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CN101914434B - Device and method for dynamically preparing heterocavity bacterium cellulose materials - Google Patents

Device and method for dynamically preparing heterocavity bacterium cellulose materials Download PDF

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CN101914434B
CN101914434B CN201010271720.3A CN201010271720A CN101914434B CN 101914434 B CN101914434 B CN 101914434B CN 201010271720 A CN201010271720 A CN 201010271720A CN 101914434 B CN101914434 B CN 101914434B
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洪枫
洪思仪
陈琳
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Abstract

本发明涉及一种动态制备异型空腔细菌纤维素材料的装置及方法,该装置包括温度计口,酸液碱液添加口,把手,通气口,pH计口,营养补料口,转轴,发酵罐,马达,水浴装置,模具;其制备包括:将细菌纤维素生产菌株接入液体培养基扩培后,将其转移到配备有特定形状模具的发酵装置中动态扰动培养,培养后即可收获空腔异形纤维素材料。本发明制备的异型空腔BC材料不仅其尺寸和形状是可控的,而且发酵装置的模具可拆卸,重复使用,且制备方法简便易行,成本低廉,生产效率高,适用于工业化生产;该异型空腔BC材料可广泛应用于人工血管、神经纤维导管等中空器官的替代品,还可作为食品包裹材料如肉制品肠衣、果冻外衣等。

The invention relates to a device and method for dynamically preparing special-shaped cavity bacterial cellulose materials. The device includes a thermometer port, an acid liquid and alkali liquid addition port, a handle, a ventilation port, a pH meter port, a nutrient feeding port, a rotating shaft, and a fermenter , a motor, a water bath device, and a mould; its preparation includes: after the bacterial cellulose production strain is inserted into the liquid medium for expansion, it is transferred to a fermentation device equipped with a mold of a specific shape for dynamic perturbation culture, and the empty space can be harvested after cultivation. Lumen profiled cellulose material. The special-shaped cavity BC material prepared by the invention is not only controllable in size and shape, but also the mold of the fermentation device can be disassembled and reused, and the preparation method is simple and easy, the cost is low, the production efficiency is high, and it is suitable for industrial production; Special-shaped cavity BC materials can be widely used as substitutes for hollow organs such as artificial blood vessels and nerve fiber catheters, and can also be used as food wrapping materials such as meat casings and jelly casings.

Description

动态制备异型空腔细菌纤维素材料的装置及方法Device and method for dynamically preparing special-shaped cavity bacterial cellulose material

技术领域 technical field

本发明属于细菌纤维素材料的制备领域,特别涉及一种动态制备异型空腔细菌纤维素材料的装置及方法。The invention belongs to the field of preparation of bacterial cellulose materials, in particular to a device and method for dynamically preparing special-shaped cavity bacterial cellulose materials.

背景技术 Background technique

细菌纤维素(Bacterial Cellulose,简称BC)是一类由微生物产生的纯纤维素。细菌纤维素和植物纤维一样都是由β-D-葡萄糖通过β-1,4-葡萄糖苷键结合成的直链,直链间彼此平行,不呈螺旋构象,无分支结构,又称为β-1,4-葡聚糖。细菌纤维素由于具有独特的生物亲和性、生物相容性和无过敏反应,以及高的持水性、聚合度、结晶度,良好的三维纳米纤维网络结构、高的张力和强度,尤其是良好的机械韧性,因此在人工血管、组织工程支架、人工皮肤以及治疗皮肤损伤等方面具有广泛的用途,是国际生物医用材料研究的热点之一。Bacterial Cellulose (BC) is a kind of pure cellulose produced by microorganisms. Bacterial cellulose, like plant fiber, is a straight chain formed by β-D-glucose through β-1,4-glucosidic bonds. The straight chains are parallel to each other, not in a helical conformation, and without branching structure, also known as β - 1,4-glucan. Bacterial cellulose has unique bioaffinity, biocompatibility and no allergic reaction, as well as high water holding capacity, degree of polymerization, crystallinity, good three-dimensional nanofiber network structure, high tension and strength, especially good Therefore, it has a wide range of uses in artificial blood vessels, tissue engineering scaffolds, artificial skin, and treatment of skin injuries. It is one of the hotspots in international biomedical materials research.

目前细菌纤维素材料的制备一般采用常规静置培养法,获得的是一张纤维素膜。用常规液体深层桨叶垂直搅拌技术会引起木醋杆菌的变异退化,导致其不再合成纤维素,而目前常用的较少引起菌种退化的动态发酵技术(在气升式发酵罐中)仅能制备颗粒状的细菌纤维素材料,由于纤维素可溶于某些化学试剂,因此很早就有人希望将细菌纤维素溶液灌注模具来“铸造”有形状的空腔生物材料。然而效果却并不理想,所获得的纤维素产品不具有原细菌纤维素的优良特性,这可能是由于它的物理结构被改变而导致性能劣化。由于木醋杆菌合成纤维素是一个耗氧的次级代谢过程,纤维素易形成于空气与培养液的交界处,因此氧气是纤维素形成的重要因素。已有的研究表明,只要在静置发酵液中提供表面透氧性能良好、具有一定形状的模具,在模具表面就可以形成该形状的纤维素膜,这样利用细菌在线发酵制备有形生物医用材料就成为可能。At present, the preparation of bacterial cellulose materials generally adopts the conventional static culture method, and a piece of cellulose film is obtained. Using conventional liquid deep paddle vertical stirring technology will cause the variation and degeneration of Acetobacter xylinum, causing it to no longer synthesize cellulose, while the dynamic fermentation technology (in the air-lift fermenter) commonly used at present that causes less strain degradation can only Granular bacterial cellulose materials can be prepared. Because cellulose is soluble in certain chemical reagents, it has long been hoped that the bacterial cellulose solution will be poured into a mold to "cast" a shaped cavity biomaterial. However, the effect is not ideal, and the obtained cellulose product does not have the excellent characteristics of the original bacterial cellulose, which may be due to its physical structure being changed and resulting in performance degradation. Since the synthesis of cellulose by Acetobacter xylinum is an oxygen-consuming secondary metabolic process, cellulose is easily formed at the junction of air and culture solution, so oxygen is an important factor for the formation of cellulose. Existing studies have shown that as long as a mold with good surface oxygen permeability and a certain shape is provided in the static fermentation broth, a cellulose film of this shape can be formed on the surface of the mold, so that it is easy to prepare tangible biomedical materials by using bacteria on-line fermentation. become possible.

首次利用该原理成功制备有形状的细菌纤维素产品是一个手套形状的人工皮肤(UKPatent 12,169,543;White and Brown,1989)。该技术是利用能透氧气的手形微型织造物(microwoven textiles)作为模具,静态条件下培养。1990和1991年日本人Yamanaka根据同样的原理,利用一个能透氧的空腔圆管,如玻璃纸、特富龙、硅胶、陶瓷等制作的模具,通过注入含活细菌的培养液在静态发酵条件下制备人工血管获得了成功(EP Patent0,396,344;JP Patent 3,272,772)。他以成年杂种狗为实验对象,将制备好的BC管材料植入到大动脉和颈静脉血管中,发现虽然在血管缝合处以及BC管内壁有轻微的血栓吸附,但是BC管始终保持良好的通畅度。2001和2003年德国Klemm等人将一个内部是玻璃圆柱而外部是玻璃圆管组成的模具浸入细菌培养液中,通过静态发酵制备成功小直径人工血管(1~3mm内径)(商品名为BASYC),并经老鼠动物实验证明该人工血管抗血栓效果很好(WO Patent 0,161,026,US Patent 2,003,013,163)。大白鼠没有经任何抗凝药物处理,观察到颈动脉-BC管复合体被结缔组织包裹,上面布满类似血管滋养管的小血管,BC管完全被活体组织包裹没有任何排斥反应。所有植入的BC管在手术后都保持100%的畅通率,而且没有血栓凝结或者组织增生的现象。由此可见,中空细菌纤维素管是制备<6mm人工血管的良好材料。此外,该空腔纤维管还可以作为气管、输尿管、软骨支架、覆盖神经纤维的护套,以及某些空腔器官的替代物等(WO Patent 0,161,026;US Patent 2,003,013,163)。2005年美国和瑞典国际合作小组的Svensson等人报道了以细菌纤维素作为软骨组织工程支架的实验结果,并指出效果较好。2006年Backdahl等人通过研究细菌纤维素的机械性能以及与人平滑肌细胞的相互作用指出该材料今后可以用于组织工程血管。以上研究证明了凝胶状的管状BC材料以其高的机械强度、大的持水力、十分规则的内表面和极好的生物相容性等特点,在显微外科手术中作为血管组织替代物具有巨大的应用前景。The first successful preparation of a shaped bacterial cellulose product using this principle was a glove-shaped artificial skin (UKPatent 12,169,543; White and Brown, 1989). The technology uses oxygen-permeable hand-shaped micro-woven fabrics (microwaven textiles) as a mold and cultivates them under static conditions. In 1990 and 1991, according to the same principle, the Japanese Yamanaka used an oxygen-permeable hollow tube, such as a mold made of cellophane, Teflon, silica gel, ceramics, etc., to inject a culture solution containing live bacteria under static fermentation conditions. Preparation of artificial blood vessels has been successful (EP Patent 0,396,344; JP Patent 3,272,772). He implanted the prepared BC tube material into the aorta and jugular vein with adult mongrel dogs as the experimental subjects, and found that although there was slight thrombus adsorption at the suture of the blood vessel and the inner wall of the BC tube, the BC tube always maintained good patency Spend. In 2001 and 2003, German Klemm et al. immersed a mold consisting of a glass cylinder inside and a glass tube outside into bacterial culture solution, and successfully prepared small-diameter artificial blood vessels (1-3mm inner diameter) through static fermentation (trade name: BASYC). , and proved that the antithrombotic effect of the artificial blood vessel is very good through mouse experiments (WO Patent 0,161,026, US Patent 2,003,013,163). Rats were not treated with any anticoagulant drugs, and it was observed that the carotid artery-BC tube complex was wrapped by connective tissue, covered with small blood vessels similar to vasa vasorum, and the BC tube was completely wrapped by living tissue without any rejection reaction. All implanted BC tubes maintained a 100% patency rate after surgery, and there was no phenomenon of thrombus clotting or tissue proliferation. It can be seen that the hollow bacterial cellulose tube is a good material for preparing artificial blood vessels <6mm. In addition, the hollow fiber tube can also be used as a trachea, ureter, cartilage scaffold, a sheath covering nerve fibers, and a substitute for certain hollow organs, etc. (WO Patent 0,161,026; US Patent 2,003,013,163). In 2005, Svensson et al. from the United States and the Swedish International Cooperation Group reported the experimental results of using bacterial cellulose as a cartilage tissue engineering scaffold, and pointed out that the effect was better. In 2006, Backdahl et al pointed out that the material could be used for tissue engineering blood vessels in the future by studying the mechanical properties of bacterial cellulose and the interaction with human smooth muscle cells. The above studies have proved that the gel-like tubular BC material is used as a vascular tissue substitute in microsurgery because of its high mechanical strength, large water holding capacity, very regular inner surface and excellent biocompatibility. It has great application prospect.

