CN115737600B - Continuous hydrogen-producing biological microsphere and preparation method and application thereof - Google Patents
Continuous hydrogen-producing biological microsphere and preparation method and application thereof Download PDFInfo
- Publication number
- CN115737600B CN115737600B CN202211493036.9A CN202211493036A CN115737600B CN 115737600 B CN115737600 B CN 115737600B CN 202211493036 A CN202211493036 A CN 202211493036A CN 115737600 B CN115737600 B CN 115737600B
- Authority
- CN
- China
- Prior art keywords
- hydrogen
- producing
- solution
- microspheres
- polylysine
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 239000001257 hydrogen Substances 0.000 title claims abstract description 141
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 141
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 134
- 239000004005 microsphere Substances 0.000 title claims abstract description 65
- 238000002360 preparation method Methods 0.000 title claims abstract description 15
- 244000005700 microbiome Species 0.000 claims abstract description 29
- 235000010410 calcium alginate Nutrition 0.000 claims abstract description 24
- 239000000648 calcium alginate Substances 0.000 claims abstract description 24
- 229960002681 calcium alginate Drugs 0.000 claims abstract description 24
- OKHHGHGGPDJQHR-YMOPUZKJSA-L calcium;(2s,3s,4s,5s,6r)-6-[(2r,3s,4r,5s,6r)-2-carboxy-6-[(2r,3s,4r,5s,6r)-2-carboxylato-4,5,6-trihydroxyoxan-3-yl]oxy-4,5-dihydroxyoxan-3-yl]oxy-3,4,5-trihydroxyoxane-2-carboxylate Chemical compound [Ca+2].O[C@@H]1[C@H](O)[C@H](O)O[C@@H](C([O-])=O)[C@H]1O[C@H]1[C@@H](O)[C@@H](O)[C@H](O[C@H]2[C@H]([C@@H](O)[C@H](O)[C@H](O2)C([O-])=O)O)[C@H](C(O)=O)O1 OKHHGHGGPDJQHR-YMOPUZKJSA-L 0.000 claims abstract description 24
- 239000011259 mixed solution Substances 0.000 claims abstract description 21
- 239000000243 solution Substances 0.000 claims abstract description 21
- 108010039918 Polylysine Proteins 0.000 claims abstract description 17
- 229920000656 polylysine Polymers 0.000 claims abstract description 17
- 206010028980 Neoplasm Diseases 0.000 claims abstract description 15
- 239000012528 membrane Substances 0.000 claims abstract description 15
- IXPNQXFRVYWDDI-UHFFFAOYSA-N 1-methyl-2,4-dioxo-1,3-diazinane-5-carboximidamide Chemical compound CN1CC(C(N)=N)C(=O)NC1=O IXPNQXFRVYWDDI-UHFFFAOYSA-N 0.000 claims abstract description 12
- 238000000034 method Methods 0.000 claims abstract description 12
- 235000010413 sodium alginate Nutrition 0.000 claims abstract description 12
- 239000000661 sodium alginate Substances 0.000 claims abstract description 12
- 229940005550 sodium alginate Drugs 0.000 claims abstract description 12
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims abstract description 10
- 238000002156 mixing Methods 0.000 claims abstract description 3
- 241000588915 Klebsiella aerogenes Species 0.000 claims description 28
- 229940092559 enterobacter aerogenes Drugs 0.000 claims description 28
- 230000005686 electrostatic field Effects 0.000 claims description 6
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 5
- 239000011780 sodium chloride Substances 0.000 claims description 3
- 241000195597 Chlamydomonas reinhardtii Species 0.000 claims description 2
- 241000193171 Clostridium butyricum Species 0.000 claims description 2
- 229940079593 drug Drugs 0.000 claims 1
- 239000003814 drug Substances 0.000 claims 1
- 239000000758 substrate Substances 0.000 abstract description 9
- 238000000855 fermentation Methods 0.000 abstract description 7
- 230000004151 fermentation Effects 0.000 abstract description 6
- 239000007789 gas Substances 0.000 abstract description 6
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 abstract description 5
- 239000008103 glucose Substances 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 4
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 abstract description 3
- 230000000813 microbial effect Effects 0.000 abstract description 3
- 206010020751 Hypersensitivity Diseases 0.000 abstract description 2
- 239000002207 metabolite Substances 0.000 abstract description 2
- LCTONWCANYUPML-UHFFFAOYSA-N Pyruvic acid Chemical compound CC(=O)C(O)=O LCTONWCANYUPML-UHFFFAOYSA-N 0.000 abstract 2
- 208000026935 allergic disease Diseases 0.000 abstract 1
- 230000009610 hypersensitivity Effects 0.000 abstract 1
- 229940107700 pyruvic acid Drugs 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 21
- 239000001963 growth medium Substances 0.000 description 12
- 150000002431 hydrogen Chemical class 0.000 description 7
- 239000002609 medium Substances 0.000 description 6
- 238000012360 testing method Methods 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 239000006143 cell culture medium Substances 0.000 description 5
- PZKRHHZKOQZHIO-UHFFFAOYSA-N [B].[B].[Mg] Chemical compound [B].[B].[Mg] PZKRHHZKOQZHIO-UHFFFAOYSA-N 0.000 description 4
- 239000002105 nanoparticle Substances 0.000 description 4
