑係為下列族群之一者:氣仿(chloroform )、三 氣乙烯(trichloroethylene )、 222-trifluoroethanol、 二甲基曱醯胺(N,N-Dimethylformamide,DMF )、 ethylacetoacetate 與 triolein ; 聚 己 内 酉旨 (polycaprolactone,PCL )之常用溶劑係為下列族群 之一者:1,4-二氧陸圜(1,4-dioxane )、氯仿 鲁 (chloroform)、二甲基甲醯胺(DMF)與二曱基亞砜 (Dimethylsulfoxide,DMSO)。 然後,在本實施例中,輸送高分子進料1 1 0至一混 和裝置中進行一溶解製程1 3 5以溶解高分子進料1 1 〇於 一溶解液1 2 0中,此溶解液包含上述之溶劑,並形成一 具有特定黏度之溶液1 4 〇,此溶液1 4 0之黏度隨著高分 子進料1 1 0之添加量減少而減小以增大所製成的生物基籲 材之孔洞。當高分子進料1 1 〇係為PLA及其衍生物時, 則其重量含量範圍約為上述溶液140的1一%至15 wt% ’其中,較佳的重量含量範圍約為上述溶液1 4〇的 3wt%至l〇wt% ;當高分子進料1 1〇係為plga及其衍 生物時,則其重量含量範圍約為上述溶液1 40的1 wt% ' 至25wt%,其中,較佳的重量含量範圍約為上述溶液 - 18 1233943 140的3wt%至l〇wt%。接著,於一特定溫度 冷束程序145以固化上述之溶液140,並形成 高分子富相物質與一高分子貧相物質之固態結 其中’南分子貧相可形成生物基材的孔洞部分 子富相可形成生物基材的孔壁部分。而且,所 物基材的孔洞係隨著調降該特定溫度而減小。 供一非溶劑1 30並進行一調整温度程序1 6〇以 劑130之溫度至冷凍程序ι45的特定溫度。接 一固液交換程序155,藉由上述之非溶劑13〇 取代咼为子貧相物質,並形成一生物基材丄6 5 在本實施例中,於冷凍程序1 45之前,更 一脫泡程序以去除上述溶液丨4〇中所含的氣泡 上述之冷凍程序145更包含一預乾燥程序,此 序係於上述之特定溫度下執行卩κ匕ϋ態結構 面所具有的高分子貧相物質。另一方面,於調 序160中,上述之非溶劑13〇於特定溫度下仍 態,或是非溶劑130更包含一抗凍劑以便於非: 能於特定溫度下保持液態。當上述之高分子進步 為PLA及其衍生物時,則其非溶劑i 3〇係為一 液’其中’此乙醇水溶液所含之乙醇濃度範圍 wt%至刚Wt%,其較佳的乙醇濃度範圍係為 下進行一 一具有一 構!5〇, ,而高分 製成之生 其次,提 調整非溶 著,進行 以交換且 〇 包含執行 。另外, 預乾燥裎 1 50之表 整溫度程 能保持液 溶劑1 3 〇 斗1 1 〇係 乙醇水溶 係為 6〇 7 5 wt% 1233943 至85 wt% ;當上述之高分子進料丨1〇係為plga及其 衍生物時,則其非溶劑1 30係為一乙醇水溶液,其中, 此乙醇水溶液所含之乙醇濃度範圍係為2〇 wt〇/〇至5〇 wt%,其較佳的乙醇濃度範圍係為25 wt%至35 wt〇/。。 參考第二圖所示,在本發明之一第二實施例中,首 先提供一高分子進料210,其中上述之高分子進料21〇 更包含一幾丁聚醣及其衍生物。然後,輸送高分子進料 2 1 0至一混和裝置中進行一溶解製程2 3 5以溶解高分子肇 進料2 10於一溶解液220中,此溶解液包含上述之溶 劑,並形成一具有特定黏度之第一溶液240,此第一溶 液2 4 0之黏度隨著高分子進料2 1 〇之添加量減少而減小 以增大所製成的生物基材之孔洞。當高分子進料2 1 〇係 為幾丁聚醣及其衍生物時,則其重量含量範圍約為上述 第一溶液240的〇.5wt%至6wt%,其中,較佳的重量 含量範圍約為上述第一溶液240的1 wt%至3wt%。接籲 著’於一特定溫度下進行一冷凍程序245以固化上述之 第一溶液240,並形成一具有一高分子富相物質與一高 分子貧相物質之固態結構2 5 0,其中,高分子貧相可形 成生物基材的孔洞部分,而高分子富相可形成生物基材 的孔壁部分。而且’所製成之生物基材的孔洞係隨著調 ~ 降該特定溫度而減小。其次,提供一第二溶液2 3 0並進 · 20 1233943 行一調整溫度程序260以調整第二溶液230之溫度至冷 ;東程序245的特定溫度,其中上述之第一溶液240係為 一酸性溶液,且第二溶液230係為一鹼性溶液;或是上 述之第一溶液240係為一鹼性溶液,且第二溶液230係 為一酸性溶液。當上述之高分子進料2 1 〇係為幾丁聚醣 及其何生物時,則第一溶液2 4 0係為一酸性溶液,且第 一洛液2 3 0係為一驗性溶液,其中,第二溶液2 3 〇所含 驗性物質之濃度範圍係為〇·5Ν至3N。接著,進行一酸 _ 驗中和程序255,藉由上述之第二溶液230以使得高分 子富相固化並藉此形成一生物基材2 6 5。 在本實施例中,於冷凍程序245之前,更包含執行 一脫泡程序以去除上述第一溶液240中所含的氣泡。另 外’上述之冷凍程序2 4 5更包含一預乾燥程序,此預乾 燥程序係於上述之特定溫度下執行以氣化固態結構250 之表面所具有的高分子貧相物質。另一方面,於調整溫鲁 度程序260中,上述之第二溶液230於特定溫度下仍能 保持液態,或是第二溶液230更包含一抗凍劑以便於第 二溶液230能於特定溫度下保持液態,其中上述之抗凍 劑更包含一乙醇成分,且乙醇濃度範圍係為第二溶液 230 的 20wt%至 70wt%。 參考第三圖所示,在本發明之一第三實施例中,首 · 21 1233943 先提供一 鬲分子推Μ 2 1 Γ>,甘丄,、,、、丄、一M heart difficult method. In order to fully understand the present invention, detailed process steps or constituent structures will be described below. To put it bluntly, the practice of the present invention is not limited to the specific details familiar to those skilled in the field of bio-substrates. The other well-known components or process steps in 1212943 are not described in detail to avoid unnecessary limitations of the present invention. The preferred embodiments of the present invention will be described in detail as follows. However, in addition to these detailed descriptions, the present invention can be widely implemented in other embodiments, and the scope of the present invention is not limited, which is subject to the scope of subsequent patents. . Referring to the first figure, in a first embodiment of the present invention, a polymer feed 110 is