BC除了用于人造血管等医用材料外,还可以用于人工皮肤等伤科敷料。微生物纤维素独特三维网状结构内部有很多“孔道”,有良好的透气、透水性能,能吸收60~700倍于其干重的水份,这些水分是以自由水的形式存在。使用BC作为伤口敷料能够迅速吸收伤口血液和组织液,防止伤口感染化脓,又能为慢性伤口附近的组织再生提供湿润的环境促进伤口愈合和减轻疼痛。同时纤维素不会和伤口粘连,不会造成二次伤害,剥离时也不会有残留。首次利用能透氧的手形微型织造物为模具静态培养成功制备的手套形状的人工皮肤在治疗大面积烧伤/烫伤的手部皮肤时具有良好效果。自1987年以来,巴西连续报道了400多例应用细菌纤维素膜对烧伤、烫伤、褥疮、冻伤、皮肤移植和慢性皮肤溃疡等治疗效果良好的实例。现已有用其制成的人工皮肤(商品名为BioFill)、纱布、绷带和“创口贴”等伤科敷料商品上市。另外一种叫做Xcell的BC创伤敷料也被用来促进慢性创伤的愈合,同样也表现出很好的治疗效果。研究显示这种BC敷料在慢性创伤的应用方面较之其他材料的敷料能够更有效地促进伤口愈合。与其它人工皮肤和伤科敷料相比,该膜的主要特点是在潮湿情况下机械强度高、对液、气及电解物有良好的通透性、与皮肤相容性好,无刺激性,可有效缓解疼痛,防止细菌的感染和吸收伤口渗出的液体,促进伤口的快速愈合,有利于皮肤组织生长。此膜作为缓释药物的载体携带各种药物,利于皮肤表面给药,促使创面的愈合和康复。因此,该纤维素作为一种极具应用潜力的生物材料具有广阔的市场应用前景。In addition to being used in medical materials such as artificial blood vessels, BC can also be used in traumatic dressings such as artificial skin. The unique three-dimensional network structure of microbial cellulose has many "pores" inside, has good air permeability and water permeability, and can absorb 60 to 700 times its dry weight of water, which exists in the form of free water. Using BC as a wound dressing can quickly absorb wound blood and tissue fluid, prevent wound infection and suppuration, and provide a moist environment for tissue regeneration near chronic wounds to promote wound healing and reduce pain. At the same time, the cellulose will not adhere to the wound, will not cause secondary damage, and will not remain when peeled off. For the first time, the glove-shaped artificial skin successfully prepared by using oxygen-permeable hand-shaped micro-woven fabrics for mold static culture has good effects in the treatment of large-area burn/scald hand skin. Since 1987, Brazil has continuously reported more than 400 examples of good therapeutic effects of bacterial cellulose membranes on burns, scalds, bedsores, frostbite, skin grafts and chronic skin ulcers. Commercial dressings such as artificial skin made from it (trade name BioFill), gauze, bandages and "band-aids" are now on the market. Another BC wound dressing called Xcell has also been used to promote healing of chronic wounds and has also shown good therapeutic results. Studies have shown that this BC dressing can promote wound healing more effectively than dressings made of other materials in the application of chronic wounds. Compared with other artificial skin and traumatic dressings, the main features of this film are high mechanical strength under wet conditions, good permeability to liquid, gas and electrolyte, good compatibility with skin, and non-irritating. It can effectively relieve pain, prevent bacterial infection and absorb the fluid exuded from the wound, promote the rapid healing of the wound, and is conducive to the growth of skin tissue. The film is used as a carrier for slow-release drugs to carry various drugs, which is beneficial to drug delivery on the skin surface, and promotes the healing and rehabilitation of wounds. Therefore, the cellulose has broad market application prospects as a biological material with great application potential.

但是现有技术方法的不足之处在于需要特定的透氧模具和静态发酵制备,生产周期长,生产成本高,生产效率低,无法进行工业化生产和应用。However, the disadvantages of the prior art methods are that specific oxygen-permeable molds and static fermentation preparation are required, the production cycle is long, the production cost is high, and the production efficiency is low, so industrial production and application cannot be carried out.

发明内容 Contents of the invention

本发明所要解决的技术问题是提供一种动态制备异型空腔细菌纤维素材料的装置及方法,该方法制备的异型空腔BC材料不仅其尺寸和形状是可控的,而且发酵装置的模具可拆卸,重复使用,且制备方法简便易行,成本低廉,生产效率高,适用于工业化生产;该异型空腔BC材料可广泛应用于人工血管、神经纤维导管等中空器官的替代品,还可作为食品包裹材料如肉制品肠衣、果冻外衣等。The technical problem to be solved by the present invention is to provide a device and method for dynamically preparing a special-shaped cavity bacterial cellulose material. Not only the size and shape of the special-shaped cavity BC material prepared by the method are controllable, but also the mold of the fermentation device can be controlled. It is disassembled and reused, and the preparation method is simple and easy, with low cost and high production efficiency, and is suitable for industrial production; the special-shaped cavity BC material can be widely used as a substitute for hollow organs such as artificial blood vessels and nerve fiber catheters, and can also be used as a Food packaging materials such as meat casings, jelly casings, etc.

本发明的一种动态制备异型空腔细菌纤维素材料的装置,包括温度计口,酸液碱液添加口,把手,通气口,pH计口,营养补料口,转轴,发酵罐,马达,水浴装置,模具,其特征是:所述的转轴一端连接固定马达输出轴,转轴另一端从发酵罐一端面中心位置伸入发酵罐内;在发酵罐内的转轴上固定有模具。A device for dynamically preparing special-shaped cavity bacterial cellulose materials according to the present invention includes a thermometer port, an acid liquid alkali liquid addition port, a handle, a vent port, a pH meter port, a nutrient feeding port, a rotating shaft, a fermenter, a motor, and a water bath The device, the mold, is characterized in that: one end of the rotating shaft is connected to a fixed motor output shaft, and the other end of the rotating shaft extends into the fermentation tank from the center of one end surface of the fermentation tank; a mold is fixed on the rotation shaft in the fermentation tank.

所述的转轴在发酵罐内腔安装固定有转盘,转轴通过转盘圆周边缘对称固定有2个以上模具。The rotating shaft is installed and fixed with a turntable in the inner cavity of the fermenter, and more than two molds are symmetrically fixed on the rotating shaft through the peripheral edge of the turntable.

所述的模具为棍形或手套形模具。The mold is stick-shaped or glove-shaped.

所述的模具为手套形模具,其中,手套形模为依次在转轴上穿入1个以上手套形模具。The mold is a glove-shaped mold, wherein more than one glove-shaped mold is sequentially inserted on the rotating shaft.

所述模具的横截面形状为圆形、方形、椭圆形、三角形、心形或五角星形。The cross-sectional shape of the mold is circular, square, oval, triangular, heart-shaped or five-pointed star-shaped.

所述的模具为实心或者中空结构。The mold is a solid or hollow structure.

所述的温度计口、酸液碱液添加口、pH计口、营养补料口、通气口、把手均位于发酵罐的外表面上。The thermometer port, the acid and alkali liquid addition port, the pH meter port, the nutrient feeding port, the ventilation port and the handle are all located on the outer surface of the fermenter.

所述的发酵罐为任意形状。The fermenter has any shape.