- 239000002135 nanosheet Substances 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 101001121408 Homo sapiens L-amino-acid oxidase Proteins 0.000 description 3
- 102100026388 L-amino-acid oxidase Human genes 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- -1 palladium hydride Chemical class 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 238000002560 therapeutic procedure Methods 0.000 description 3
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 2
- LCTONWCANYUPML-UHFFFAOYSA-M Pyruvate Chemical compound CC(=O)C([O-])=O LCTONWCANYUPML-UHFFFAOYSA-M 0.000 description 2
- 101100012902 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) FIG2 gene Proteins 0.000 description 2
- 101100233916 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) KAR5 gene Proteins 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 2
- 125000003277 amino group Chemical group 0.000 description 2
- 229940041514 candida albicans extract Drugs 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000012258 culturing Methods 0.000 description 2
- 201000010099 disease Diseases 0.000 description 2
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 2
- 230000003902 lesion Effects 0.000 description 2
- 239000002502 liposome Substances 0.000 description 2
- 230000003287 optical effect Effects 0.000 description 2
- 230000001225 therapeutic effect Effects 0.000 description 2
- 230000001988 toxicity Effects 0.000 description 2
- 231100000419 toxicity Toxicity 0.000 description 2
- 239000012138 yeast extract Substances 0.000 description 2
- 206010067484 Adverse reaction Diseases 0.000 description 1
- 101000827703 Homo sapiens Polyphosphoinositide phosphatase Proteins 0.000 description 1
- 206010061218 Inflammation Diseases 0.000 description 1
- 206010027476 Metastases Diseases 0.000 description 1
- 102100023591 Polyphosphoinositide phosphatase Human genes 0.000 description 1
- 230000006838 adverse reaction Effects 0.000 description 1
- 229960005070 ascorbic acid Drugs 0.000 description 1
- 235000010323 ascorbic acid Nutrition 0.000 description 1
- 239000011668 ascorbic acid Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 238000002512 chemotherapy Methods 0.000 description 1
- 229930002868 chlorophyll a Natural products 0.000 description 1
- ATNHDLDRLWWWCB-AENOIHSZSA-M chlorophyll a Chemical compound C1([C@@H](C(=O)OC)C(=O)C2=C3C)=C2N2C3=CC(C(CC)=C3C)=[N+]4C3=CC3=C(C=C)C(C)=C5N3[Mg-2]42[N+]2=C1[C@@H](CCC(=O)OC\C=C(/C)CCC[C@H](C)CCC[C@H](C)CCCC(C)C)[C@H](C)C2=C5 ATNHDLDRLWWWCB-AENOIHSZSA-M 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000013270 controlled release Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 210000002249 digestive system Anatomy 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 210000002865 immune cell Anatomy 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 208000015181 infectious disease Diseases 0.000 description 1
- 230000004054 inflammatory process Effects 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000009401 metastasis Effects 0.000 description 1
- 239000002539 nanocarrier Substances 0.000 description 1
- 231100000957 no side effect Toxicity 0.000 description 1
- 230000036542 oxidative stress Effects 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- KDLHZDBZIXYQEI-UHFFFAOYSA-N palladium Substances [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 230000001699 photocatalysis Effects 0.000 description 1
- 238000007146 photocatalysis Methods 0.000 description 1
- 230000035755 proliferation Effects 0.000 description 1
- 238000001959 radiotherapy Methods 0.000 description 1
- 210000002345 respiratory system Anatomy 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 229940126585 therapeutic drug Drugs 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Landscapes
- Medicinal Preparation (AREA)
Abstract
Description
技术领域Technical Field
本发明涉及生物微球制备技术领域,具体涉及一种持续产氢生物微球及其制备方法与应用。The present invention relates to the technical field of biomicrosphere preparation, and in particular to a biomicrosphere that continuously produces hydrogen, and a preparation method and application thereof.
背景技术Background technique
氢气疗法能够抑制肿瘤的增殖与转移,同时可减轻肿瘤放化疗继发的不良反应,且几乎无副作用。控制氢气在病灶部位有效蓄积,是保证肿瘤氢气治疗效果的关键。但高压氢气易燃且有爆炸危险,现阶段难以广泛应用于临床。再者由于氢气的溶解度较低,在体内可任意扩散,使氢气分子难以有效到达并大量蓄积在深层病灶组织,导致治疗效果有限。Hydrogen therapy can inhibit tumor proliferation and metastasis, and at the same time reduce the adverse reactions secondary to tumor radiotherapy and chemotherapy, with almost no side effects. Controlling the effective accumulation of hydrogen in the lesion site is the key to ensuring the effectiveness of hydrogen therapy for tumors. However, high-pressure hydrogen is flammable and explosive, and it is difficult to be widely used in clinical practice at this stage. In addition, due to the low solubility of hydrogen, it can diffuse arbitrarily in the body, making it difficult for hydrogen molecules to effectively reach and accumulate in large quantities in deep lesion tissues, resulting in limited treatment effects.