first provided, wherein the polymer feed is one of the following groups: Polylactic acid (PLA) , · Polylactic acid-glycolic acid [p〇ly (lactide-co-glyCoiide), PLGA], PHA [P〇ly (hydroxyalkonate) s], PHB [poly (3_hydroxybutyrate)], polycaprolactone (PoiCaproiactone, PCL) and its derivatives. Polylactic acid (pla) includes L-polylactic acid (PLLA), d-polylactic acid (PDLA), and poly-L-d-lactic acid PDLLA, and the commonly used solvent of polylactic acid (PLA) is 1,4-dioxolane (1, 4-dioxane); commonly used solvents for polylactic acid-glycolic acid (PLGA) include Dim ethyl sulfoxide (DM SO) or ethyl acetate or 1,4-dioxolane ( 1,4-dioxane) or Dimethylformamide (DMF) or N-Methyl-Pyrrolidone (NMP); The common solvent of PHA is one of the following groups: chloroform ), Acetonitrile, benzene, cyclohexane, 1212943943 (cyclohexane), 1,4-dioxane (l, 4-dioxane), and dimethyl sulfoxide (DMSO); PHB of Commonly used solvents are one of the following groups: chloroform, trichloroethylene, 222-trifluoroethanol, N, N-Dimethylformamide (DMF), ethylacetoacetate and triolein; polycaproline The common solvents of polycaprolactone (PCL) are the following groups One of: 1,4-dioxane (1,4-dioxane), Lu chloroform (chloroform), dimethylformamide (DMF) and two Yue sulfoxide (Dimethylsulfoxide, DMSO). Then, in this embodiment, a polymer feed 110 is transported to a mixing device to perform a dissolving process 1 35 to dissolve the polymer feed 1 1 0 in a dissolving solution 120. The dissolving solution contains The above-mentioned solvent forms a solution 140 with a specific viscosity, and the viscosity of the solution 140 decreases with the decrease of the amount of the polymer feed 110 to increase the prepared bio-based material. Holes. When the polymer feed 1 10 is PLA and its derivatives, the weight content range is about 11% to 15 wt% of the above solution 140. Among them, the preferred weight content range is about the above solution 1 4 〇3wt% to 10wt%; when the polymer feed 110 is plga and its derivatives, its weight content range is about 1 wt% 'to 25wt% of the above solution 1 40, where, compared with A preferred weight content range is about 3% to 10% by weight of the above solution-18 1233943 140. Next, a cold beam procedure 145 at a specific temperature is used to solidify the above-mentioned solution 140 and form a solid junction between a polymer-rich phase substance and a polymer-lean phase substance. Among them, the south molecular-lean phase can form the pore portion of the biological substrate. The pore wall portion of the biological substrate is formed. Moreover, the pores of the substrate are reduced as the specific temperature is lowered. A non-solvent 130 is supplied and an adjustment temperature program 160 is performed, and the temperature of the agent 130 is reached to a specific temperature of the freezing program 45. Following a solid-liquid exchange program 155, the above-mentioned non-solvent 13 is used to replace the tritium as a sub-lean phase, and a biological substrate is formed. 