所述的模具的材料为玻璃、陶瓷、紫砂、金属、硅胶、木材、纤维素、橡胶、涤纶、尼龙(Nylon)、奥纶(Orlon)、聚乙烯醇(PVA)、聚乙烯乙醇(Ivalon)、涤纶(Dacron)、特氟纶(Teflon)、膨体聚四氟乙烯(ePTFE)和真丝等高分子材料以及塑料等无机有机材料的一种或几种组合。The material of the mold is glass, pottery, purple sand, metal, silica gel, wood, cellulose, rubber, polyester, nylon (Nylon), Orlon (Orlon), polyvinyl alcohol (PVA), polyvinyl alcohol (Ivalon) , polyester (Dacron), Teflon (Teflon), expanded polytetrafluoroethylene (ePTFE) and silk and other polymer materials, as well as one or more combinations of inorganic organic materials such as plastics.

本发明的一种动态制备异型空腔细菌纤维素材料的方法,包括:A kind of method for dynamically preparing special-shaped cavity bacterial cellulose material of the present invention comprises:

(1)菌种培养(1) Bacteria culture

将细菌纤维素生产菌株接入液体培养基扩培,于20-30℃、100-250r/min条件下摇床培养或者静置培养12~48h后备用;Insert the bacterial cellulose production strain into the liquid medium for expansion, and cultivate it on a shaking table under the conditions of 20-30°C and 100-250r/min or static culture for 12-48 hours before use;

(2)异性空腔BC材料的发酵制备(2) Fermentation preparation of heterosexual cavity BC material

将步骤(1)制备的含生产菌株的液体培养基转移到上述发酵装置中,然后旋转模具以3-20rpm的转速进行扰动培养,于20~32℃动态培养4-20天后,即可收获空腔异形纤维素材料;Transfer the liquid culture medium containing the production strain prepared in step (1) to the above-mentioned fermentation device, then rotate the mold at a speed of 3-20rpm to carry out disturbed culture, and after dynamic culture at 20-32°C for 4-20 days, you can harvest the empty lumen profiled cellulose material;

(3)材料处理(3) Material handling

将制备的中空异形细菌纤维素材料从模具上取下,然后浸泡于0.5~2wt%的NaOH溶液中,70-100℃水浴处理30-120min,使细菌纤维素材料呈白色半透明后即可;然后洗涤至中性,即得异形细菌纤维素产品。Remove the prepared hollow special-shaped bacterial cellulose material from the mold, soak it in 0.5-2wt% NaOH solution, and treat it in a water bath at 70-100°C for 30-120 minutes, so that the bacterial cellulose material is white and translucent; Then wash until neutral to obtain the special-shaped bacterial cellulose product.

所述步骤(1)中的BC生产菌株为醋酸菌属(Acetobacter sp.)、葡萄糖酸杆菌属(Gluconobacter sp.)、葡糖酸醋杆菌属(Gluconacetobacter sp.)、根瘤菌属(Rhizobium sp.)、八叠球菌属(Sarcina sp.)、假单胞菌属(Pseudomounas sp.)、无色杆菌属(Achromobactersp.)、产碱菌属(Alcaligenes sp.)、气杆菌属(Aerobacter sp.)、固氮菌属(Azotobacter sp.)、土壤杆菌属(Agrobacterium sp.)、洋葱假单胞菌(Seudomonas cepacia)、空肠弯曲菌(Campylobacter jejuni)或红茶菌(kombucha);其中优选菌株为木醋杆菌(Acetobacterxylinum)或红茶菌;The BC production strains in the step (1) are Acetobacter sp., Gluconobacter sp., Gluconacetobacter sp., Rhizobium sp. ), Sarcina sp., Pseudomounas sp., Achromobacter sp., Alcaligenes sp., Aerobacter sp. , Azotobacter sp., Agrobacterium sp., Seudomonas cepacia, Campylobacter jejuni or kombucha; wherein the preferred strain is Acetobacter xylinum (Acetobacterxylinum) or kombucha;

其中,除红茶菌以外的菌种按2~3接种环的接种量接入液体种子培养基;红茶菌按接入1-10片直径0.5cm圆片含菌BC膜的接种量接入液体种子培养基;Among them, the strains other than kombucha are inserted into the liquid seed medium according to the inoculation amount of 2 to 3 inoculation loops; Culture medium;

或者先制备生产菌的液体种子,再转接入液体发酵培养基;除红茶菌以外的菌种按2~3接种环的接种量接入液体种子培养基制备种子液,然后按3vol%~20vol%的接种量转接到液体发酵培养基;红茶菌按接入1-10片直径0.5cm圆片含菌BC膜的接种量接入液体种子培养基,以及按1~10片直径0.5-1cm圆片含菌BC膜的接种量转接到液体发酵培养基。Or prepare the liquid seeds of the production bacteria first, and then transfer them to the liquid fermentation medium; the strains other than kombucha are inserted into the liquid seed medium to prepare the seed liquid according to the inoculation amount of 2 to 3 inoculation loops, and then press 3vol% to 20vol % of the inoculum is transferred to the liquid fermentation medium; kombucha is inserted into the liquid seed medium according to the inoculum of 1-10 discs with a diameter of 0.5cm containing bacteria BC film, and 1-10 discs with a diameter of 0.5-1cm The inoculum of the disc containing bacteria BC membrane was transferred to the liquid fermentation medium.

所述的除了红茶菌以外的液体种子培养基和液体发酵培养基的组分均为:每1L水中,甘露醇、葡萄糖、麦芽糖、蔗糖或果糖20-200g、蛋白胨或胰蛋白胨3g、酵母浸膏5g,pH3.0-7.5,121℃灭菌20min;或甘露醇、葡萄糖、蔗糖或果糖20-200g,酵母浸膏5g,蛋白胨或胰蛋白胨5g,柠檬酸115g,Na2HPO42.7g,水1L,pH3.0-7.5,121℃灭菌20min;The components of the liquid seed culture medium and liquid fermentation medium other than kombucha are: per 1L of water, 20-200g of mannitol, glucose, maltose, sucrose or fructose, 3g of peptone or tryptone, yeast extract 5g, pH3.0-7.5, sterilized at 121°C for 20min; or mannitol, glucose, sucrose or fructose 20-200g, yeast extract 5g, peptone or tryptone 5g, citric acid 115g, Na 2 HPO 4 2.7g, water 1L, pH3.0-7.5, sterilized at 121°C for 20min;

红茶菌液体种子培养基和液体发酵培养基,其组成均为:(1)每1L水中,绿茶或者红茶1-10g(茶叶5g时最优),葡萄糖、蔗糖或者果糖10~200g、蛋白胨或者胰蛋白胨3g、酵母浸膏5g,pH3.0-7.5,巴氏灭菌30min;(2)将葡萄糖、蔗糖或果糖、绿茶或红茶、以及水配成培养基,其中糖、茶、水的质量比为5∶0.1-0.4∶100-200,pH3.0-7.5,巴氏灭菌30min;或者(3)每1L水中,甘露醇、葡萄糖、蔗糖或果糖20-200g、蛋白胨或胰蛋白胨3g、酵母浸膏5g,pH3.0-7.5,121℃灭菌20min;其中,最优培养基为(1)的配方。Kombucha liquid seed medium and liquid fermentation medium are composed of: (1) per 1L of water, 1-10g of green tea or black tea (5g of tea leaves is optimal), 10-200g of glucose, sucrose or fructose, peptone or tryptone 3g of peptone, 5g of yeast extract, pH3.0-7.5, pasteurized for 30min; (2) Glucose, sucrose or fructose, green tea or black tea, and water are made into a medium, wherein the mass ratio of sugar, tea, and water 5:0.1-0.4:100-200, pH3.0-7.5, pasteurized for 30 minutes; or (3) per 1L of water, mannitol, glucose, sucrose or fructose 20-200g, peptone or tryptone 3g, yeast Extract 5g, pH 3.0-7.5, sterilized at 121°C for 20 minutes; among them, the optimal medium is the formula of (1).

所述步骤(2)中的含生产菌株的液体培养基为步骤(1)制备的含生产菌株的液体种子培养基或含生产菌株的液体发酵培养基。The liquid medium containing the production strain in the step (2) is the liquid seed medium containing the production strain prepared in step (1) or the liquid fermentation medium containing the production strain.

此外,为加速在模具上形成纤维素膜,可以在转轴或模具内腔中注入含氧量为1-100vol%的空气,当含氧量为100vol%时,通入的是纯氧。In addition, in order to accelerate the formation of cellulose film on the mould, air with an oxygen content of 1-100 vol% can be injected into the rotating shaft or the inner cavity of the mould. When the oxygen content is 100 vol%, pure oxygen is introduced.

目前已有的BC中空异形材料的制备技术一般采用单层透氧模具制备,效率低且外表面或者内表面粗糙,本发明利用细菌纤维素在液体中易缠绕的特性,在水平扰动的生物反应器中,通过转盘上模具围绕着转轴轴心的转动,使得模具在液体培养基中进行缓慢且循环浸没的扰动培养方式,缠绕和吸附发酵液中的细菌纤维素而在模具表面形成一定形状的中空细菌纤维素材料。The existing technology for preparing BC hollow special-shaped materials generally adopts a single-layer oxygen-permeable mold, which is low in efficiency and has rough outer or inner surfaces. In the container, the mold rotates around the axis of the rotating shaft on the turntable, so that the mold is slowly and cyclically submerged in the liquid culture medium, and the bacterial cellulose in the fermentation broth is entangled and adsorbed to form a certain shape on the surface of the mold. Hollow bacterial cellulose material.