目前,氢气治疗的供氢途径包括:吸入氢氧混合气、注射富氢生理盐水以及口服富氢水。例如专利CN201910163975.9公开了一种安全吸氢机,输出氢浓度约2%的氢氧混合气体供给患者吸入,氢气通过呼吸系统扩散进入人体治疗疾病。但普通氢呼吸机普遍存在氢氧制备效率不高、气路顺畅度不佳以及氢氧输出的精准控制程度不高等缺点,且在使用一段时间后,若清洁不彻底易给患者带来感染风险。专利CN202121453005.1公开了一种富氢水机,将氢气与饮用水加压混合,输出氢浓度约1.6ppm的富氢水供给患者饮用,水中氢气通过消化系统扩散进入人体治疗疾病。富氢水中的氢在常温常压下易解离逸散,导致患者的实际氢摄入量往往低于预期值。此外,通过口服或吸入方式摄入的氢气会在体内自由扩散,难以在深层组织达到具有治疗效果的氢浓度,作用效果有限。上述氢传递法无法靶向肿瘤,导致肿瘤部位氢气浓度较低,且上述氢传递法无法实现持续供氢作用于肿瘤部位,导致治疗效果不理想。At present, the hydrogen supply methods for hydrogen therapy include: inhalation of hydrogen-oxygen mixed gas, injection of hydrogen-rich saline, and oral administration of hydrogen-rich water. For example, patent CN201910163975.9 discloses a safe hydrogen inhaler that outputs a hydrogen-oxygen mixed gas with a hydrogen concentration of about 2% for patients to inhale, and the hydrogen diffuses into the human body through the respiratory system to treat diseases. However, ordinary hydrogen respirators generally have the disadvantages of low hydrogen-oxygen preparation efficiency, poor gas path smoothness, and low precision control of hydrogen-oxygen output. After a period of use, if the cleaning is not thorough, it is easy to bring infection risks to patients. Patent CN202121453005.1 discloses a hydrogen-rich water machine that pressurizes and mixes hydrogen with drinking water, outputs hydrogen-rich water with a hydrogen concentration of about 1.6ppm for patients to drink, and the hydrogen in the water diffuses into the human body through the digestive system to treat diseases. The hydrogen in hydrogen-rich water is easy to dissociate and dissipate at normal temperature and pressure, resulting in the patient's actual hydrogen intake often being lower than the expected value. In addition, hydrogen ingested by oral or inhalation will diffuse freely in the body, and it is difficult to reach a hydrogen concentration with therapeutic effects in deep tissues, and the effect is limited. The above hydrogen transfer method cannot target the tumor, resulting in a low hydrogen concentration at the tumor site, and the above hydrogen transfer method cannot achieve continuous hydrogen supply to the tumor site, resulting in unsatisfactory treatment effect.
供氢纳米载体的开发(如纳米钯氢化物,硼化镁纳米片),为肿瘤靶向供氢提供有效解决方案。然而纳米颗粒的负载能力有限,无法实现持续性供氢,且纳米颗粒在体内难以降解,部分含重金属离子具有生物毒性,安全性未能得到保障。Wan等人构建了脂质体纳米粒(Wan W L,Lin Y J,Chen H L,et al.In situ nanoreactor for photosynthesizingH2 gas to mitigate oxidative stress in tissue inflammation[J].Journal of theAmerican Chemical Society,2017,139(37):12923-12926),包埋叶绿素a、抗坏血酸和金纳米粒子,在红外光催化下可以在肿瘤部位实现催化产氢。然而,在组织体内红外光穿透深度有限,极大限制了其催化产氢能力,且脂质体膜对氢气的渗透性过高,导致氢气逸散快速难以有效蓄积。因此,如何实现氢的有效存储、靶向递送和可控释放,对提高氢气治疗效果以及临床应用具有重要意义。The development of hydrogen supply nanocarriers (such as nano palladium hydride, magnesium boride nanosheets) provides an effective solution for tumor-targeted hydrogen supply. However, the loading capacity of nanoparticles is limited, and continuous hydrogen supply cannot be achieved. In addition, nanoparticles are difficult to degrade in the body, and some of them contain heavy metal ions with biological toxicity, and their safety cannot be guaranteed. Wan et al. constructed liposome nanoparticles (Wan WL, Lin YJ, Chen HL, et al. In situ nanoreactor for photosynthesizing H 2 gas to mitigate oxidative stress in tissue inflammation [J]. Journal of the American Chemical Society, 2017, 139 (37): 12923-12926), embedded chlorophyll a, ascorbic acid and gold nanoparticles, and catalytic hydrogen production can be achieved at the tumor site under infrared photocatalysis. However, the limited penetration depth of infrared light in the tissue body greatly limits its catalytic hydrogen production ability, and the liposome membrane is too permeable to hydrogen, resulting in rapid hydrogen escape and difficulty in effective accumulation. Therefore, how to achieve effective storage, targeted delivery and controlled release of hydrogen is of great significance to improving the therapeutic effect and clinical application of hydrogen.
发明内容Summary of the invention
本发明要解决的技术问题是提供一种持续产氢生物微球及其制备方法与应用,利用海藻酸钙包埋活性产氢微生物,并通过海藻酸钙表面的羧酸根离子与聚赖氨酸表面的氨基反应,在包载产氢微生物的海藻酸钙凝胶微球的表面形成聚赖氨酸半透膜,制备得到产氢生物微球,可实现持续供氢。The technical problem to be solved by the present invention is to provide a continuous hydrogen-producing biological microsphere and a preparation method and application thereof. Active hydrogen-producing microorganisms are embedded in calcium alginate, and carboxylate ions on the surface of calcium alginate react with amino groups on the surface of polylysine to form a polylysine semipermeable membrane on the surface of the calcium alginate gel microsphere encapsulating the hydrogen-producing microorganisms, thereby preparing hydrogen-producing biological microspheres that can achieve continuous hydrogen supply.
为了解决上述技术问题,本发明提供以下技术方案:In order to solve the above technical problems, the present invention provides the following technical solutions:
本发明第一方面提供了一种产氢生物微球,由载产氢微生物的海藻酸钙凝胶微球及其表面包覆的聚赖氨酸半透膜组成。The first aspect of the present invention provides a hydrogen-producing biological microsphere, which is composed of calcium alginate gel microspheres carrying hydrogen-producing microorganisms and polylysine semipermeable membranes coated on the surface thereof.
进一步地,所述产氢微生物为经过驯化的产气肠杆菌、丁酸梭菌、莱茵衣藻中一种或多种。Furthermore, the hydrogen-producing microorganism is one or more of domesticated Enterobacter aerogenes, Clostridium butyricum, and Chlamydomonas reinhardtii.