6 5 In this embodiment, before the freezing procedure 1 45, a defoaming procedure is further performed. In order to remove the air bubbles contained in the solution, the freezing process 145 described above further includes a pre-drying process. This sequence is performed at the specific temperature mentioned above to carry out the polymer-lean phase substance in the 卩 κ 卩 卩 structure surface. On the other hand, in the sequence 160, the above-mentioned non-solvent 13 is still at a specific temperature, or the non-solvent 130 further includes an antifreeze so as not to be able to maintain a liquid state at a specific temperature. When the above polymer progresses to PLA and its derivatives, the non-solvent i 30 is a one-liquid 'wherein' the ethanol concentration in the ethanol aqueous solution ranges from wt% to just Wt%, and its preferred ethanol concentration is The scope is one structure for the next! 50, while the high score is made of the second, the adjustment of non-dissolved, carried out in exchange and 〇 contains the implementation. In addition, the pre-drying temperature range of 150 can maintain the liquid solvent of 1300, 1100, and 100% ethanol. The water-soluble ethanol is 605.5% by weight, 1233943 to 85% by weight. When it is plga and its derivatives, its non-solvent 130 is an ethanol aqueous solution, wherein the ethanol concentration contained in the ethanol aqueous solution ranges from 20 wt% / 50 to 50 wt%. The ethanol concentration range was 25 wt% to 35 wt%. . Referring to the second figure, in a second embodiment of the present invention, a polymer feed 210 is first provided, wherein the polymer feed 21 described above further includes a chitosan and a derivative thereof. Then, the polymer feed 2 10 is transported to a mixing device to perform a dissolution process 2 3 5 to dissolve the polymer feed 2 10 in a dissolving solution 220. The dissolving solution contains the above-mentioned solvent and forms The first solution 240 having a specific viscosity, and the viscosity of the first solution 240 decreases with the addition of the polymer feed 2 10 to increase the pores of the prepared biological substrate. When the polymer feed 2 10 is chitosan and its derivatives, the weight content range is about 0.5 wt% to 6 wt% of the first solution 240, and the preferred weight content range is about It is 1 wt% to 3 wt% of the first solution 240 described above. Then, a freezing process 245 is performed at a specific temperature to solidify the first solution 240 and form a solid structure 250 having a polymer-rich phase substance and a polymer-lean phase substance. Among them, the polymer The lean phase can form the pore portion of the biological substrate, while the polymer rich phase can form the pore wall portion of the biological substrate. Moreover, the pores of the biological substrate made by ′ decrease with the adjustment of the specific temperature. Secondly, a second solution 2 3 0 is provided in parallel. 20 1233943 A temperature adjustment program 260 is performed to adjust the temperature of the second solution 230 to cold; a specific temperature of the East program 245, wherein the first solution 240 is an acidic solution. And the second solution 230 is an alkaline solution; or the first solution 240 described above is an alkaline solution, and the second solution 230 is an acidic solution. When the above-mentioned polymer feed 210 is chitosan and other organisms, the first solution 240 is