由于是亚静态培养(转轴的转速很缓慢,<20rpm,菌体在亚静态的环境下生长),可以使模具在液体培养基和含氧介质中不停地交替,既给液体培养基提供足够的溶解氧,促进液体中菌体的快速繁殖和产生纤维素,从而利于模具的缠绕;又有利于已固定在模具上的纤维素膜中的菌体可以接触到营养,同时使得菌体充分接触氧,从而促使菌体大量繁殖和分泌纤维素,高效制备细菌纤维素材料。多种因素促使生产效率大大提升。Because it is a substatic culture (the rotation speed of the rotating shaft is very slow, <20rpm, and the bacteria grow in a substatic environment), the mold can be continuously alternated in the liquid medium and the oxygen-containing medium, which not only provides enough for the liquid medium The dissolved oxygen in the liquid promotes the rapid reproduction of bacteria in the liquid and the production of cellulose, which is beneficial to the winding of the mold; it also helps the bacteria in the cellulose film fixed on the mold to have access to nutrients, and at the same time allows the bacteria to fully contact Oxygen, thereby promoting the proliferation of bacterial cells and secreting cellulose, and efficiently preparing bacterial cellulose materials. A variety of factors contributed to the dramatic increase in production efficiency.

根据所需制备的BC材料的尺寸和形状,选择合适的模具材料,制备出横截面形状为圆形、方形、椭圆形、三角形、心形、五角星形等异形BC材料。According to the size and shape of the BC material to be prepared, select the appropriate mold material to prepare special-shaped BC materials with cross-sectional shapes such as circles, squares, ellipses, triangles, hearts, and five-pointed stars.

本发明制备得到异型空腔细菌纤维素材料作为一种新型纳米生物材料不仅可以用于人工血管、覆盖神经纤维的护套,还可用于人造气管、输尿管、组织工程支架、人工皮肤、脑膜,以及某些中空器官的替代品;或者可作为一种可食用的食品包裹材料(如肉制品肠衣、果冻外衣等)等,具有非常广阔的应用范围和美好的应用前景。The special-shaped hollow bacterial cellulose material prepared by the present invention can be used as a new type of nano-biological material not only for artificial blood vessels and sheaths covering nerve fibers, but also for artificial trachea, ureter, tissue engineering scaffolds, artificial skin, meninges, and It can be used as a substitute for certain hollow organs; or it can be used as an edible food wrapping material (such as meat casings, jelly casings, etc.), and has a very broad application range and bright application prospects.

有益效果Beneficial effect

(1)本发明制备的异型空腔BC材料相较于其他物理化学的方法,保留了其独特的三维网状纳米结构、高化学纯度、高结晶度、高聚合度、高强度以及良好的生物相容性等优点;且制备方法简便易行,成本低廉,生产效率高,适合大规模工业化生产;(1) Compared with other physical and chemical methods, the special-shaped cavity BC material prepared by the present invention retains its unique three-dimensional network nanostructure, high chemical purity, high crystallinity, high degree of polymerization, high strength and good biological properties. Compatibility and other advantages; and the preparation method is simple and easy, low cost, high production efficiency, suitable for large-scale industrial production;

(2)本发明制备的异型空腔BC材料的长度、内径、厚度等尺寸和形状均不受限制,可以人工调控,而且材料内外均具有光滑平整的表面;(2) The length, inner diameter, thickness and other sizes and shapes of the special-shaped cavity BC material prepared by the present invention are not limited, can be manually regulated, and the inside and outside of the material have smooth and even surfaces;

(3)发酵装置的模具可拆卸,重复使用,所制备的各种异形BC材料可以在表面毫无损伤的情况下剥离出来;为了进一步提高异形BC材料的制备效率,在水平生物反应器中可配备多个模具以提高产量。(3) The mold of the fermentation device can be disassembled and reused, and the prepared various special-shaped BC materials can be peeled off without any damage on the surface; in order to further improve the preparation efficiency of the special-shaped BC materials, the horizontal bioreactor can Equipped with multiple molds to increase production.

附图说明 Description of drawings

图1a为制备管状细菌纤维素材料的发酵装置示意图1,其中模具为棍子或者管子,模具内腔可以充满氧气或空气;Figure 1a is a schematic diagram 1 of a fermentation device for preparing tubular bacterial cellulose materials, wherein the mold is a stick or a pipe, and the cavity of the mold can be filled with oxygen or air;

图1b为制备手形细菌纤维素材料的发酵装置示意图2,其中模具为手形,模具内腔可以充满氧气或空气;Figure 1b is a schematic diagram 2 of a fermentation device for preparing hand-shaped bacterial cellulose materials, wherein the mold is hand-shaped, and the cavity of the mold can be filled with oxygen or air;

图2为用于制备管状细菌纤维素材料的转盘结构设计模型;Fig. 2 is the design model of the turntable structure for preparing tubular bacterial cellulose material;

图3为不同棒状模具材料制备得到的细菌纤维素结果,上为硅胶棒,中为木棒,下为磨砂玻璃棒;Figure 3 shows the results of bacterial cellulose prepared from different rod-shaped mold materials, the top is a silica gel rod, the middle is a wooden rod, and the bottom is a frosted glass rod;

图4为制备管状细菌纤维素材料的配备磨砂玻璃棒模具的发酵装置实拍图;Fig. 4 is the real photo of the fermentation device equipped with frosted glass rod molds for preparing tubular bacterial cellulose materials;

图5为发酵5-7天制备的管形细菌纤维素材料的实物图;Fig. 5 is the actual picture of the tubular bacterial cellulose material prepared by fermentation for 5-7 days;

图6为发酵5天制备的管形细菌纤维素材料的电镜图;其中A为外表面,B为内表面,C为与管中心轴方向垂直截面(横截面),D为沿管中心轴方向截面(纵截面);Figure 6 is an electron microscope image of the tube-shaped bacterial cellulose material prepared by fermentation for 5 days; wherein A is the outer surface, B is the inner surface, C is a section (cross section) perpendicular to the direction of the central axis of the tube, and D is the direction along the central axis of the tube Section (longitudinal section);

图8为发酵1~8天制备的细菌纤维素管沿管中心轴方向测试的绝对拉力(轴向拉力)随时间变化的曲线图;Fig. 8 is a graph showing the absolute tensile force (axial tensile force) of bacterial cellulose tubes tested along the direction of the central axis of the tube as a function of time for 1 to 8 days of fermentation;

图9为发酵1~8天制备的细菌纤维素管沿与管中心轴垂直方向测试的绝对拉力(径向拉力)和相对干重拉力随时间变化的曲线图。Fig. 9 is a graph showing the absolute tensile force (radial tensile force) and the relative dry weight tensile force over time of bacterial cellulose tubes prepared by fermentation for 1-8 days along the direction perpendicular to the central axis of the tube.

具体实施方式 Detailed ways

下面结合具体实施例,进一步阐述本发明。应理解,这些实施例仅用于说明本发明而不用于限制本发明的范围。此外应理解,在阅读了本发明讲授的内容之后,本领域技术人员可以对本发明作各种改动或修改,这些等价形式同样落于本申请所附权利要求书所限定的范围。Below in conjunction with specific embodiment, further illustrate the present invention. It should be understood that these examples are only used to illustrate the present invention and are not intended to limit the scope of the present invention. In addition, it should be understood that after reading the teachings of the present invention, those skilled in the art can make various changes or modifications to the present invention, and these equivalent forms also fall within the scope defined by the appended claims of the present application.

以管状BC材料的制备为例Taking the preparation of tubular BC materials as an example

实施例1Example 1

1.发酵装置的设计组装1. Design and assembly of fermentation equipment

1.1设计思想1.1 Design thinking

由于Acetobacterxylinum属于好氧性细菌,在长期的发酵代谢过程中需要大量的氧气,细菌纤维素的生长属于吸附式生长并且必须要有培养基的支持,因此要让细菌纤维素按照一定的形状生长成形,细菌纤维素就必须在特定形状的模具材料上进行好氧生长。如果要制备的细菌纤维素材料为管状材料,则要考虑采用棍形、棒形或管状模具,不仅让细菌纤维素在这些模具上生长,而且还必须提供足够的氧气,为此我们设计了采用一个配备棍形模具的水平生物反应器,让模具在液体培养基中进行缓慢循环反复浸没的方式进行扰动培养,这样培养基中产生细菌纤维素就可以缠绕吸附在模具上,时而浸没在培养基中补充营养,时而暴露在空气或氧气中的循环反复操作,直到培养形成所需的管状细菌纤维素材料。为加快以固定在模具上菌体的生长和合成分泌纤维素,模具中充满1-100%氧气或者空气有很大帮助。Since Acetobacterxylinum belongs to aerobic bacteria, it needs a lot of oxygen in the long-term fermentation and metabolism process. The growth of bacterial cellulose belongs to adsorption growth and must be supported by the medium. Therefore, the bacterial cellulose must be grown in a certain shape. , bacterial cellulose must be grown aerobically on a mold material of a specific shape. If the bacterial cellulose material to be prepared is a tubular material, stick-shaped, rod-shaped or tubular molds should be considered, not only to allow the bacterial cellulose to grow on these molds, but also to provide sufficient oxygen. For this reason, we have designed a A horizontal bioreactor equipped with a stick-shaped mold, which allows the mold to be slowly circulated and repeatedly submerged in the liquid medium for disturbed culture, so that the bacterial cellulose produced in the medium can be wound and adsorbed on the mold, and sometimes submerged in the medium The cycle of supplementing nutrients in the medium and exposing to air or oxygen is repeated until the desired tubular bacterial cellulose material is formed in the culture. In order to speed up the growth and synthesis and secretion of cellulose fixed on the mold, it is very helpful to fill the mold with 1-100% oxygen or air.