进一步地,所述驯化具体为:在培养微生物的培养基中,逐步提升培养基中细胞培养基的比例,直至细菌完全适应细胞培养基的环境,得到驯化后的微生物。Furthermore, the domestication specifically includes: in the culture medium for culturing microorganisms, gradually increasing the proportion of the cell culture medium in the culture medium until the bacteria are fully adapted to the environment of the cell culture medium, thereby obtaining domesticated microorganisms.
本发明第二方面提供了第一方面所述的产氢生物微球的制备方法,包括以下步骤:The second aspect of the present invention provides a method for preparing the hydrogen-producing biomicrospheres described in the first aspect, comprising the following steps:
(1)将海藻酸钠溶液与产氢微生物共混,得到混合溶液,利用静电液滴法将混合溶液滴至氯化钙溶液中,形成载产氢微生物的海藻酸钙凝胶微球;(1) mixing a sodium alginate solution with hydrogen-producing microorganisms to obtain a mixed solution, and dropping the mixed solution into a calcium chloride solution using an electrostatic drop method to form calcium alginate gel microspheres carrying hydrogen-producing microorganisms;
(2)将步骤(1)制备的载产氢微生物的海藻酸钙凝胶微球浸渍于聚赖氨酸溶液中,反应得到所述产氢生物微球。(2) The calcium alginate gel microspheres carrying hydrogen-producing microorganisms prepared in step (1) are immersed in a polylysine solution to react and obtain the hydrogen-producing biological microspheres.
进一步地,步骤(1)中,所述混合溶液中产氢微生物的密度为5×107~109cells/mL。Furthermore, in step (1), the density of hydrogen-producing microorganisms in the mixed solution is 5×10 7 to 10 9 cells/mL.
进一步地,步骤(1)中,所述海藻酸钠溶液由海藻酸钠溶于氯化钠溶液中得到;所述海藻酸钠溶液的浓度为1.3~2.0%(w/v)。Furthermore, in step (1), the sodium alginate solution is obtained by dissolving sodium alginate in a sodium chloride solution; and the concentration of the sodium alginate solution is 1.3-2.0% (w/v).
进一步地,步骤(1)中,所述氯化钙溶液的浓度为0.8-2.0%(w/v)。Furthermore, in step (1), the concentration of the calcium chloride solution is 0.8-2.0% (w/v).
进一步地,步骤(1)中,所述静电液滴法具体为:将混合溶液加入注射器,在静电场作用下利用注射泵将混合溶液匀速滴入氯化钙溶液中。Furthermore, in step (1), the electrostatic drop method is specifically as follows: adding the mixed solution into a syringe, and using a syringe pump to uniformly drop the mixed solution into the calcium chloride solution under the action of an electrostatic field.
进一步地,所述静电场的电压为4.0~5.5kv,注射器的流速为5~15mL/h。Furthermore, the voltage of the electrostatic field is 4.0 to 5.5 kV, and the flow rate of the syringe is 5 to 15 mL/h.
进一步地,所述注射器针头的规格为0.4~0.7mm。Furthermore, the specification of the syringe needle is 0.4-0.7 mm.
进一步地,步骤(1)中,所述海藻酸钙凝胶微球的直径为100~300μm。Furthermore, in step (1), the diameter of the calcium alginate gel microspheres is 100 to 300 μm.
进一步地,步骤(1)中,当混合溶液滴至氯化钙溶液中形成凝胶微球10~30min后,通过自然沉淀收集微球。Furthermore, in step (1), after the mixed solution is dropped into the calcium chloride solution to form gel microspheres for 10 to 30 minutes, the microspheres are collected by natural precipitation.
进一步地,步骤(2)中,所述聚赖氨酸溶液的浓度为0.05%~0.2%(w/v)。Furthermore, in step (2), the concentration of the polylysine solution is 0.05% to 0.2% (w/v).
进一步地,将载产氢微生物的海藻酸钙凝胶微球浸渍于聚赖氨酸溶液中,置于摇床上反应10~20min;所述摇床的转速为20~100rpm。Furthermore, the calcium alginate gel microspheres carrying hydrogen-producing microorganisms are immersed in a polylysine solution and placed on a shaker for reaction for 10 to 20 minutes; the rotation speed of the shaker is 20 to 100 rpm.
本发明通过静电液滴法将活体产氢微生物包载在海藻酸钙凝胶微球内,并利用海藻酸钙表面富含的羧酸根离子与聚赖氨酸表面的氨基反应,在微球表面形成聚赖氨酸半透膜,制备得到产氢微生物微球;所述产氢微生物微球内部的活体产氢微生物以葡萄糖、丙酮酸等作为底物进行发酵产氢,且微球表面的半透膜对发酵底物以及氢气具有选择透过性,因此该微球可实现持续供氢。The present invention encapsulates live hydrogen-producing microorganisms in calcium alginate gel microspheres by an electrostatic droplet method, and utilizes carboxylate ions rich in the surface of calcium alginate to react with amino groups on the surface of polylysine to form a polylysine semipermeable membrane on the surface of the microspheres to prepare hydrogen-producing microbial microspheres; the live hydrogen-producing microorganisms inside the hydrogen-producing microbial microspheres ferment and produce hydrogen using glucose, pyruvate, etc. as substrates, and the semipermeable membrane on the surface of the microspheres has selective permeability to the fermentation substrate and hydrogen, so the microspheres can achieve continuous hydrogen supply.
本发明第三方面提供了一种第一方面所述的产氢生物微球在制备氢气治疗药物方面的应用。The third aspect of the present invention provides a use of the hydrogen-producing biomicrospheres described in the first aspect in preparing hydrogen therapeutic drugs.