an acidic solution, and the first solution Luo 230 is an experimental solution. Wherein, the concentration range of the test substance contained in the second solution 2 30 is from 0.5N to 3N. Next, an acid neutralization procedure 255 is performed, and the high-molecular-rich phase is solidified by the second solution 230 described above, thereby forming a biological substrate 2 6 5. In this embodiment, before the freezing process 245, it further includes performing a defoaming process to remove air bubbles contained in the first solution 240. In addition, the above-mentioned freezing process 2 4 5 further includes a pre-drying process. The pre-drying process is performed at the above-mentioned specific temperature to vaporize the polymer-lean phase substance on the surface of the solid structure 250. On the other hand, in the temperature adjustment program 260, the above-mentioned second solution 230 can remain liquid at a specific temperature, or the second solution 230 further includes an antifreeze agent so that the second solution 230 can be at a specific temperature. The antifreeze agent further includes an ethanol component, and the ethanol concentration range is 20 wt% to 70 wt% of the second solution 230. Referring to the third figure, in a third embodiment of the present invention, the first 212133943 first provides a 鬲 molecule push Μ 2 1 Γ >, Gan, ,,,,, 一, a
料31〇之添加量減少而 孔洞。當高分子進料310係為幾丁聚醣及其衍生物時,籲 則/、重里含1範圍約為上述溶液34〇的〇.5wt%至 tb溶液340之黏度隨著該高分子進 而減小以增大所製成的生物基材之 6 Wt /〇其中,較佳的重量含量範圍約為上述溶液3 4 0 的 lwt%至 3wt% ; 當高分子進料3 1 0係為海藻酸鈉及 其何生物時,則其重量含量範圍約為上述溶液340的 0.5wt /〇至8wt%,其中,較佳的重量含量範圍約為上述 溶液340的lwt%至4wt%。接著,於一特定溫度下進 4亍東程序345以固化上述之溶液340,並形成一具 有一高分子富相物質與一高分子貧相物質之固態結構 3 50 ’其中,高分子貧相可形成生物基材的孔洞部分, 而高分子富相可形成生物基材的孔壁部分。而且,所製 成之生物基材的孔洞係隨著調降該特定溫度而減小。其 -人,知供一父聯劑3 3 0並進行一調整溫度程序3 6 0以調 整父聯劑3 3 0之溫度至冷凍程序3 4 5的特定溫度。當高 22 1233943 分子進料3 1 0係為幾丁聚醣及其衍生物時,則上述之交 聯劑330包含下列族群中之一者··硫酸溶液、醛類溶液 (aldehyde)、二醛類溶液(dialdehyde)及 genipinThe amount of material 31 is reduced and the holes are formed. When the polymer feed 310 is chitosan and its derivatives, the viscosity of 0.5% by weight of the solution containing 1 to about 34% of the above solution to the tb solution 340 decreases with the polymer. In order to increase the 6 Wt / 〇 of the prepared biological substrate, the preferred weight content range is about 1% to 3% by weight of the above solution 3 4 0; when the polymer feed 3 1 0 is alginic acid In the case of sodium and other organisms, the weight content range is about 0.5 wt / 0 to 8 wt% of the solution 340, and the preferred weight content range is about 1 wt% to 4 wt% of the solution 340. Then, the procedure 345 is performed at a specific temperature to solidify the above solution 340, and a solid structure 3 50 ′ having a polymer rich phase substance and a polymer poor phase substance is formed. Among them, the polymer poor phase can form a biological The pore portion of the substrate, and the polymer rich phase can form the pore wall portion of the biological substrate. Moreover, the pores of the prepared biological substrate decrease as the specific temperature is lowered. It is known that a parent couple agent 3 3 0 is supplied and an adjustment temperature program 3 60 is performed to adjust the temperature of the parent couple agent 3 3 0 to a specific temperature of the freezing program 3 4 5. When the high 22 1233943 molecular feed 3 1 0 is chitosan and its derivatives, the above-mentioned crosslinking agent 330 includes one of the following groups: sulfuric acid solution, aldehyde solution, dialdehyde Dialdehyde and Genipin