1.2水平扰动生物反应器的结构特点1.2 Structural characteristics of horizontal disturbance bioreactor

反应器由上下两个半圆柱体或其它形状的玻璃容器组成,生物反应器的体积为1000mL,有效体积为500mL,转盘由电机带动,反应器的装液量为300-350mL,设备示意图如图1a-b所示:顶部开有直径为1cm大小的开口,分别进行温度,通气和补料操作。反应器中发酵液浸没转盘的2/5左右,确保当某根棍形模具旋转达到最低端时,整个模具可以完全浸没在发酵液中。The reactor is composed of upper and lower half cylinders or glass containers of other shapes. The volume of the bioreactor is 1000mL, the effective volume is 500mL, the turntable is driven by a motor, and the liquid volume of the reactor is 300-350mL. The schematic diagram of the equipment is shown in the figure As shown in 1a-b: there is an opening with a diameter of 1cm on the top, and the temperature, ventilation and feeding operations are performed respectively. The fermented liquid in the reactor is immersed in about 2/5 of the turntable to ensure that when a stick-shaped mold rotates to the lowest end, the entire mold can be completely submerged in the fermented liquid.

1.3生物反应器的转盘结构设计1.3 Turntable structure design of bioreactor

利用模具进行一定转速的旋转,将细菌纤维素缠绕在模具上,因此本实验的最重要的部件在转盘固定的棒状模具上。The mold is rotated at a certain speed, and the bacterial cellulose is wound on the mold. Therefore, the most important part of this experiment is on the rod-shaped mold fixed on the turntable.

采用两种不同类型结构的转盘,一种为模具夹在两个转盘之间,另一个为转盘都在模具一端,另一端留出一定长度的模具(见图2),所需要的管状细菌纤维素主要生长缠绕于模具上,两个转盘主要对模具起支撑作用。Two different types of turntables are used, one is that the mold is clamped between two turntables, the other is that the turntable is at one end of the mold, and the other end leaves a certain length of mold (see Figure 2), the required tubular bacterial fiber The element mainly grows and winds on the mold, and the two turntables mainly support the mold.

1.4反应器转盘和棒形模具材料的筛选1.4 Screening of reactor turntable and rod mold materials

考虑到本试验制备的是管状细菌纤维素材料,所以转盘圆片由无毒的聚乙烯塑料片或其它无毒性的材料组成,转轴则由玻璃棒或不锈钢棒等有一定刚性的材料组成。由于考虑到模具材料的毒性、对细菌纤维素的吸附性、机械强度以及加工的难易程度等因素,因此可以是玻璃、陶瓷、紫砂、金属、硅胶、木材、纤维素、橡胶、涤纶、尼龙(Nylon)、奥纶(Orlon)、聚乙烯醇(PVA)、聚乙烯乙醇(Ivalon)、涤纶(Dacron)、特氟纶(Teflon)、膨体聚四氟乙烯(ePTFE)和真丝等高分子材料以及塑料等无机有机材料的一种或几种组合。本实验重点选择了木质、玻璃、硅胶进行研究。将三种不同类型的材料分别装在转盘上,进行培养,观察纤维素的生长成形情况(见图3)。实验结果表明在相同天数内,形成的管状材料由厚到薄依次为木棒、磨砂玻璃棒、硅胶管。以磨砂玻璃棒为模具的生物反应器实拍图见图4。制备得到的不同尺寸的细菌纤维素管实物图见图5。Considering that the tube-shaped bacterial cellulose material is prepared in this test, the turntable disc is composed of non-toxic polyethylene plastic sheet or other non-toxic materials, and the rotating shaft is composed of glass rods or stainless steel rods and other rigid materials. Due to the consideration of the toxicity of the mold material, the adsorption of bacterial cellulose, the mechanical strength and the ease of processing, it can be glass, ceramics, purple sand, metal, silica gel, wood, cellulose, rubber, polyester, nylon (Nylon), Orlon (Orlon), polyvinyl alcohol (PVA), polyvinyl alcohol (Ivalon), polyester (Dacron), Teflon (Teflon), expanded polytetrafluoroethylene (ePTFE) and silk and other polymers One or more combinations of materials and inorganic organic materials such as plastics. This experiment focuses on choosing wood, glass, and silica gel for research. Three different types of materials were placed on the turntables respectively, cultured, and the growth and shape of the cellulose were observed (see Figure 3). The experimental results show that within the same number of days, the tubular materials formed are wooden rods, frosted glass rods, and silicone tubes in order from thick to thin. See Figure 4 for the real photo of the bioreactor with the frosted glass rod as the mold. The physical pictures of the prepared bacterial cellulose tubes of different sizes are shown in Fig. 5 .

实施例2Example 2

如图1所示,一种动态制备异型空腔细菌纤维素材料的装置,一种简便高效动态生产异型空腔细菌纤维素材料的发酵装置,包括温度计口1,酸液碱液添加口2,把手3,通气口4,pH计口5,营养补料口6,转轴8,发酵罐9,马达10,水浴装置11,模具,其特征是:所述的转轴8一端连接固定马达10输出轴,转轴8另一端从发酵罐9一端面中心位置伸入发酵罐9内;在发酵罐9内的转轴8上固定有模具。As shown in Figure 1, a device for dynamically preparing bacterial cellulose materials with special-shaped cavities, a simple and efficient fermentation device for dynamically producing bacterial cellulose materials with special-shaped cavities, including a thermometer port 1, an acid and alkali liquid addition port 2, Handle 3, ventilation port 4, pH meter port 5, nutrient feeding port 6, rotating shaft 8, fermentation tank 9, motor 10, water bath device 11, mold, characterized in that: one end of the rotating shaft 8 is connected to the output shaft of the fixed motor 10 The other end of the rotating shaft 8 extends into the fermenting tank 9 from the center of one end of the fermenting tank 9; a mold is fixed on the rotating shaft 8 in the fermenting tank 9.

模具12的材料选自玻璃、陶瓷、紫砂、金属、硅胶、木材、纤维素、橡胶、涤纶、尼龙、奥纶、聚乙烯醇、聚乙烯乙醇、涤纶、特氟纶、膨体聚四氟乙烯、真丝、塑料中的一种或几种组合。The material of mold 12 is selected from glass, pottery, purple sand, metal, silica gel, wood, cellulose, rubber, polyester, nylon, Orlon, polyvinyl alcohol, polyvinyl alcohol, polyester, Teflon, expanded polytetrafluoroethylene , silk, plastic in one or a combination of several.

转轴8在发酵罐9内腔靠近发酵罐9一端面一侧安装固定有转盘7,转轴8通过转盘7圆周边缘对称固定有棍形管形模具12,且棍形管形模具12为实心或中空结构。The rotating shaft 8 is installed and fixed with a turntable 7 on the inner cavity of the fermenter 9 close to one end of the fermenter 9, and the rotating shaft 8 is symmetrically fixed with a stick-shaped tubular mold 12 through the periphery of the turntable 7, and the stick-shaped tubular mold 12 is solid or hollow. structure.

温度计口1、酸液碱液添加口2、pH计口5、营养补料口6、通气口4、把手3均位于发酵罐9的外表面上。Thermometer port 1, acid liquid alkali liquid addition port 2, pH meter port 5, nutrient feeding port 6, ventilation port 4, and handle 3 are all located on the outer surface of fermenter 9.

棍形管形模具12的横截面形状为圆形、方形、椭圆形、三角形、心形或五角星形。The cross-sectional shape of the stick-shaped tubular mold 12 is circular, square, elliptical, triangular, heart-shaped or five-pointed star-shaped.

使用时,通过将含生产菌株的液体培养基转移到本实用新型的发酵装置中,然后旋转模具以3-20rpm的转速进行扰动培养,即可收获空腔异形纤维素材料。When in use, by transferring the liquid culture medium containing the production strains to the fermentation device of the present invention, and then rotating the mold at a speed of 3-20rpm for disturbing culture, the cavity special-shaped cellulose material can be harvested.

实施例3Example 3

如图2所示,本实施例与实施例2的区别仅在于:As shown in Figure 2, the difference between this embodiment and embodiment 2 is only:

(1)模具的形状不同,本实施例中模具为手套形模具12,且手套形模具12为实心或中空结构,手套形模具12的横截面形状为圆形、方形、椭圆形、三角形、心形或五角星形;(1) The shape of the mold is different. In the present embodiment, the mold is a glove-shaped mold 12, and the glove-shaped mold 12 is a solid or hollow structure. The cross-sectional shape of the glove-shaped mold 12 is circular, square, oval, triangle, heart shape or pentagram;

(2)本实施例的装置中不需要转盘对手套形模具进行固定,只需在转轴上依次穿入1个以上手套形模具即可。(2) In the device of the present embodiment, there is no need for the turntable to fix the glove-shaped molds, and only one or more glove-shaped molds need to be inserted sequentially on the rotating shaft.

实施例4Example 4

本实施例与实施例2的区别仅在于:The difference between this embodiment and embodiment 2 only lies in:

模具的形状不同,本实施例中模具为手套形模具12,且转轴8通过转盘7圆周边缘对称固定有2个以上手套形模具;手套形模具12为实心或中空结构,手套形模具12的横截面形状为圆形、方形、椭圆形、三角形、心形或五角星形。The shapes of the moulds are different. In the present embodiment, the mold is a glove-shaped mold 12, and the rotating shaft 8 is symmetrically fixed with more than two glove-shaped moulds; the glove-shaped mold 12 is a solid or hollow structure. The cross-sectional shape is round, square, oval, triangular, heart-shaped or pentagram.