与现有技术相比,本发明的有益效果:Compared with the prior art, the present invention has the following beneficial effects:
1.本发明提供了一种产氢生物微球,通过海藻酸钙凝胶包埋经驯化已适应人体生理环境的产氢微生物形成微球,并在微球表面包覆聚赖氨酸半透膜得到,该产氢生物微球中的微生物以葡萄糖、丙酮酸等作为底物进行发酵产氢,发酵底物和氢气可选择性通过半透膜,实现持续供氢。1. The present invention provides a hydrogen-producing biological microsphere, which is formed by embedding hydrogen-producing microorganisms that have been domesticated and adapted to the physiological environment of the human body in calcium alginate gel, and coating the surface of the microsphere with a polylysine semipermeable membrane. The microorganisms in the hydrogen-producing biological microsphere ferment and produce hydrogen using glucose, pyruvate, etc. as substrates, and the fermentation substrate and hydrogen can selectively pass through the semipermeable membrane to achieve continuous hydrogen supply.
2.本发明制备的产氢生物微球,在不同培养基中(包括细胞培养基)均具有高产氢量,且受外界环境的影响小;微生物在海藻酸钙凝胶基底以及半透膜的作用下被限制在微球内部,有效防止微生物或其成分外溢导致超敏反应或生物毒性作用,同时保护微生物不被体内免疫细胞识别清除,发挥最佳产氢效率。2. The hydrogen-producing biological microspheres prepared by the present invention have high hydrogen production in different culture media (including cell culture media) and are less affected by the external environment; the microorganisms are confined inside the microspheres under the action of the calcium alginate gel substrate and the semipermeable membrane, which effectively prevents the overflow of the microorganisms or their components from causing hypersensitivity reactions or biological toxicity, while protecting the microorganisms from being recognized and eliminated by the immune cells in the body, thereby achieving the best hydrogen production efficiency.
3.本发明制备的产氢生物微球可通过介入手段到达需氢气治疗的部位(例如肿瘤部位),从而在靶向部位实现持续供氢,达到氢气治疗有效的氢浓度;此外,肿瘤组织代谢物可作为微生物的发酵底物,实现微球在肿瘤组织部位持续供氢,无需额外提供发酵底物。本发明提供的一种持续产氢生物微球,为临床气体治疗肿瘤提供新的思路。3. The hydrogen-producing bio-microspheres prepared by the present invention can reach the site that needs hydrogen treatment (such as the tumor site) through interventional means, thereby achieving continuous hydrogen supply at the targeted site and reaching a hydrogen concentration that is effective for hydrogen treatment; in addition, tumor tissue metabolites can be used as fermentation substrates for microorganisms, so that the microspheres can continuously supply hydrogen at the tumor tissue site without the need for additional fermentation substrates. The continuous hydrogen-producing bio-microspheres provided by the present invention provide a new idea for clinical gas treatment of tumors.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
图1为实施例1中产氢生物微球的制备过程示意图;FIG1 is a schematic diagram of the preparation process of hydrogen-producing biomicrospheres in Example 1;
图2为实施例1制备的产氢生物微球在#1培养基中培养0、48h的光学显微图片;FIG2 is an optical microscopic image of the hydrogen-producing biomicrospheres prepared in Example 1 cultured in #1 medium at 0 and 48 h;
图3为实施例1制备的产氢生物微球在#1培养基中培养48h后,细菌的生长情况;FIG3 shows the growth of bacteria after the hydrogen-producing bio-microspheres prepared in Example 1 were cultured in #1 medium for 48 hours;
图4为MgB2、已驯化的产气肠杆菌及产氢生物微球在不同培养基中培养48h后的产氢量;FIG4 shows the hydrogen production of MgB 2 , domesticated Enterobacter aerogenes and hydrogen-producing biomicrospheres after culturing in different culture media for 48 hours;
图5为实施例1制备的产氢生物微球在#1培养基中,37℃持续无氧发酵的产氢量变化曲线。FIG5 is a curve showing the change in hydrogen production of the hydrogen-producing biomicrospheres prepared in Example 1 in a #1 culture medium under continuous anaerobic fermentation at 37° C.
具体实施方式Detailed ways
除非另有定义,本文所使用的所有的技术和科学术语与属于本发明的技术领域的技术人员通常理解的含义相同。本文中在本发明的说明书中所使用的术语只是为了描述具体的实施例的目的,不是旨在于限制本发明。本文所使用的术语“及/或”包括一个或多个相关的所列项目的任意的和所有的组合。Unless otherwise defined, all technical and scientific terms used herein have the same meaning as those commonly understood by those skilled in the art of the present invention. The terms used herein in the specification of the present invention are only for the purpose of describing specific embodiments and are not intended to limit the present invention. The term "and/or" used herein includes any and all combinations of one or more related listed items.
下面结合附图和具体实施例对本发明作进一步说明,以使本领域的技术人员可以更好地理解本发明并能予以实施,但所举实施例不作为对本发明的限定。The present invention will be further described below in conjunction with the accompanying drawings and specific embodiments so that those skilled in the art can better understand the present invention and implement it, but the embodiments are not intended to limit the present invention.