>谷液,當南分子進料3 1 〇係為海藻酸鈉及其衍生物時, 則上述之交聯劑330係為一氣化鈣溶液,且氯化鈣溶液 所含氣化妈之濃度範圍係為1^%至2〇wt%。接著,進 行一膠化程序3 5 5,藉由上述之交聯劑3 3 〇以膠化高分 子富相物質,並形成一生物基材365。 在本實施例中,於冷凍程序345之前,更 一脫泡程序以去除上述溶液34〇中所含的氣泡。另外 上述之冷康程彳345更包含一預&燥程序,政匕預乾燥芳 序係於上述之特定溫度下執行以氣化固態結構35〇之$ 面所具有的高分子貧相物質。另一方面,力調整溫度|> Valley liquid, when the South Molecular Feed 3 10 is sodium alginate and its derivatives, the above-mentioned cross-linking agent 330 is a gasified calcium solution, and the concentration of the gasified liquid contained in the calcium chloride solution The range is from 1% to 20% by weight. Next, a gelation process 3 5 5 is performed, and the polymer-rich phase substance is gelatinized with the cross-linking agent 3 3 0 described above, and a biological substrate 365 is formed. In this embodiment, before the freezing process 345, a defoaming process is further performed to remove the air bubbles contained in the solution 34. In addition, the above-mentioned Lengkang Cheng 彳 345 also includes a pre-drying process. The pre-dried aromatic sequence is performed at the above-mentioned specific temperature to vaporize the polymer-depleted phase substance in the solid surface of 35 °. On the other hand, force adjusts temperature |
f 360巾’上述之交聯劑33〇於特定溫度下仍能保持分 態’或是交聯劑330更包含一抗;東劑以便於交聯劑33 能於特定溫度下保持液態,#中上述之抗;東劑更包含一 乙醇成分’且乙醇濃度範圍係為交聯齊丨33〇的2〇州 至 7 0 w t %。 在上述本發明之實施例中,本 + ¾明揭示了一種生物 基材的形成方法,因應不同的高分 ^ 刀于材質或應用需求, 提供不同種類的固定劑於低溫條件 卞卜進行固定程序。由 23 1233943 於是在低溫的情形下移除高分子貧相或是固定高分子富 相,所以能夠維持冷束時之高分子富相結構,藉此形: 生物基材。而且本發明並不限定使用溶劑的種類,例如 可以使用高沸點的溶劑,或是傳統冷涑乾燥法所無法處 理的溶劑。由於使用溶劑的選擇增加,高分子材質的選 擇也隨之增加,因此能製成具有不同材質的生物基材。f 360 towel 'The above-mentioned cross-linking agent 33 can still maintain the state at a specific temperature' or the cross-linking agent 330 further contains a primary antibody; the east agent so that the cross-linking agent 33 can remain liquid at a specific temperature, # 中The above-mentioned resistance; the east agent further includes an ethanol component ', and the ethanol concentration range is from 20 to 70 wt% of the crosslinked Qi 33. In the above-mentioned embodiments of the present invention, the present invention discloses a method for forming a biological substrate. In response to different high scores, depending on the material or application requirements, different types of fixatives are provided under low temperature conditions to perform the fixation procedure. . Since 23 1233943, the polymer-depleted phase or the fixed polymer-rich phase is removed at a low temperature, so the polymer-rich phase structure can be maintained in the cold beam, thereby forming: a biological substrate. Moreover, the present invention is not limited to the type of solvent used, for example, a solvent having a high boiling point or a solvent that cannot be processed by the conventional cold heading drying method can be used. As the choice of solvents used increases, so does the choice of polymer materials, so bio-based materials with different materials can be made.