实施例5Example 5

(1)菌种培养(1) Bacteria culture

将木醋杆菌(Acetobacter xylinum)接入300mL液体培养基(本实施例以下面培养基配方为例:每1L水中,甘露醇、葡萄糖、麦芽糖、蔗糖或果糖20-200g、蛋白胨或胰蛋白胨3g、酵母浸膏5g,pH3.0-7.5,121℃灭菌20min;或甘露醇、葡萄糖、蔗糖或果糖20-200g,酵母浸膏5g,蛋白胨或胰蛋白胨5g,柠檬酸115g,Na2HPO42.7g,水1L,pH3.0-7.5,121℃灭菌20min)扩培,于20-30℃、100-250r/min条件下摇床培养或者静置培养12~48h后备用;Acetobacter xylinum (Acetobacter xylinum) was inserted into 300mL liquid culture medium (this embodiment takes the following culture medium formula as example: every 1L of water, mannitol, glucose, maltose, sucrose or fructose 20-200g, peptone or tryptone 3g, Yeast extract 5g, pH3.0-7.5, sterilized at 121°C for 20min; or mannitol, glucose, sucrose or fructose 20-200g, yeast extract 5g, peptone or tryptone 5g, citric acid 115g, Na 2 HPO 4 2.7 g, water 1L, pH 3.0-7.5, sterilized at 121°C for 20 minutes) for expansion, cultured on a shaking table at 20-30°C, 100-250r/min or standing for 12-48 hours before use;

(2)中空异形细菌纤维素材料的发酵制备(2) Fermentation preparation of hollow shaped bacterial cellulose material

将步骤(1)制备的含生产菌株的液体培养基转移到配备有棒状模具的生物反应器中,然后旋转模具以7、15、30和60rpm的转速进行扰动培养,于30℃动态培养4-20天后,即可收获空腔异形纤维素材料;The liquid medium containing the production strain prepared in step (1) was transferred to a bioreactor equipped with a rod-shaped mold, and then the mold was rotated to disturb the cultivation at a speed of 7, 15, 30 and 60 rpm, and the 4- After 20 days, the cavity shaped cellulose material can be harvested;

或者取步骤(1)活化好的菌种以10%的接种量接入到300mL发酵培养基中,置于500mL锥形瓶中,在30℃和160rpm的条件下培养4小时,然后再将发酵液转移到生物反应器中,然后旋转模具以7、15、30和60rpm的转速进行扰动培养,于30℃条件下分别培养不同的天数,制备得到不同厚度的管状细菌纤维素材料。Or get the activated bacterial classification of step (1) to insert in 300mL fermentation medium with 10% inoculum size, place in 500mL Erlenmeyer flask, cultivate 4 hours under the condition of 30 ℃ and 160rpm, then ferment The solution was transferred to the bioreactor, and then the mold was rotated to disturb the culture at the speed of 7, 15, 30 and 60rpm, and cultured at 30°C for different days to prepare tubular bacterial cellulose materials with different thicknesses.

该发酵装置由一个水平搅拌反应器和在转盘上固定若干棍状模具的转轴组成,形成了一个水平扰动的生物反应器。通过转盘上模具围绕着转轴轴心的转动,使得模具缠绕发酵液中的细菌纤维素而在模具表面形成一定形状的中空细菌纤维素材料。The fermentation device is composed of a horizontal stirring reactor and a rotating shaft on which several stick-shaped molds are fixed on a turntable, forming a horizontally disturbed bioreactor. Through the rotation of the mold on the turntable around the axis of the rotating shaft, the mold wraps the bacterial cellulose in the fermentation broth to form a hollow bacterial cellulose material of a certain shape on the surface of the mold.

由于木醋杆菌属于好氧性微生物且对外界的剪切力敏感,因此,在对生物反应器设计时不仅要考虑氧气的供应,而且还要考虑剪切力(即转速)对菌体和细菌纤维素缠绕成形的影响,本实验分别选取了7、15、30、60rpm四个较低的转速,研究转速对纤维素成形的影响。Since Acetobacter xylinum is an aerobic microorganism and is sensitive to external shear force, it is not only necessary to consider the supply of oxygen, but also to consider the impact of shear force (ie rotational speed) on the bacteria and bacteria when designing the bioreactor. For the influence of cellulose winding forming, four lower rotational speeds of 7, 15, 30, and 60rpm were selected in this experiment to study the influence of rotational speed on cellulose forming.

表1转速对管状材料成形的影响Table 1 Effect of rotational speed on the forming of tubular materials

由表1可知,在7rpm和15rpm时,管状材料可以成形,而当增加到30rpm或者以上的时候,管状材料较难形成。当转速为7rpm时,发酵过程中在生物反应器底部会有较多类似凝胶状的纤维素形成,而在转速为15rpm以及更高时形成较少。这是由于当转速较慢时,生物反应器内剪切力不足,导致纤维素聚集在一起,纤维素的聚集对于管状材料的成形是不利的。It can be seen from Table 1 that at 7rpm and 15rpm, the tubular material can be formed, but when it is increased to 30rpm or above, the tubular material is difficult to form. When the rotational speed was 7rpm, more gel-like cellulose was formed at the bottom of the bioreactor during the fermentation process, but less when the rotational speed was 15rpm and higher. This is because when the rotational speed is low, the shear force in the bioreactor is insufficient, resulting in the aggregation of cellulose, and the aggregation of cellulose is unfavorable for the shaping of the tubular material.

(3)材料处理(3) Material handling

将制备的空腔异形BC材料从模具上取下,蒸馏水多次冲洗后,然后浸泡于0.5~2wt%的NaOH溶液中,70-100℃水浴处理30-120min,使BC管状材料呈白色半透明后即可,先用含0.5mol/L的醋酸的水溶液洗涤4~5次,再用纯水反复洗涤至中性,然后冷藏,即得异形细菌纤维素产品。Remove the prepared cavity special-shaped BC material from the mold, rinse it with distilled water several times, then soak it in 0.5-2wt% NaOH solution, and treat it in a water bath at 70-100°C for 30-120min, so that the BC tubular material is white and translucent After that, it can be washed with an aqueous solution containing 0.5mol/L acetic acid for 4 to 5 times, then repeatedly washed with pure water until neutral, and then refrigerated to obtain the special-shaped bacterial cellulose product.

(4)管状BC材料的表征(4) Characterization of tubular BC materials

A、管状细菌纤维素的扫描电镜观察A. Scanning electron microscope observation of tubular bacterial cellulose

对冷冻干燥得到的样品分别进行管外表面、管内表面、与管中心轴方向垂直截面(横截面),沿管中心轴方向截面(纵截面)四个部分的扫描电镜(SEM)观察(图6)。The samples obtained by freeze-drying were respectively subjected to scanning electron microscope (SEM) observation of four parts: the outer surface of the tube, the inner surface of the tube, the section perpendicular to the direction of the central axis of the tube (cross section), and the section along the direction of the central axis of the tube (longitudinal section) (Fig. 6 ).

由管状细菌纤维素的电镜扫描照片可以看出,木醋杆菌动态合成的细菌纤维素与静态制备的膜一样具有超微网络结构,由高密度微纤维互相交联形成。照片中显示,外表面具有相对规则的走势,但不明显。从图(6A)中可以看到细菌纤维素的生长有向着某个方向延伸的趋势。在图(6B)管状细菌纤维素的内表面SEM照片中可以发现,纤维素的生长方向基本无规律性,这个可能是前期细菌纤维素的生长主要是靠吸附生长在玻璃柱上,生长不规则。由管状细菌纤维素材料的横截面和纵截面的电镜照片(图6C和6D)可以看出,纤维素的生长具有明显的规律性,纤维素向着某个方向交织生长,纤维素的每一层之间也有交织,形成了一个空间立体的网状结构,这个结果与静态培养的管状纤维素材料明显不同,在静态培养下细菌纤维素的截面电镜明显出现分层现象。而本实验的动态法制备的管状材料没有出现分层。From the scanning electron microscope photos of tubular bacterial cellulose, it can be seen that the bacterial cellulose dynamically synthesized by Acetobacter xylinum has the same ultra-fine network structure as the statically prepared film, which is formed by cross-linking high-density microfibers. As shown in the photographs, the outer surface has relatively regular but indistinct trends. It can be seen from Figure (6A) that the growth of bacterial cellulose tends to extend in a certain direction. In the SEM photo of the inner surface of the tubular bacterial cellulose in Figure (6B), it can be found that the growth direction of the cellulose is basically irregular. This may be that the growth of the bacterial cellulose in the early stage was mainly grown on the glass column by adsorption, and the growth was irregular. . From the electron micrographs of the cross-section and longitudinal section of the tubular bacterial cellulose material (Figure 6C and 6D), it can be seen that the growth of cellulose has obvious regularity, and the cellulose grows intertwined in a certain direction, and each layer of cellulose There is also interweaving among them, forming a three-dimensional network structure, which is obviously different from the static cultured tubular cellulose material, and the cross-sectional electron microscope of bacterial cellulose under static culture clearly shows layering. However, the tubular material prepared by the dynamic method in this experiment did not appear delamination.

B、X-射线衍射分析B. X-ray diffraction analysis

采用日本RIGAKU公司X-射线衍射仪对静态膜试样和动态管试样进行X-射线衍射分析。经计算得静态发酵制备的细菌纤维素膜的结晶度为86.54%,动态发酵制备的细菌纤维素管的结晶度为89.36%。The X-ray diffraction analysis of the static film sample and the dynamic tube sample was carried out by using the X-ray diffractometer of Japan RIGAKU Company. It is calculated that the crystallinity of the bacterial cellulose film prepared by static fermentation is 86.54%, and the crystallinity of the bacterial cellulose tube prepared by dynamic fermentation is 89.36%.

C、力学性能测定C. Determination of mechanical properties

将制备得到的管状细菌纤维素,利用万能材料测试仪分别进行轴向和径向的强力测试。(A)轴向强力测试(图7):将样品切成4cm长的管状,设定两夹头之间的夹距为3cm,移动速率为100mm/min,测试机的探头最大测定强力为10N。(B)径向强力测试(图7):将样品切成1cm长的管状,采用两个U型铁丝(直径为3mm)穿过BC管,设定两夹头之间的夹距为5cm,移动速率为100mm/min。测试机的探头最大测定强力为10N。The prepared tubular bacterial cellulose was subjected to axial and radial strength tests using a universal material tester. (A) Axial strength test (Figure 7): Cut the sample into a 4cm-long tube, set the clamping distance between the two chucks to 3cm, the moving speed to 100mm/min, and the maximum measuring strength of the probe of the testing machine to be 10N . (B) Radial strength test (Fig. 7): the sample is cut into a 1cm long tube, using two U-shaped iron wires (diameter 3mm) through the BC tube, set the clamping distance between the two chucks to 5cm, and the moving speed to 100mm/min. The maximum measuring strength of the probe of the testing machine is 10N.

图8显示反应器发酵制备的材料轴向强力随着培养天数的增加不断提高,这是由于随着培养天数的增加,细菌纤维素的厚度也会随之增加,生成的纤维素的量也更多。通过过程观察可以发现,管状材料的生长速率是随着细菌纤维素在玻璃棒上的缠绕逐渐加快的。在第一天时纤维素的缠绕量比较少,但是一天后,当玻璃棒上缠绕有一定量的细菌纤维素时,细菌纤维素的生长明显具有加快的趋势,第二天缠绕的厚度明显大于第一天,依次类推,这可能是因为培养刚开始时,玻璃棒不利于纤维素的缠绕,而当玻璃棒上具有一些纤维素时则缠绕变得容易,缠绕增厚速度也就变快。Figure 8 shows that the axial strength of the material prepared by fermentation in the reactor increases continuously with the increase of the number of days of culture. This is because the thickness of the bacterial cellulose increases with the increase of the number of days of culture, and the amount of cellulose produced is also more many. Through the observation of the process, it can be found that the growth rate of the tubular material is gradually accelerated as the bacterial cellulose is wound on the glass rod. On the first day, the amount of cellulose winding was relatively small, but one day later, when a certain amount of bacterial cellulose was wound on the glass rod, the growth of bacterial cellulose was obviously accelerated, and the thickness of the second day was significantly larger than that of the first day. One day, and so on, this may be because at the beginning of the culture, the glass rod is not conducive to the winding of cellulose, but when there is some cellulose on the glass rod, the winding becomes easier, and the speed of winding thickening becomes faster.

图9显示径向强力的变化规律与轴向强力结果具有一定的相似性。随着培养天数的增加管状材料的径向强力逐渐加强,而且后期材料强力的增加量相对于前期的要大,这与前面提出的管状材料随着天数的增加,厚度的增加量明显加大相一致。图中N/g代表测得的实际力与纤维素干重的比值。由于管状材料的干重相对很小,只有不到10mg,所以相对于干重的强力的变化就会相对比较大,导致了它的偏差也相对较大。Figure 9 shows that the changing law of radial strength is similar to the results of axial strength. As the number of days of cultivation increases, the radial strength of the tubular material gradually strengthens, and the increase in the strength of the material in the later period is larger than that in the early stage, which is in line with the increase in the thickness of the tubular material as the number of days increases. unanimous. N/g in the figure represents the ratio of the measured actual force to the dry weight of cellulose. Since the dry weight of the tubular material is relatively small, less than 10mg, the change in strength relative to the dry weight will be relatively large, resulting in a relatively large deviation.

实施例5Example 5

(1)菌种培养(1) Bacteria culture

将红茶菌(kombucha)按接入1-10片直径0.5cm圆片含菌BC膜的接种量接入300mL液体种子培养基(本实施例以下面培养基配方为例:每1L水中,绿茶或者红茶1-10g(茶叶5g时最优),葡萄糖、蔗糖或者果糖10~200g、蛋白胨或者胰蛋白胨3g、酵母浸膏5g,pH3.0-7.5,巴氏灭菌30min;每1L水中,甘露醇、葡萄糖、蔗糖或果糖20-200g、蛋白胨或胰蛋白胨3g、酵母浸膏5g,pH3.0-7.5,121℃灭菌20min)扩培,于20-30℃、100-250r/min条件下摇床培养或者静置培养12~48h后备用;Put kombucha (kombucha) into 300mL liquid seed culture medium according to the inoculation amount of 1-10 discs with a diameter of 0.5cm containing bacteria BC film (this embodiment takes the following medium formula as an example: in every 1L of water, green tea or 1-10g of black tea (5g of tea leaves is optimal), 10-200g of glucose, sucrose or fructose, 3g of peptone or tryptone, 5g of yeast extract, pH3.0-7.5, pasteurized for 30min; per 1L of water, mannitol , glucose, sucrose or fructose 20-200g, peptone or tryptone 3g, yeast extract 5g, pH3.0-7.5, sterilized at 121°C for 20min) to expand culture, shake at 20-30°C, 100-250r/min Bed culture or static culture for 12 to 48 hours before use;

(2)中空异形细菌纤维素材料的发酵制备(2) Fermentation preparation of hollow shaped bacterial cellulose material

将步骤(1)制备的含生产菌株的液体培养基转移到配备有棒状模具的生物反应器中,然后旋转模具以10rpm的转速进行扰动培养,于30℃动态培养4-20天后,即可收获空腔异形纤维素材料;Transfer the liquid culture medium containing the production strain prepared in step (1) to a bioreactor equipped with a rod-shaped mold, then rotate the mold at a speed of 10 rpm for disturbed culture, and culture it dynamically at 30°C for 4-20 days before harvesting Hollow profiled cellulose material;

或者取步骤(1)活化好的菌种按1~10片直径0.5-1cm圆片含菌BC膜的接种量转接到300mL液体发酵培养基中,置于500mL锥形瓶中,在30℃和160rpm的条件下培养4小时,然后再将发酵液转移到生物反应器中,,然后旋转模具以10rpm的转速进行扰动培养,于30℃条件下分别培养不同的天数,可制备得到不同厚度的管状细菌纤维素材料。Or take the activated strain of step (1) and transfer it to 300mL liquid fermentation medium according to the inoculation amount of 1-10 discs with a diameter of 0.5-1cm containing bacteria BC film, place in a 500mL Erlenmeyer flask, at 30°C and 160rpm for 4 hours, and then transfer the fermentation broth to the bioreactor, and then rotate the mold at a speed of 10rpm to disturb the culture, and culture at 30°C for different days, and different thicknesses can be prepared. Tubular bacterial cellulose material.

该发酵装置由一个水平搅拌反应器和在转盘上固定若干手套形模具的转轴组成,形成了一个水平扰动的生物反应器。通过转盘上模具围绕着转轴轴心的转动,使得模具缠绕发酵液中的细菌纤维素而在模具表面形成一定形状的中空细菌纤维素材料。获得的产品与图5中类似。The fermentation device consists of a horizontal stirring reactor and a rotating shaft on which several glove-shaped molds are fixed on a turntable, forming a horizontally disturbed bioreactor. Through the rotation of the mold on the turntable around the axis of the rotating shaft, the mold wraps the bacterial cellulose in the fermentation broth to form a hollow bacterial cellulose material of a certain shape on the surface of the mold. The product obtained is similar to that in Figure 5.

(3)材料处理(3) Material handling

将制备的空腔异形BC材料从模具上取下,蒸馏水多次冲洗后,然后浸泡于0.5~2wt%的NaOH溶液中,70-100℃水浴处理30-120min,使BC管状材料呈白色半透明后即可,用纯水反复洗涤至中性,然后冷冻干燥,即得异形细菌纤维素产品。Remove the prepared cavity special-shaped BC material from the mold, rinse it with distilled water several times, then soak it in 0.5-2wt% NaOH solution, and treat it in a water bath at 70-100°C for 30-120min, so that the BC tubular material is white and translucent After that, it can be washed repeatedly with pure water until neutral, and then freeze-dried to obtain the special-shaped bacterial cellulose product.