实施例1Example 1
本实施例涉及一种产氢生物微球的制备,制备过程如图1所示,具体操作如下:This embodiment relates to the preparation of a hydrogen-producing biomicrosphere. The preparation process is shown in FIG1 , and the specific operations are as follows:
(1)将已驯化的产气肠杆菌在8000rpm离心后,与2mL 1.5%(w/v)的海藻酸钠溶液混合,得到混合溶液,混合溶液中产气肠杆菌的密度为1×108;使用注射器(针头为0.5mm)吸取混合溶液,在静电场作用下(电压为4.5kV)利用注射泵(流速为8.2mL/h)将混合溶液匀速滴入氯化钙溶液中,凝胶化10min,自然沉淀收集100μM载产气肠杆菌的海藻酸钙凝胶微球;(1) After centrifuging the domesticated Enterobacter aerogenes at 8000 rpm, the mixture was mixed with 2 mL of 1.5% (w/v) sodium alginate solution to obtain a mixed solution, in which the density of Enterobacter aerogenes in the mixed solution was 1×10 8 ; the mixed solution was drawn up using a syringe (needle of 0.5 mm), and the mixed solution was uniformly dripped into a calcium chloride solution using a syringe pump (flow rate of 8.2 mL/h) under the action of an electrostatic field (voltage of 4.5 kV), and gelled for 10 minutes, and 100 μM calcium alginate gel microspheres carrying Enterobacter aerogenes were collected by natural precipitation;
(2)将步骤(1)中收集的载产气肠杆菌的海藻酸钙凝胶微球与10mL0.05%w/v的聚赖氨酸溶液以体积比1:10混合,并置于摇床中在转速为50rpm下反应10min,形成内部包封产气肠杆菌,表面包覆半透膜的凝胶微球(产氢生物微球)。(2) The calcium alginate gel microspheres containing Enterobacter aerogenes collected in step (1) were mixed with 10 mL of 0.05% w/v polylysine solution at a volume ratio of 1:10, and placed in a shaker for reaction at a speed of 50 rpm for 10 min to form gel microspheres (hydrogen-producing biomicrospheres) with Enterobacter aerogenes encapsulated inside and a semipermeable membrane coated on the surface.
实施例2Example 2
本实施例涉及一种产氢生物微球的制备,制备过程如图1所示,具体操作如下:This embodiment relates to the preparation of a hydrogen-producing biomicrosphere. The preparation process is shown in FIG1 , and the specific operations are as follows:
(3)将已驯化的产气肠杆菌在8000rpm离心后,与2mL 1.5%(w/v)的海藻酸钠溶液混合,得到混合溶液,混合溶液中产气肠杆菌的密度为5×107;使用注射器(针头为0.5mm)吸取混合溶液,在静电场作用下(电压为4.5kV)利用注射泵(流速为8.2mL/h)将混合溶液匀速滴入氯化钙溶液中,凝胶化10min,自然沉淀收集100μM载产气肠杆菌的海藻酸钙凝胶微球;(3) After centrifuging the domesticated Enterobacter aerogenes at 8000 rpm, the mixture was mixed with 2 mL of 1.5% (w/v) sodium alginate solution to obtain a mixed solution, in which the density of Enterobacter aerogenes in the mixed solution was 5×10 7 ; the mixed solution was drawn up using a syringe (needle of 0.5 mm), and the mixed solution was uniformly dripped into a calcium chloride solution using a syringe pump (flow rate of 8.2 mL/h) under the action of an electrostatic field (voltage of 4.5 kV), and gelled for 10 minutes, and 100 μM calcium alginate gel microspheres carrying Enterobacter aerogenes were collected by natural precipitation;
(4)将步骤(1)中收集的载产气肠杆菌的海藻酸钙凝胶微球与10mL0.05%w/v的聚赖氨酸溶液以体积比1:10混合,并置于摇床中在转速为50rpm下反应10min,形成内部包封产气肠杆菌,表面包覆半透膜的凝胶微球(产氢生物微球)。(4) The calcium alginate gel microspheres containing Enterobacter aerogenes collected in step (1) were mixed with 10 mL of 0.05% w/v polylysine solution at a volume ratio of 1:10, and placed in a shaker for reaction at a speed of 50 rpm for 10 min to form gel microspheres (hydrogen-producing biomicrospheres) with Enterobacter aerogenes encapsulated inside and a semipermeable membrane coated on the surface.
性能测试Performance Testing
配制#1培养基:向水中加入K2HPO4、NH4SO4、MgSO4、酵母提取物以及葡萄糖,混合均匀得到#1培养基,#1培养基中K2HPO4的浓度为6g/L、NH4SO4的浓度为2g/L、MgSO4的浓度为0.4g/L、酵母提取物的浓度为5g/L、葡萄糖的浓度为3g/L。Prepare medium #1: add K 2 HPO 4 , NH 4 SO 4 , MgSO 4 , yeast extract and glucose to water, mix well to obtain medium #1, in which the concentration of K 2 HPO 4 is 6 g/L, the concentration of NH 4 SO 4 is 2 g/L, the concentration of MgSO 4 is 0.4 g/L, the concentration of yeast extract is 5 g/L, and the concentration of glucose is 3 g/L.
1.微球内产气肠杆菌的稳定性1. Stability of Enterobacter aerogenes in microspheres
将实施例1制备的产氢生物微球悬浮于#1培养基中,在37℃的培养箱中培养48h,利用光学显微镜观察培养前后的微球形态,如图2所示,培养48h后的微球内部产气肠杆菌的密度显著增长,这也说明微球内的产气肠杆菌在#1培养基环境下可大量繁殖。The hydrogen-producing biomicrospheres prepared in Example 1 were suspended in #1 culture medium and cultured in an incubator at 37°C for 48 h. The morphology of the microspheres before and after the culture was observed using an optical microscope. As shown in FIG2 , the density of Enterobacter aerogenes inside the microspheres increased significantly after 48 h of culture, which also indicates that Enterobacter aerogenes inside the microspheres can multiply in large quantities in the #1 culture medium environment.