综合以上所述,本發明揭示了—種生物基材的形成 方法,此方法步驟簡單,不需要使用特別的冷束乾燥設 備,因此’本發明能符合經濟上的效益與產業上的利用 性。上述之生物基材的形成方法包含下列步驟:—溶解 製程、-調整溫度程序、—冷;東程序與_固定程序,此 固定程序更包含-固液交換程序、—酸驗中和程序與一 膠化程序。 顯然地,依照上面實施例中的描述,本發明可能有 許多的修正與差異。因此需要在其附加的權利要求項\ 範圍内加以理解,除了上述詳細的描述外,本發明還可 以廣泛地在其他的實施例中施行。上述僅為本發明之較 佳實施例而已,並非用以限定本發明之t請專利範圍; 凡其它未脫離本發明所揭示之精神下所完成的等效改變 或修飾,均應包含在下述申請專利範圍内。 【圖式的簡單說明】 24 1233943 第一圖所示係為钿4去, 中 中 中 …根據本發明之一第一較佳 ,具有一固液交換裎床夕▲ 〜例 、矛序之生物基材的製程流程圖; 圖所示係為根據本發明之一第二較佳每 ’具有-酸驗中和程序之生物基材的製程流:圖:: 弟三圖所示係為根據本發明之一第三較佳實施例 ,具有一膠化程序之生物基材的製程流程圖。 主要部分之代表符號】 高分子進料110 溶解液1 2 0 非溶劑130 溶解製程1 3 5 具有特定黏度之溶液1 4 〇 冷凍程序1 4 5 固態結構1 5 0 固液交換程序1 5 5 調整溫度程序1 6 〇 生物基材1 6 5 高分子進料210 溶解液2 2 0 第二溶液2 3 0 溶解製程2 3 5 第一溶液2 4 0 冷凍程序2 4 5 固態結構2 5 0 酸鹼中和程序2 5 5 調整溫度程序2 6 0 生物基材2 6 5 高分子進料3 1 0 溶解液320 交聯劑3 3 0 溶解製程3 3 5 具有特定黏度之溶液340 冷凍程序345 固態結構3 5 0 膠化程序3 5 5 調整溫度程序360 生物基材3 6 5In summary, the present invention discloses a method for forming a biological substrate. The method has simple steps and does not require the use of a special cold beam drying device. Therefore, the present invention can meet economic benefits and industrial applicability. The above-mentioned method for forming a biological substrate includes the following steps:-dissolution process,-temperature adjustment procedure,-cold; east procedure and _ fixed procedure, the fixed procedure further includes-solid-liquid exchange procedure,-acid test neutralization procedure and Gelatinization procedure. Obviously, according to the description in the above embodiment, the present invention may have many modifications and differences. Therefore, it needs to be understood within the scope of the appended claims. In addition to the above detailed description, the present invention can be widely implemented in other embodiments. The above are only the preferred embodiments of the present invention, and are not intended to limit the scope of the patents of the present invention. All other equivalent changes or modifications made without departing from the spirit disclosed by the present invention should be included in the following applications Within the scope of the patent. [Brief description of the figure] 24 1233943 The first picture shows a 钿 4 go, middle, middle, and… according to one of the present invention is the first best, with a solid-liquid exchange 裎 bed ▲ ~ Example, spear order creature The process flow chart of the substrate; the figure shows a process flow of a biological substrate with a second acid-neutralization neutralization procedure according to one of the present invention: Figure :: The third figure shows A third preferred embodiment of the invention is a process flow chart of a biological substrate having a gelling process. Representative symbols of main parts] Polymer feed 110 Dissolving solution 1 2 0 Non-solvent 130 Dissolving process 1 3 5 Solution with specific viscosity 1 4 〇 Freezing procedure 1 4 5 Solid state structure 1 5 0 Solid-liquid exchange procedure 1 5 5 Adjustment Temperature program 1 6 〇 Biological substrate 1 6 5 Polymer feed 210 Dissolving solution 2 2 0 Second solution 2 3 0 Dissolving process 2 3 5 First solution 2 4 0 Freezing procedure 2 4 5 Solid state structure 2 5 0 Acid-base Neutralization procedure 2 5 5 Temperature adjustment procedure 2 6 0 Biological substrate 2 6 5 Polymer feed 3 1 0 Dissolving solution 320 Crosslinking agent 3 3 0 Dissolution process 3 3 5 Solution with specific viscosity 340 Freezing procedure 345 Solid state structure 3 5 0 Gelatinization program 3 5 5 Temperature adjustment program 360 Biological substrate 3 6 5
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