Claims (8)

1.一种动态制备异型空腔细菌纤维素材料的方法,包括:1. A method for dynamically preparing special-shaped cavity bacterial cellulose materials, comprising: (1)菌种培养(1) Bacteria culture 将细菌纤维素生产菌株接入液体培养基扩培,于20-30℃、100-250r/min条件下摇床培养或者静置培养12~48h后备用;Insert the bacterial cellulose production strain into the liquid medium for expansion, and cultivate it on a shaking table under the conditions of 20-30°C and 100-250r/min or static culture for 12-48 hours before use; (2)异型空腔BC材料的发酵制备(2) Fermentation preparation of special-shaped cavity BC materials 将步骤(1)制备的含生产菌株的液体培养基转移到发酵装置中,然后旋转模具以3-20rpm的转速进行扰动培养,于20~32℃动态培养4-20天后,即可收获空腔异形纤维素材料;其中,模具为棍形或手套形模具,转轴在发酵罐内腔安装固定有两个转盘,转轴通过转盘圆周边缘对称固定有2个以上模具;Transfer the liquid medium containing the production strain prepared in step (1) to the fermentation device, then rotate the mold at a speed of 3-20rpm for disturbed culture, and after dynamic culture at 20-32°C for 4-20 days, the cavity can be harvested Special-shaped cellulose material; wherein, the mold is a stick-shaped or glove-shaped mold, and the rotating shaft is installed and fixed in the inner cavity of the fermenter with two turntables, and the rotating shaft is symmetrically fixed with more than two molds through the peripheral edge of the turntable; (3)材料处理(3) Material handling 将制备的中空异形细菌纤维素材料从模具上取下,然后浸泡于0.5~2wt%的NaOH溶液中,70-100℃水浴处理30-120min,使细菌纤维素材料呈白色半透明后即可,然后洗涤至中性,即得异形细菌纤维素产品。The prepared hollow special-shaped bacterial cellulose material is removed from the mold, then soaked in 0.5-2wt% NaOH solution, treated in a water bath at 70-100°C for 30-120min, and the bacterial cellulose material is white and translucent. Then wash until neutral to obtain the special-shaped bacterial cellulose product. 2.根据权利要求1述的一种动态制备异型空腔细菌纤维素材料的方法,其特征在于:所述步骤(1)中的BC生产菌株为醋酸菌属Acetobacter sp.、葡萄糖酸杆菌属Gluconobacter sp.、葡糖酸醋杆菌属Gluconacetobacter sp.、根瘤菌属Rhizobium sp.、八叠球菌属Sarcina sp.、假单胞菌属Pseudomounas sp.、无色杆菌属Achromobacter sp.、产碱菌属Alcaligenes sp.、气杆菌属Aerobacter sp.、固氮菌属Azotobacter sp.、土壤杆菌属Agrobacterium sp.、洋葱假单胞菌Seudomonas cepacia、空肠弯曲菌Campylobacter jejuni或红茶菌(kombucha)。2. a kind of method for dynamically preparing special-shaped cavity bacterial cellulose material according to claim 1 is characterized in that: the BC production bacterial strain in the described step (1) is Acetobacter sp., Gluconobacter Gluconobacter sp., Gluconacetobacter sp., Rhizobium sp., Sarcina sp., Pseudomounas sp., Achromobacter sp., Alcaligenes sp., Aerobacter sp., Azotobacter sp., Agrobacterium sp., Pseudomonas cepacia, Campylobacter jejuni or kombucha. 3.根据权利要求2所述的一种动态制备异型空腔细菌纤维素材料的方法,其特征在于:其中BC生产菌株为木醋杆菌Acetobacter xylinum或红茶菌。3. a kind of method for dynamically preparing special-shaped cavity bacterial cellulose material according to claim 2, is characterized in that: wherein BC production bacterial strain is Acetobacter xylinum or kombucha. 4.根据权利要求1或2所述的一种动态制备异型空腔细菌纤维素材料的方法,其特征在于:除红茶菌以外的菌种按2~3接种环的接种量接入液体种子培养基;红茶菌按接入1-10片直径0.5cm圆片含菌BC膜的接种量接入液体种子培养基;4. A method for dynamically preparing special-shaped cavity bacterial cellulose material according to claim 1 or 2, characterized in that: bacterial classifications other than kombucha are inserted into liquid seed culture with an inoculum size of 2 to 3 inoculation loops base; Kombucha fungus is inserted into the liquid seed medium according to the inoculation amount of 1-10 discs with a diameter of 0.5cm containing bacteria BC film; 或者先制备生产菌的液体种子,再转接入液体发酵培养基,具体步骤如下:Or prepare the liquid seeds of the production bacteria first, and then transfer them to the liquid fermentation medium. The specific steps are as follows: 除红茶菌以外的菌种按2~3接种环的接种量接入液体种子培养基制备种子液,然后按3vol%~20vol%的接种量转接到液体发酵培养基;红茶菌按接入1-10片直径0.5cm圆片含菌BC膜的接种量接入液体种子培养基,以及按1~10片直径0.5-1cm圆片含菌BC膜的接种量转接到液体发酵培养基。Bacteria except kombucha are inserted into liquid seed culture medium to prepare seed solution according to the inoculation amount of 2 to 3 inoculation loops, and then transferred to liquid fermentation medium according to the inoculum amount of 3vol% to 20vol%; kombucha is inserted into 1 - The inoculum of 10 discs with a diameter of 0.5 cm containing bacteria BC membranes is inserted into the liquid seed medium, and the inoculum of 1 to 10 discs with a diameter of 0.5-1 cm containing bacteria BC films is transferred to the liquid fermentation medium. 5.根据权利要求1所述的一种动态制备异型空腔细菌纤维素材料的方法,其特征在于:所述的除了红茶菌以外的液体种子培养基和液体发酵培养基的组分均为:每1L水中,甘露醇、葡萄糖、麦芽糖、蔗糖或果糖20-200 g、蛋白胨或胰蛋白胨3g、酵母浸膏5g,pH3.0-7.5,121℃灭菌20min;或甘露醇、葡萄糖、蔗糖或果糖20-200g,酵母浸膏5g,蛋白胨或胰蛋白胨5g,柠檬酸1.15g,Na2HPO42.7g,水1L,pH3.0-7.5,121℃灭菌20min;5. a kind of method for dynamically preparing special-shaped cavity bacterial cellulose material according to claim 1 is characterized in that: the components of described liquid seed medium and liquid fermentation medium except kombucha are: For every 1L of water, 20-200 g of mannitol, glucose, maltose, sucrose or fructose, 3 g of peptone or tryptone, 5 g of yeast extract, pH 3.0-7.5, sterilized at 121°C for 20 minutes; or mannitol, glucose, sucrose or Fructose 20-200g, yeast extract 5g, peptone or tryptone 5g, citric acid 1.15g, Na 2 HPO 4 2.7g, water 1L, pH 3.0-7.5, sterilized at 121°C for 20min; 红茶菌液体种子培养基和液体发酵培养基,其组成均为:(1)每1L水中,绿茶或者红茶1-10g,葡萄糖、蔗糖或者果糖10~200g、蛋白胨或者胰蛋白胨3g、酵母浸膏5g,pH3.0-7.5,巴氏灭菌30min;(2)将葡萄糖、蔗糖或果糖、绿茶或红茶、以及水配成培养基,其中糖、茶、水的质量比为5∶0.1-0.4∶100-200,pH3.0-7.5,巴氏灭菌30min;或者(3)每1L水中,甘露醇、葡萄糖、蔗糖或果糖20-200g、蛋白胨或胰蛋白胨3g、酵母浸膏5g,pH3.0-7.5,121℃灭菌20min。Kombucha liquid seed medium and liquid fermentation medium are composed of: (1) per 1L of water, 1-10g of green tea or black tea, 10-200g of glucose, sucrose or fructose, 3g of peptone or tryptone, and 5g of yeast extract , pH3.0-7.5, pasteurized for 30min; (2) glucose, sucrose or fructose, green tea or black tea, and water are made into medium, wherein the mass ratio of sugar, tea, and water is 5:0.1-0.4: 100-200, pH3.0-7.5, pasteurized for 30 minutes; or (3) per 1L of water, mannitol, glucose, sucrose or fructose 20-200g, peptone or tryptone 3g, yeast extract 5g, pH3.0 -7.5, sterilized at 121°C for 20 minutes. 6.根据权利要求5所述的一种动态制备异型空腔细菌纤维素材料的方法,其特征在于:所述红茶菌液体种子培养基和液体发酵培养基(1)中绿茶或者红茶5g。6. A kind of method for dynamically preparing special-shaped cavity bacterial cellulose material according to claim 5, characterized in that: 5g of green tea or black tea in the kombucha liquid seed culture medium and liquid fermentation medium (1). 7.根据权利要求1所述的一种动态制备异型空腔细菌纤维素材料的方法,其特征在于:所述步骤(2)中的含生产菌株的液体培养基为步骤(1)制备的含生产菌株的液体种子培养基或含生产菌株的液体发酵培养基。7. a kind of method for dynamically preparing special-shaped cavity bacterial cellulose material according to claim 1, is characterized in that: the liquid culture medium that contains the production strain in the described step (2) is the liquid culture medium that contains the bacterial strain that step (1) prepares Liquid seed medium for production strains or liquid fermentation medium containing production strains. 8.根据权利要求1所述的一种动态制备异型空腔细菌纤维素材料的方法,其特征在于:在异型空腔BC材料的发酵制备的过程中,通过在转轴或模具内腔中注入含氧量为1-100vol%的空气,以加速纤维素膜在模具上形成。8. a kind of method for dynamically preparing special-shaped cavity bacterial cellulose material according to claim 1 is characterized in that: in the process of the fermentation preparation of special-shaped cavity BC material, by injecting containing Air with an oxygen content of 1-100vol% to accelerate the formation of the cellulose film on the mold.
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