利用荧光显微镜观察上述产氢生物微球内部产气肠杆菌在培养48h后的生长情况,如图3所示,有部分产气肠杆菌死亡,但微球内仍有大量存活的产气肠杆菌,且存活的产气肠杆菌基本被包裹在微球内部,微球外部未发现明显扩散,这也说明本发明制备产氢生物微球可将产气肠杆菌很好的限制在半透膜内。The growth of Enterobacter aerogenes inside the hydrogen-producing biomicrospheres after 48 hours of culture was observed using a fluorescence microscope. As shown in FIG3 , some Enterobacter aerogenes died, but a large number of surviving Enterobacter aerogenes were still present in the microspheres, and the surviving Enterobacter aerogenes were basically encapsulated inside the microspheres, and no obvious diffusion was found outside the microspheres. This also indicates that the preparation of hydrogen-producing biomicrospheres by the present invention can well confine Enterobacter aerogenes within the semipermeable membrane.
2.产氢生物微球的产氢效率2. Hydrogen production efficiency of hydrogen-producing biomicrospheres
以硼化镁纳米片(乐研、货号1268675)作为对照品,将实施例1制备的产氢生物微球与产气肠杆菌各分别接种至#1和1640(CORNING)两种培养基中发酵,控制微球中产气肠杆菌量与单一产气肠杆菌的量相同,培养48h后测定其产氢量。测试数据以均值±标准偏差表示,采用双尾T检验与对照组进行比较,***P<0.001,*P<0.05。测试结果如图4所示:Using magnesium boride nanosheets (Leyan, item number 1268675) as a control, the hydrogen-producing biomicrospheres prepared in Example 1 and Enterobacter aerogenes were inoculated into two culture media #1 and 1640 (CORNING) for fermentation, and the amount of Enterobacter aerogenes in the microspheres was controlled to be the same as that of a single Enterobacter aerogenes. The hydrogen production was measured after 48 hours of culture. The test data are expressed as mean ± standard deviation, and compared with the control group using a two-tailed T test, *** P < 0.001, * P < 0.05. The test results are shown in Figure 4:
1640培养基为细胞培养基,驯化后的产气肠杆菌已完全适应细胞培养基的环境,在1640培养基中培养48h产氢量略高于微球且显著高于硼化镁纳米片的产氢量,这也说明产气肠杆菌及本发明制备的产氢生物微球可在类生物体内环境中具有高产氢效率。The 1640 culture medium is a cell culture medium. The domesticated Enterobacter aerogenes has fully adapted to the environment of the cell culture medium. The hydrogen production after 48 hours of culture in the 1640 culture medium is slightly higher than that of the microspheres and significantly higher than that of the magnesium boride nanosheets. This also shows that Enterobacter aerogenes and the hydrogen-producing biological microspheres prepared by the present invention can have high hydrogen production efficiency in an in vivo-like environment.
在#1培养基中,驯化后的产气肠杆菌的产氢量相对于在1640培养基中产氢量有显著下降,且远低于产氢生物微球的产氢量,而产氢生物微球在两种不同的培养基中培养48h的产氢量相近,均高于硼化镁纳米片的产氢量。这也说明本发明制备的产氢生物微球通过海藻酸钙凝胶包埋以及半透膜包裹的作用,将微球内部的产气肠杆菌与外部环境隔离,其产氢能力不会因外界环境的变化而产生较大影响,具有稳定且高效的产氢能力。In #1 medium, the hydrogen production of the domesticated Enterobacter aerogenes decreased significantly compared to that in 1640 medium, and was much lower than that of the hydrogen-producing biomicrospheres. The hydrogen production of the hydrogen-producing biomicrospheres cultured in two different mediums for 48 hours was similar, both higher than that of the magnesium boride nanosheets. This also shows that the hydrogen-producing biomicrospheres prepared by the present invention isolate the Enterobacter aerogenes inside the microspheres from the external environment through calcium alginate gel embedding and semipermeable membrane wrapping, and their hydrogen production capacity will not be greatly affected by changes in the external environment, and have stable and efficient hydrogen production capacity.
3.产氢生物微球持续产氢能力3. Continuous hydrogen production capacity of hydrogen-producing bio-microspheres
将实施例2制备的产氢生物微球接种至#1培养基中,在37℃下持续无氧发酵,每间隔24h测定产氢量并更新培养液,测试数据以均值±标准偏差表示。测试结果如图5所示:The hydrogen-producing bio-microspheres prepared in Example 2 were inoculated into the #1 culture medium and continued to ferment anaerobicly at 37°C. The hydrogen production was measured every 24 hours and the culture medium was updated. The test data was expressed as mean ± standard deviation. The test results are shown in Figure 5:
产氢生物微球的产氢量在前3天增长迅速,由~2nmol/mL增加至~23nmol/mL,第3天至第6天的产氢量相对平稳,每天的产氢量在20~27nmol/mL内波动。由此可知,本发明制备的产氢生物微球具有持续产氢能力且产氢量高。The hydrogen production of the hydrogen-producing bio-microspheres increased rapidly in the first three days, from 2 nmol/mL to 23 nmol/mL, and the hydrogen production from the third to the sixth day was relatively stable, with the daily hydrogen production fluctuating between 20 and 27 nmol/mL. It can be seen that the hydrogen-producing bio-microspheres prepared by the present invention have a continuous hydrogen production capacity and a high hydrogen production capacity.
以上所述实施例仅是为充分说明本发明而所举的较佳的施例,本发明的保护范围不限于此。本技术领域的技术人员在本发明基础上所作的等同替代或变换,均在本发明的保护范围之内。本发明的保护范围以权利要求书为准。The above-described embodiments are only preferred embodiments for fully illustrating the present invention, and the protection scope of the present invention is not limited thereto. Equivalent substitutions or changes made by those skilled in the art based on the present invention are within the protection scope of the present invention. The protection scope of the present invention shall be subject to the claims.
Claims (4)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202211493036.9A CN115737600B (en) | 2022-11-25 | 2022-11-25 | Continuous hydrogen-producing biological microsphere and preparation method and application thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202211493036.9A CN115737600B (en) | 2022-11-25 | 2022-11-25 | Continuous hydrogen-producing biological microsphere and preparation method and application thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN115737600A CN115737600A (en) | 2023-03-07 |
CN115737600B true CN115737600B (en) | 2024-05-31 |
Family
ID=85338250
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202211493036.9A Active CN115737600B (en) | 2022-11-25 | 2022-11-25 | Continuous hydrogen-producing biological microsphere and preparation method and application thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN115737600B (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA2243352A1 (en) * | 1996-01-23 | 1997-07-31 | Mcgill University | Microencapsulated genetically engineered microorganisms for clinical application |
CA2437250A1 (en) * | 2003-08-14 | 2005-02-14 | Ims Recherche Inc. | Microencapsulation of living cells in covalently crosslinked alginate-poly-l-lysine-alginate membranes |
CN102101037A (en) * | 2009-12-18 | 2011-06-22 | 中国科学院大连化学物理研究所 | Preparation method of alginate/epsilon-polylysine/alginate biological microcapsule |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9044385B2 (en) * | 2007-05-16 | 2015-06-02 | Abbott Cardiovascular Systems Inc. | Therapeutic compositions for targeted vessel delivery |
-
2022
- 2022-11-25 CN CN202211493036.9A patent/CN115737600B/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA2243352A1 (en) * | 1996-01-23 | 1997-07-31 | Mcgill University | Microencapsulated genetically engineered microorganisms for clinical application |
CA2437250A1 (en) * | 2003-08-14 | 2005-02-14 | Ims Recherche Inc. | Microencapsulation of living cells in covalently crosslinked alginate-poly-l-lysine-alginate membranes |
CN102101037A (en) * | 2009-12-18 | 2011-06-22 | 中国科学院大连化学物理研究所 | Preparation method of alginate/epsilon-polylysine/alginate biological microcapsule |
CN102101036A (en) * | 2009-12-18 | 2011-06-22 | 中国科学院大连化学物理研究所 | Alginate-epsilon-polylysine microcapsules and preparation and application thereof |
Non-Patent Citations (1)
Title |
---|
王伟东等.《微生物学》.中国农业大学出版,2015,第324-325页. * |
Also Published As
Publication number | Publication date |
---|---|
CN115737600A (en) | 2023-03-07 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Yu et al. | Hydrogen‐bonded organic framework (HOF)‐based single‐neural stem cell encapsulation and transplantation to remodel impaired neural networks | |
EP2104492B1 (en) | Oxygen supply for cell transplant and vascularization | |
CN116919648A (en) | System of stacked tissue encapsulation devices with or without oxygen delivery | |
JP3228941B2 (en) | Microencapsulated genetically engineered microorganisms for clinical use | |
Wang et al. | A Self‐Adaptive Pyroptosis Inducer: Optimizing the Catalytic Microenvironment of Nanozymes by Membrane‐Adhered Microbe Enables Potent Cancer Immunotherapy | |
CN113440640B (en) | Algae-bacterium gel dressing and preparation method thereof | |
CN115737600B (en) | Continuous hydrogen-producing biological microsphere and preparation method and application thereof | |
JP2005104987A5 (en) | ||
CN111686092B (en) | Preparation method of porous silicon graphene quantum dot composite drug-loaded particles, wound dressing, preparation method of wound dressing and application of wound dressing | |
CN113509488B (en) | Oxygen-carrying bionic nano antidote as well as preparation method and application thereof | |
CN117503731A (en) | Nanocapsule method of umbilical blood mesenchymal stem cell source exosome | |
CN114376985B (en) | A kind of 3D stem cell microsphere capsule, its preparation method and its application in the field of transplantation therapy | |
WO2000078295A1 (en) | Microencapsulated bovine adrenal medulla chromaffin cell-drug for alleviating pain | |
CN103099779A (en) | Prescription and preparation process for irinotecan hydrochloride injection | |
Prakash et al. | Artificial cells microencapsulated genetically engineered E. Coli DH 5 cells for the lowering of plasma creatinine in-vitro and in-vivo | |
Zhao et al. | Nanozymes in Biomedical Applications: Innovations Originated From Metal‐Organic Frameworks | |
CN115501348A (en) | Nano-drug carrier with anticancer activity and preparation method and application thereof | |
Garofalo et al. | Immobilization of P. Pictorijm in Open Pore Agar, Alginate and Polylysine-Alginate Microcapsules for Serum Cholesterol Depletion | |
CN115960790B (en) | Biological hybrid material capable of self-producing oxygen for long time and preparation method and application thereof | |
Feng et al. | Promoting renal I/R injury repair by in-situ electric stimulation using biodegradable piezoelectric polylactide/vitamin B2 composite nanofibrous membrane | |
Coussa et al. | Oral microencapsulated live Saccharomyces cerevisiae cells for use in renal failure uremia: preparation and in vivo analysis | |
CN116603069B (en) | Microorganism targeting implantation system and method | |
CN1324130C (en) | Flavobacterium microencapsulation | |
CN118384293B (en) | Stable and controllable multifunctional oxygen-carrying nano preparation and preparation method thereof | |
CN118903193A (en) | Medicine for hair follicle transplantation protection and minimally invasive healing by utilizing hydrogen and application of hydrogen molecules in preparation of medicine |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |