CN116813816A - A kind of preparation method of compound pullulan - Google Patents
A kind of preparation method of compound pullulan Download PDFInfo
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- 229920001218 Pullulan Polymers 0.000 title claims abstract description 50
- 239000004373 Pullulan Substances 0.000 title claims abstract description 50
- 235000019423 pullulan Nutrition 0.000 title claims abstract description 50
- 238000002360 preparation method Methods 0.000 title claims abstract description 28
- 150000001875 compounds Chemical class 0.000 title abstract description 9
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims abstract description 123
- 239000011259 mixed solution Substances 0.000 claims abstract description 76
- 239000000243 solution Substances 0.000 claims abstract description 59
- 238000006243 chemical reaction Methods 0.000 claims abstract description 55
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 26
- 238000003756 stirring Methods 0.000 claims abstract description 23
- 239000002131 composite material Substances 0.000 claims abstract description 20
- 239000002253 acid Substances 0.000 claims abstract description 19
- 238000000034 method Methods 0.000 claims abstract description 8
- 239000012528 membrane Substances 0.000 claims description 51
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 36
- 239000007788 liquid Substances 0.000 claims description 33
- 238000000108 ultra-filtration Methods 0.000 claims description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 23
- 239000007921 spray Substances 0.000 claims description 16
- 239000000843 powder Substances 0.000 claims description 13
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 12
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 12
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 12
- 239000000203 mixture Substances 0.000 claims description 12
- 239000000126 substance Substances 0.000 claims description 12
- 239000011148 porous material Substances 0.000 claims description 9
- 229910052757 nitrogen Inorganic materials 0.000 claims description 7
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 6
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 6
- 239000012141 concentrate Substances 0.000 claims description 6
- 230000009977 dual effect Effects 0.000 claims description 6
- 230000004907 flux Effects 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 6
- 229910017604 nitric acid Inorganic materials 0.000 claims description 6
- 239000012466 permeate Substances 0.000 claims description 6
- 238000001694 spray drying Methods 0.000 claims description 6
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 6
- 150000004676 glycans Chemical class 0.000 claims description 5
- 229920001282 polysaccharide Polymers 0.000 claims description 5
- 239000005017 polysaccharide Substances 0.000 claims description 5
- 230000007071 enzymatic hydrolysis Effects 0.000 abstract description 5
- 238000006047 enzymatic hydrolysis reaction Methods 0.000 abstract description 5
- 238000012271 agricultural production Methods 0.000 abstract description 3
- 241000223678 Aureobasidium pullulans Species 0.000 abstract 1
- 229920000642 polymer Polymers 0.000 abstract 1
- 239000002609 medium Substances 0.000 description 13
- 241000209140 Triticum Species 0.000 description 6
- 235000021307 Triticum Nutrition 0.000 description 6
- 239000008367 deionised water Substances 0.000 description 4
- 229910021641 deionized water Inorganic materials 0.000 description 4
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- 241000196324 Embryophyta Species 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- YBJHBAHKTGYVGT-ZKWXMUAHSA-N (+)-Biotin Chemical compound N1C(=O)N[C@@H]2[C@H](CCCCC(=O)O)SC[C@@H]21 YBJHBAHKTGYVGT-ZKWXMUAHSA-N 0.000 description 2
- VHYFNPMBLIVWCW-UHFFFAOYSA-N 4-Dimethylaminopyridine Chemical compound CN(C)C1=CC=NC=C1 VHYFNPMBLIVWCW-UHFFFAOYSA-N 0.000 description 2
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000000502 dialysis Methods 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 229920001542 oligosaccharide Polymers 0.000 description 2
- 150000002482 oligosaccharides Chemical class 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 208000035240 Disease Resistance Diseases 0.000 description 1
- 229920002683 Glycosaminoglycan Polymers 0.000 description 1
- 241000238631 Hexapoda Species 0.000 description 1
- 241000607479 Yersinia pestis Species 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 229960002685 biotin Drugs 0.000 description 1
- 235000020958 biotin Nutrition 0.000 description 1
- 239000011616 biotin Substances 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000001963 growth medium Substances 0.000 description 1
- 238000003306 harvesting Methods 0.000 description 1
- 230000036039 immunity Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000003755 preservative agent Substances 0.000 description 1
- 230000002335 preservative effect Effects 0.000 description 1
- 239000002688 soil aggregate Substances 0.000 description 1
- 230000009885 systemic effect Effects 0.000 description 1
- 239000002562 thickening agent Substances 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B37/00—Preparation of polysaccharides not provided for in groups C08B1/00 - C08B35/00; Derivatives thereof
- C08B37/0006—Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid
- C08B37/0009—Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid alpha-D-Glucans, e.g. polydextrose, alternan, glycogen; (alpha-1,4)(alpha-1,6)-D-Glucans; (alpha-1,3)(alpha-1,4)-D-Glucans, e.g. isolichenan or nigeran; (alpha-1,4)-D-Glucans; (alpha-1,3)-D-Glucans, e.g. pseudonigeran; Derivatives thereof
- C08B37/0018—Pullulan, i.e. (alpha-1,4)(alpha-1,6)-D-glucan; Derivatives thereof
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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- Chemical & Material Sciences (AREA)
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- Biochemistry (AREA)
- Molecular Biology (AREA)
- Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
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Abstract
本发明公开了一种复合出芽短梗霉聚糖的制备方法,涉及复合出芽短梗霉聚糖制备方法技术领域,该制备方法旨在解决现有技术下采用生物酶解进行制备,其成本较高,不能提高作物抗逆性的技术问题,该制备方法,其步骤如下:步骤一:配制1%的乙酸溶液;步骤二:将普鲁兰多糖溶解于步骤一的乙酸溶液中,并充分搅拌均匀,得到混合溶液一;步骤三:往混合溶液一内加入双氧水,并充分搅拌,得到混合溶液二,步骤四:设定反应釜的内部温度和转速,混合溶液二加入反应釜内,并加入酸,反应至1h时,取出反应液的1/10,该制备方法其工艺简单,与生物酶解相比具有成本低廉的优点,实现了大规模农业生产应用,制备的复合出芽短梗霉聚糖,并提高作物的抗逆性。The invention discloses a preparation method of compound pullulan, and relates to the technical field of preparation methods of compound pullulan. The preparation method aims to solve the problem of using biological enzymatic hydrolysis for preparation under the existing technology, and its cost is relatively low. High and unable to improve crop stress resistance, the preparation method has the following steps: Step 1: Prepare a 1% acetic acid solution; Step 2: Dissolve pullulan in the acetic acid solution of Step 1, and stir thoroughly uniformly to obtain mixed solution one; step three: add hydrogen peroxide into mixed solution one and stir thoroughly to obtain mixed solution two; step four: set the internal temperature and rotation speed of the reaction kettle, add mixed solution two into the reaction kettle, and add Acid, when the reaction reaches 1 hour, take out 1/10 of the reaction solution. This preparation method has a simple process and has the advantage of low cost compared with biological enzymatic hydrolysis. It has realized large-scale agricultural production and application. The prepared composite Aureobasidium pullulans polymer sugar and improve crop stress resistance.
Description
技术领域Technical field
本发明属于复合出芽短梗霉聚糖制备方法技术领域,具体涉及一种复合出芽短梗霉聚糖的制备方法。The invention belongs to the technical field of preparation methods of compound pullulan, and specifically relates to a preparation method of compound pullulan.
背景技术Background technique
普鲁兰多糖是一种以玉米为原料发酵而成的胞外水溶性粘质多糖,又名短梗霉多糖,在农业生产上,多糖喷雾可用作增稠剂和保鲜剂,多糖施入土壤,可改善土壤团粒结构,面对各种胁迫条件,寡糖可以激发植物自身的免疫能力,使植物获得系统性抗性,提高植物的抗病、抗虫、抗逆性,达到预防病虫害的目的。Pullulan is an extracellular water-soluble mucopolysaccharide fermented from corn, also known as pullulan. In agricultural production, polysaccharide spray can be used as a thickener and preservative. Soil can improve the soil aggregate structure. In the face of various stress conditions, oligosaccharides can stimulate the plant's own immunity, enable the plant to acquire systemic resistance, improve the plant's disease resistance, insect resistance, and stress resistance, and achieve the purpose of preventing pests and diseases. Purpose.
目前,专利号为CN202011443169.6的发明专利公开了一种生物素化出芽短梗酶多糖衍生物的制备方法,包括以下步骤:(1)在锥形瓶中一次加入无水二甲基亚砜、生物素、N,N’-二环已基碳酰亚胺和4-二甲基氨基吡啶,室温下反应0.5-1h,然后加入出芽短梗酶多糖,继续在室温下反应1-2h,直至白色浑浊物析出,得到浑浊溶液;(2)过滤步骤1中得到的浑浊溶液,进行一次均质得到溶液1,静置3-5h后,出去表面杂质及上层溶液,得到溶液1;(3)将溶液1的白色浑浊物过滤除去,收集滤液放入截留分子量为9000Da的透析袋中,加入去离子水透析4-8d,每隔1h更换一次去离子水,透析结束后,抽滤得到白色沉淀,依次用二氯甲烷和去离子水洗涤白色沉淀,干燥,得到生物素化出芽短梗酶多糖衍生物,其可以适应高温热加工工序,但该出芽短梗霉聚糖采用生物酶解进行制备,其成本较高,且制备工艺较为繁琐,出芽短梗霉聚糖对促进作物的生长效果不明显,不能提高作物的抗逆性。Currently, the invention patent with patent number CN202011443169.6 discloses a method for preparing biotinylated pullulase polysaccharide derivatives, which includes the following steps: (1) Add anhydrous dimethyl sulfoxide once in an Erlenmeyer flask , biotin, N,N'-dicyclohexylcarboimide and 4-dimethylaminopyridine, react at room temperature for 0.5-1h, then add pullulase polysaccharide, continue to react at room temperature for 1-2h, Until the white turbid matter precipitates, a turbid solution is obtained; (2) Filter the turbid solution obtained in step 1, homogenize once to obtain solution 1, let it stand for 3-5 hours, remove the surface impurities and the upper layer solution, and obtain solution 1; (3) ) Filter out the white turbidity in solution 1, collect the filtrate and put it into a dialysis bag with a molecular weight cutoff of 9000Da. Add deionized water to dialyze for 4-8 days. Replace the deionized water every 1 hour. After the dialysis is completed, suction filtrate to obtain white Precipitate, wash the white precipitate with dichloromethane and deionized water in sequence, and dry to obtain a biotinylated pullulan polysaccharide derivative, which can adapt to high-temperature thermal processing processes, but the pullulan is processed by biological enzymatic hydrolysis The preparation cost is high and the preparation process is complicated. Pullulan has no obvious effect on promoting the growth of crops and cannot improve the stress resistance of crops.
因此,针对上述成本高和不能提高作物抗逆性的问题,亟需得到解决,以改善复合出芽短梗霉聚糖的使用场景。Therefore, the above-mentioned problems of high cost and inability to improve crop stress resistance need to be solved urgently to improve the use scenarios of compound pullulan.
发明内容Contents of the invention
(1)要解决的技术问题(1) Technical problems to be solved
针对现有技术的不足,本发明的目的在于提供一种复合出芽短梗霉聚糖的制备方法,该制备方法旨在解决现有技术下采用生物酶解进行制备,其成本较高,不能提高作物抗逆性的技术问题。In view of the shortcomings of the existing technology, the purpose of the present invention is to provide a preparation method of compound pullulan. This preparation method is intended to solve the problem of using biological enzymatic hydrolysis for preparation under the existing technology, which has a high cost and cannot be improved. Technical issues in crop stress resistance.
(2)技术方案(2)Technical solutions
为了解决上述技术问题,本发明提供了这样一种复合出芽短梗霉聚糖的制备方法,其步骤如下:In order to solve the above technical problems, the present invention provides such a preparation method of composite pullulan, the steps of which are as follows:
步骤一:配制1%的乙酸溶液;Step 1: Prepare 1% acetic acid solution;
步骤二:将普鲁兰多糖溶解于步骤一的乙酸溶液中,并充分搅拌均匀,得到混合溶液一;Step 2: Dissolve pullulan in the acetic acid solution of step 1, and stir thoroughly to obtain mixed solution 1;
步骤三:往混合溶液一内加入双氧水,并充分搅拌,得到混合溶液二;Step 3: Add hydrogen peroxide into mixed solution one and stir thoroughly to obtain mixed solution two;
步骤四:设定反应釜的内部温度和转速,混合溶液二加入反应釜内,并加入酸,反应至1h时,取出反应液的1/10;Step 4: Set the internal temperature and rotation speed of the reaction kettle, add mixed solution 2 into the reaction kettle, and add acid. When the reaction reaches 1 hour, take out 1/10 of the reaction solution;
步骤五:然后继续反应至4h时,反应结束,取出反应液;Step 5: Then continue the reaction for 4 hours. When the reaction is completed, take out the reaction solution;
步骤六:将步骤四和步骤五中的反应液倒入搅拌机内,设定搅拌速度和时间,使其充分混合均匀,得到混合溶液三;Step 6: Pour the reaction solution in step 4 and step 5 into the mixer, set the stirring speed and time, and mix it thoroughly to obtain mixed solution three;
步骤七:用pH试纸或pH计来测试混合溶液三的pH值,然后逐渐加入氢氧化钾,调节混合溶液三的pH值,直至符合pH值要求后停止加入氢氧化钾,得到混合溶液四;Step 7: Use pH test paper or a pH meter to test the pH value of mixed solution three, and then gradually add potassium hydroxide to adjust the pH value of mixed solution three until the pH value is met. Stop adding potassium hydroxide to obtain mixed solution four;
步骤八:超滤设备对混合溶液四进行浓缩,以膜两侧的压力差为驱动力,以超滤膜为过滤介质,在一定的压力下,当混合溶液四流过膜表面时,超滤膜表面密布的许多细小的微孔只允许水及小分子物质通过而成为透过液,而混合溶液四中体积大于膜表面微孔径的物质则被截留在膜的进液侧,成为浓缩液;Step 8: The ultrafiltration equipment concentrates the mixed solution IV, using the pressure difference on both sides of the membrane as the driving force, and the ultrafiltration membrane as the filter medium. Under a certain pressure, when the mixed solution IV flows through the membrane surface, the ultrafiltration The many tiny pores densely covered on the membrane surface only allow water and small molecular substances to pass through and become the permeate, while the substances in the mixed solution 4 that are larger than the pore size on the membrane surface are trapped on the inlet side of the membrane and become concentrated liquid;
步骤九:使用喷雾干燥设备对浓缩液进行干燥,浓缩液由料泵加压后通过管道经喷嘴进入喷雾塔,设定喷雾压力,浓缩液雾化形成小液滴,在表面张力和热氮气的双重作用下,液滴收缩成球状,液体介质被蒸发,粉末从塔底部收集,得到复合出芽短梗霉聚糖粉末。Step 9: Use spray drying equipment to dry the concentrated liquid. The concentrated liquid is pressurized by the material pump and enters the spray tower through the pipe and nozzle. Set the spray pressure and the concentrated liquid is atomized to form small droplets. Under the influence of surface tension and hot nitrogen, Under the dual action, the droplets shrink into spherical shapes, the liquid medium is evaporated, and the powder is collected from the bottom of the tower to obtain composite pullulan powder.
进一步地,所述配制1%的乙酸溶液的具体步骤为:按1:100的比例准备乙酸和水,然后将乙酸和水充分混合均匀,得到1%的乙酸溶液。Further, the specific steps for preparing a 1% acetic acid solution are: prepare acetic acid and water in a ratio of 1:100, and then mix the acetic acid and water thoroughly to obtain a 1% acetic acid solution.
进一步地,所述普鲁兰多糖与乙酸溶液的重量比为1:0.5-20。Further, the weight ratio of the pullulan to the acetic acid solution is 1:0.5-20.
进一步地,所述混合溶液一和双氧水的重量比为1:10。Further, the weight ratio of the mixed solution 1 and hydrogen peroxide is 1:10.
进一步地,所述酸为浓盐酸、浓硫酸、硝酸和磷酸中的任意一种或多种,普鲁兰多糖和酸的重量比为1-4:10-100。Further, the acid is any one or more of concentrated hydrochloric acid, concentrated sulfuric acid, nitric acid and phosphoric acid, and the weight ratio of pullulan and acid is 1-4:10-100.
进一步地,所述设定的反应釜内部温度为50-99℃、转速为400r/min。Further, the set internal temperature of the reaction kettle is 50-99°C, and the rotation speed is 400 r/min.
进一步地,所述设定的搅拌速度为30-200r/min、时间为5-10分钟。Further, the set stirring speed is 30-200r/min and the time is 5-10 minutes.
进一步地,所述pH值要求为pH值等于7.0。Further, the pH value requirement is that the pH value is equal to 7.0.
进一步地,所述超滤设备的操作压力为0.11-0.6Mpa、超滤膜的膜通量为1-500L/㎡h。Further, the operating pressure of the ultrafiltration equipment is 0.11-0.6Mpa, and the membrane flux of the ultrafiltration membrane is 1-500L/㎡h.
进一步地,所述喷雾压力为0.65-1.2MPa。Further, the spray pressure is 0.65-1.2MPa.
(3)有益效果(3) Beneficial effects
与现有技术相比,本发明的有益效果在于:本发明的制备方法其工艺简单,与生物酶解相比具有成本低廉的优点,且生产过程安全,无有害气体产生,不会对环境造成影响,工艺简单,实现了大规模农业生产应用,制备的复合出芽短梗霉聚糖,能够在土壤微生物的作用下,逐步降解为寡糖,从而延长促进作物生长,并提高作物的抗逆性。Compared with the existing technology, the beneficial effects of the present invention are: the preparation method of the present invention has a simple process, has the advantage of low cost compared with biological enzymatic hydrolysis, and the production process is safe, no harmful gas is generated, and does not cause any harm to the environment. Impact, the process is simple, and large-scale agricultural production applications have been realized. The prepared compound pullulan can gradually degrade into oligosaccharides under the action of soil microorganisms, thereby prolonging and promoting crop growth and improving crop stress resistance. .
具体实施方式Detailed ways
本具体实施方式是复合出芽短梗霉聚糖的制备方法,其步骤如下:This specific embodiment is a preparation method of composite pullulan, and the steps are as follows:
步骤一:配制1%的乙酸溶液;Step 1: Prepare 1% acetic acid solution;
步骤二:将普鲁兰多糖溶解于步骤一的乙酸溶液中,并充分搅拌均匀,得到混合溶液一;Step 2: Dissolve pullulan in the acetic acid solution of step 1, and stir thoroughly to obtain mixed solution 1;
步骤三:往混合溶液一内加入双氧水,并充分搅拌,得到混合溶液二;Step 3: Add hydrogen peroxide into mixed solution one and stir thoroughly to obtain mixed solution two;
步骤四:设定反应釜的内部温度和转速,混合溶液二加入反应釜内,并加入酸,反应至1h时,取出反应液的1/10;Step 4: Set the internal temperature and rotation speed of the reaction kettle, add mixed solution 2 into the reaction kettle, and add acid. When the reaction reaches 1 hour, take out 1/10 of the reaction solution;
步骤五:然后继续反应至4h时,反应结束,取出反应液;Step 5: Then continue the reaction for 4 hours. When the reaction is completed, take out the reaction solution;
步骤六:将步骤四和步骤五中的反应液倒入搅拌机内,设定搅拌速度和时间,使其充分混合均匀,得到混合溶液三;Step 6: Pour the reaction solution in step 4 and step 5 into the mixer, set the stirring speed and time, and mix it thoroughly to obtain mixed solution three;
步骤七:用pH试纸或pH计来测试混合溶液三的pH值,然后逐渐加入氢氧化钾,调节混合溶液三的pH值,直至符合pH值要求后停止加入氢氧化钾,得到混合溶液四;Step 7: Use pH test paper or a pH meter to test the pH value of mixed solution three, and then gradually add potassium hydroxide to adjust the pH value of mixed solution three until the pH value is met. Stop adding potassium hydroxide to obtain mixed solution four;
步骤八:超滤设备对混合溶液四进行浓缩,以膜两侧的压力差为驱动力,以超滤膜为过滤介质,在一定的压力下,当混合溶液四流过膜表面时,超滤膜表面密布的许多细小的微孔只允许水及小分子物质通过而成为透过液,而混合溶液四中体积大于膜表面微孔径的物质则被截留在膜的进液侧,成为浓缩液;Step 8: The ultrafiltration equipment concentrates the mixed solution IV, using the pressure difference on both sides of the membrane as the driving force, and the ultrafiltration membrane as the filter medium. Under a certain pressure, when the mixed solution IV flows through the membrane surface, the ultrafiltration The many tiny pores densely covered on the membrane surface only allow water and small molecular substances to pass through and become the permeate, while the substances in the mixed solution 4 that are larger than the pore size on the membrane surface are trapped on the inlet side of the membrane and become concentrated liquid;
步骤九:使用喷雾干燥设备对浓缩液进行干燥,浓缩液由料泵加压后通过管道经喷嘴进入喷雾塔,设定喷雾压力,浓缩液雾化形成小液滴,在表面张力和热氮气的双重作用下,液滴收缩成球状,液体介质被蒸发,粉末从塔底部收集,得到复合出芽短梗霉聚糖粉末。Step 9: Use spray drying equipment to dry the concentrated liquid. The concentrated liquid is pressurized by the material pump and enters the spray tower through the pipe and nozzle. Set the spray pressure and the concentrated liquid is atomized to form small droplets. Under the influence of surface tension and hot nitrogen, Under the dual action, the droplets shrink into spherical shapes, the liquid medium is evaporated, and the powder is collected from the bottom of the tower to obtain composite pullulan powder.
进一步地,所述配制1%的乙酸溶液的具体步骤为:按1:100的比例准备乙酸和水,然后将乙酸和水充分混合均匀,得到1%的乙酸溶液。Further, the specific steps for preparing a 1% acetic acid solution are: prepare acetic acid and water in a ratio of 1:100, and then mix the acetic acid and water thoroughly to obtain a 1% acetic acid solution.
进一步地,所述普鲁兰多糖与乙酸溶液的重量比为1:0.5-20。Further, the weight ratio of the pullulan to the acetic acid solution is 1:0.5-20.
进一步地,所述混合溶液一和双氧水的重量比为1:10。Further, the weight ratio of the mixed solution 1 and hydrogen peroxide is 1:10.
进一步地,所述酸为浓盐酸、浓硫酸、硝酸和磷酸中的任意一种或多种,普鲁兰多糖和酸的重量比为1-4:10-100。Further, the acid is any one or more of concentrated hydrochloric acid, concentrated sulfuric acid, nitric acid and phosphoric acid, and the weight ratio of pullulan and acid is 1-4:10-100.
进一步地,所述设定的反应釜内部温度为50-99℃、转速为400r/min。Further, the set internal temperature of the reaction kettle is 50-99°C, and the rotation speed is 400 r/min.
进一步地,所述设定的搅拌速度为30-200r/min、时间为5-10分钟。Further, the set stirring speed is 30-200r/min and the time is 5-10 minutes.
进一步地,所述pH值要求为pH值等于7.0。Further, the pH value requirement is that the pH value is equal to 7.0.
进一步地,所述超滤设备的操作压力为0.11-0.6Mpa、超滤膜的膜通量为1-500L/㎡h。Further, the operating pressure of the ultrafiltration equipment is 0.11-0.6Mpa, and the membrane flux of the ultrafiltration membrane is 1-500L/㎡h.
进一步地,所述喷雾压力为0.65-1.2MPa。Further, the spray pressure is 0.65-1.2MPa.
实施例1Example 1
使用本技术方案的制备方法时,其步骤如下:When using the preparation method of this technical solution, the steps are as follows:
步骤一:配制1%的乙酸溶液:按1:100的比例准备乙酸和水,然后将乙酸和水充分混合均匀,得到1%的乙酸溶液;Step 1: Prepare a 1% acetic acid solution: Prepare acetic acid and water in a ratio of 1:100, then mix the acetic acid and water thoroughly to obtain a 1% acetic acid solution;
步骤二:将普鲁兰多糖溶解于步骤一的乙酸溶液中,普鲁兰多糖与乙酸溶液的重量比为1:0.5,并充分搅拌均匀,得到混合溶液一;Step 2: Dissolve pullulan in the acetic acid solution of step 1. The weight ratio of pullulan to acetic acid solution is 1:0.5, and stir thoroughly to obtain mixed solution 1;
步骤三:往混合溶液一内加入双氧水,混合溶液一和双氧水的重量比为1:10,并充分搅拌,得到混合溶液二;Step 3: Add hydrogen peroxide into mixed solution one. The weight ratio of mixed solution one and hydrogen peroxide is 1:10, and stir thoroughly to obtain mixed solution two;
步骤四:设定反应釜内部温度为50℃、转速为400r/min,混合溶液二加入反应釜内,并加入酸,酸为浓盐酸、浓硫酸、硝酸和磷酸中的任意一种或多种,普鲁兰多糖和酸的重量比为1:10,反应至1h时,取出反应液的1/10;Step 4: Set the internal temperature of the reaction kettle to 50°C and the rotation speed to 400r/min. Add mixed solution 2 into the reaction kettle and add acid. The acid is any one or more of concentrated hydrochloric acid, concentrated sulfuric acid, nitric acid and phosphoric acid. , the weight ratio of pullulan and acid is 1:10, when the reaction reaches 1 hour, take out 1/10 of the reaction solution;
步骤五:然后继续反应至4h时,反应结束,取出反应液;Step 5: Then continue the reaction for 4 hours. When the reaction is completed, take out the reaction solution;
步骤六:将步骤四和步骤五中的反应液倒入搅拌机内,设定的搅拌速度为30r/min、时间为10分钟,使其充分混合均匀,得到混合溶液三;Step 6: Pour the reaction solution in step 4 and step 5 into the mixer, set the stirring speed to 30r/min and the time to 10 minutes, and mix it thoroughly to obtain mixed solution three;
步骤七:用pH试纸或pH计来测试混合溶液三的pH值,然后逐渐加入氢氧化钾,调节混合溶液三的pH值,直至符合pH值要求后停止加入氢氧化钾,得到混合溶液四,pH值要求为pH值等于7.0;Step 7: Use pH test paper or pH meter to test the pH value of mixed solution three, and then gradually add potassium hydroxide to adjust the pH value of mixed solution three until the pH value meets the requirements. Stop adding potassium hydroxide to obtain mixed solution four. The pH value requirement is that the pH value is equal to 7.0;
步骤八:超滤设备对混合溶液四进行浓缩,超滤设备的操作压力为0.11Mpa、超滤膜的膜通量为500L/㎡h,以膜两侧的压力差为驱动力,以超滤膜为过滤介质,在一定的压力下,当混合溶液四流过膜表面时,超滤膜表面密布的许多细小的微孔只允许水及小分子物质通过而成为透过液,而混合溶液四中体积大于膜表面微孔径的物质则被截留在膜的进液侧,成为浓缩液;Step 8: The ultrafiltration equipment concentrates the mixed solution 4. The operating pressure of the ultrafiltration equipment is 0.11Mpa, and the membrane flux of the ultrafiltration membrane is 500L/㎡h. The pressure difference on both sides of the membrane is used as the driving force. The membrane is a filtration medium. Under a certain pressure, when the mixed solution 4 flows through the membrane surface, the many tiny pores densely covered on the surface of the ultrafiltration membrane only allow water and small molecular substances to pass through and become the permeate, while the mixed solution 4 flows through the membrane surface. Substances with a medium volume larger than the micropore size on the membrane surface are trapped on the liquid inlet side of the membrane and become concentrated liquid;
步骤九:使用喷雾干燥设备对浓缩液进行干燥,浓缩液由料泵加压后通过管道经喷嘴进入喷雾塔,设定喷雾压力为0.65MPa,浓缩液雾化形成小液滴,在表面张力和热氮气的双重作用下,液滴收缩成球状,液体介质被蒸发,粉末从塔底部收集,得到复合出芽短梗霉聚糖粉末。Step 9: Use spray drying equipment to dry the concentrated liquid. The concentrated liquid is pressurized by the material pump and enters the spray tower through the pipe and nozzle. The spray pressure is set to 0.65MPa. The concentrated liquid is atomized to form small droplets. The surface tension and Under the dual action of hot nitrogen, the droplets shrink into spherical shapes, the liquid medium is evaporated, and the powder is collected from the bottom of the tower to obtain composite pullulan powder.
实施例2Example 2
使用本技术方案的制备方法时,其步骤如下:When using the preparation method of this technical solution, the steps are as follows:
步骤一:配制1%的乙酸溶液:按1:100的比例准备乙酸和水,然后将乙酸和水充分混合均匀,得到1%的乙酸溶液;Step 1: Prepare a 1% acetic acid solution: Prepare acetic acid and water in a ratio of 1:100, then mix the acetic acid and water thoroughly to obtain a 1% acetic acid solution;
步骤二:将普鲁兰多糖溶解于步骤一的乙酸溶液中,普鲁兰多糖与乙酸溶液的重量比为1:20,并充分搅拌均匀,得到混合溶液一;Step 2: Dissolve pullulan in the acetic acid solution of step 1. The weight ratio of pullulan to acetic acid solution is 1:20, and stir thoroughly to obtain mixed solution 1;
步骤三:往混合溶液一内加入双氧水,混合溶液一和双氧水的重量比为1:10,并充分搅拌,得到混合溶液二;Step 3: Add hydrogen peroxide into mixed solution one. The weight ratio of mixed solution one and hydrogen peroxide is 1:10, and stir thoroughly to obtain mixed solution two;
步骤四:设定反应釜内部温度为99℃、转速为400r/min,混合溶液二加入反应釜内,并加入酸,酸为浓盐酸、浓硫酸、硝酸和磷酸中的任意一种或多种,普鲁兰多糖和酸的重量比为4:100,反应至1h时,取出反应液的1/10;Step 4: Set the internal temperature of the reaction kettle to 99°C and the rotation speed to 400r/min. Add mixed solution 2 into the reaction kettle and add acid. The acid is any one or more of concentrated hydrochloric acid, concentrated sulfuric acid, nitric acid and phosphoric acid. , the weight ratio of pullulan and acid is 4:100, when the reaction reaches 1 hour, take out 1/10 of the reaction solution;
步骤五:然后继续反应至4h时,反应结束,取出反应液;Step 5: Then continue the reaction for 4 hours. When the reaction is completed, take out the reaction solution;
步骤六:将步骤四和步骤五中的反应液倒入搅拌机内,设定的搅拌速度为200r/min、时间为5分钟,使其充分混合均匀,得到混合溶液三;Step 6: Pour the reaction solution in step 4 and step 5 into the mixer, set the stirring speed to 200r/min and the time to 5 minutes, and mix it thoroughly to obtain mixed solution three;
步骤七:用pH试纸或pH计来测试混合溶液三的pH值,然后逐渐加入氢氧化钾,调节混合溶液三的pH值,直至符合pH值要求后停止加入氢氧化钾,得到混合溶液四,pH值要求为pH值等于7.0;Step 7: Use pH test paper or pH meter to test the pH value of mixed solution three, and then gradually add potassium hydroxide to adjust the pH value of mixed solution three until the pH value meets the requirements. Stop adding potassium hydroxide to obtain mixed solution four. The pH value requirement is that the pH value is equal to 7.0;
步骤八:超滤设备对混合溶液四进行浓缩,超滤设备的操作压力为0.6Mpa、超滤膜的膜通量为1L/㎡h,以膜两侧的压力差为驱动力,以超滤膜为过滤介质,在一定的压力下,当混合溶液四流过膜表面时,超滤膜表面密布的许多细小的微孔只允许水及小分子物质通过而成为透过液,而混合溶液四中体积大于膜表面微孔径的物质则被截留在膜的进液侧,成为浓缩液;Step 8: The ultrafiltration equipment concentrates the mixed solution 4. The operating pressure of the ultrafiltration equipment is 0.6Mpa, and the membrane flux of the ultrafiltration membrane is 1L/㎡h. The pressure difference on both sides of the membrane is used as the driving force. The membrane is a filtration medium. Under a certain pressure, when the mixed solution 4 flows through the membrane surface, the many tiny pores densely covered on the surface of the ultrafiltration membrane only allow water and small molecular substances to pass through and become the permeate, while the mixed solution 4 flows through the membrane surface. Substances with a medium volume larger than the micropore size on the membrane surface are trapped on the liquid inlet side of the membrane and become concentrated liquid;
步骤九:使用喷雾干燥设备对浓缩液进行干燥,浓缩液由料泵加压后通过管道经喷嘴进入喷雾塔,设定喷雾压力为1.2MPa,浓缩液雾化形成小液滴,在表面张力和热氮气的双重作用下,液滴收缩成球状,液体介质被蒸发,粉末从塔底部收集,得到复合出芽短梗霉聚糖粉末。Step 9: Use spray drying equipment to dry the concentrated liquid. The concentrated liquid is pressurized by the material pump and enters the spray tower through the pipe and nozzle. The spray pressure is set to 1.2MPa. The concentrated liquid is atomized to form small droplets. The surface tension and Under the dual action of hot nitrogen, the droplets shrink into spherical shapes, the liquid medium is evaporated, and the powder is collected from the bottom of the tower to obtain composite pullulan powder.
实施例3Example 3
使用本技术方案的制备方法时,其步骤如下:When using the preparation method of this technical solution, the steps are as follows:
步骤一:配制1%的乙酸溶液:按1:100的比例准备乙酸和水,然后将乙酸和水充分混合均匀,得到1%的乙酸溶液;Step 1: Prepare a 1% acetic acid solution: Prepare acetic acid and water in a ratio of 1:100, then mix the acetic acid and water thoroughly to obtain a 1% acetic acid solution;
步骤二:将普鲁兰多糖溶解于步骤一的乙酸溶液中,普鲁兰多糖与乙酸溶液的重量比为1:2,并充分搅拌均匀,得到混合溶液一;Step 2: Dissolve pullulan in the acetic acid solution of step 1. The weight ratio of pullulan to acetic acid solution is 1:2, and stir thoroughly to obtain mixed solution 1;
步骤三:往混合溶液一内加入双氧水,混合溶液一和双氧水的重量比为1:10,并充分搅拌,得到混合溶液二;Step 3: Add hydrogen peroxide into mixed solution one. The weight ratio of mixed solution one and hydrogen peroxide is 1:10, and stir thoroughly to obtain mixed solution two;
步骤四:设定反应釜内部温度为70℃、转速为400r/min,混合溶液二加入反应釜内,并加入酸,酸为浓盐酸、浓硫酸、硝酸和磷酸中的任意一种或多种,普鲁兰多糖和酸的重量比为1:8,反应至1h时,取出反应液的1/10;Step 4: Set the internal temperature of the reaction kettle to 70°C and the rotation speed to 400r/min. Add mixed solution 2 into the reaction kettle and add acid. The acid is any one or more of concentrated hydrochloric acid, concentrated sulfuric acid, nitric acid and phosphoric acid. , the weight ratio of pullulan and acid is 1:8, when the reaction reaches 1 hour, take out 1/10 of the reaction solution;
步骤五:然后继续反应至4h时,反应结束,取出反应液;Step 5: Then continue the reaction for 4 hours. When the reaction is completed, take out the reaction solution;
步骤六:将步骤四和步骤五中的反应液倒入搅拌机内,设定的搅拌速度为100r/min、时间为8分钟,使其充分混合均匀,得到混合溶液三;Step 6: Pour the reaction solution in step 4 and step 5 into the mixer, set the stirring speed to 100r/min and the time to 8 minutes, and mix it thoroughly to obtain mixed solution three;
步骤七:用pH试纸或pH计来测试混合溶液三的pH值,然后逐渐加入氢氧化钾,调节混合溶液三的pH值,直至符合pH值要求后停止加入氢氧化钾,得到混合溶液四,pH值要求为pH值等于7.0;Step 7: Use pH test paper or pH meter to test the pH value of mixed solution three, and then gradually add potassium hydroxide to adjust the pH value of mixed solution three until the pH value meets the requirements. Stop adding potassium hydroxide to obtain mixed solution four. The pH value requirement is that the pH value is equal to 7.0;
步骤八:超滤设备对混合溶液四进行浓缩,超滤设备的操作压力为0.3Mpa、超滤膜的膜通量为200L/㎡h,以膜两侧的压力差为驱动力,以超滤膜为过滤介质,在一定的压力下,当混合溶液四流过膜表面时,超滤膜表面密布的许多细小的微孔只允许水及小分子物质通过而成为透过液,而混合溶液四中体积大于膜表面微孔径的物质则被截留在膜的进液侧,成为浓缩液;Step 8: The ultrafiltration equipment concentrates the mixed solution 4. The operating pressure of the ultrafiltration equipment is 0.3Mpa, and the membrane flux of the ultrafiltration membrane is 200L/㎡h. The pressure difference on both sides of the membrane is used as the driving force. The membrane is a filtration medium. Under a certain pressure, when the mixed solution 4 flows through the membrane surface, the many tiny pores densely covered on the surface of the ultrafiltration membrane only allow water and small molecular substances to pass through and become the permeate, while the mixed solution 4 flows through the membrane surface. Substances with a medium volume larger than the micropore size on the membrane surface are trapped on the liquid inlet side of the membrane and become concentrated liquid;
步骤九:使用喷雾干燥设备对浓缩液进行干燥,浓缩液由料泵加压后通过管道经喷嘴进入喷雾塔,设定喷雾压力为0.85MPa,浓缩液雾化形成小液滴,在表面张力和热氮气的双重作用下,液滴收缩成球状,液体介质被蒸发,粉末从塔底部收集,得到复合出芽短梗霉聚糖粉末。Step 9: Use spray drying equipment to dry the concentrated liquid. The concentrated liquid is pressurized by the material pump and enters the spray tower through the pipe and nozzle. The spray pressure is set to 0.85MPa. The concentrated liquid is atomized to form small droplets. The surface tension and Under the dual action of hot nitrogen, the droplets shrink into spherical shapes, the liquid medium is evaporated, and the powder is collected from the bottom of the tower to obtain composite pullulan powder.
实验例Experimental example
进行水培小麦试验,供试品种为济麦22,分别使用实施例1、实施例2和实施例3制备的复合出芽短梗霉聚糖粉末,试验步骤如下:A hydroponic wheat test was carried out. The test variety was Jimai 22. The composite pullulan powder prepared in Example 1, Example 2 and Example 3 was used respectively. The test steps were as follows:
S1:种子的处理:根据试验用量,在培养皿中加入适量小麦种子,然后添加去离子水,使水没过小麦种子,轻微摇动培养皿,使种子浸入水中,24h;S1: Treatment of seeds: According to the test amount, add an appropriate amount of wheat seeds to the petri dish, then add deionized water to cover the wheat seeds, shake the petri dish slightly to immerse the seeds in water, and wait for 24 hours;
S2:配制培养液:复合出芽短梗霉聚糖,稀释500倍;S2: Prepare culture medium: compound pullulan, diluted 500 times;
S3:清洗烧杯、定植篮,将定植篮置入烧杯;S3: Clean the beaker and planting basket, and place the planting basket into the beaker;
S4:用镊子将种子置入烧杯,每个烧杯内不少于10粒种子,设置3烧杯;S4: Use tweezers to place the seeds into beakers, with no less than 10 seeds in each beaker, and set up 3 beakers;
S5:将准备好的培养液分别倒入不同的烧杯,至页面刚好没过小麦种子;S5: Pour the prepared culture solution into different beakers until the page just covers the wheat seeds;
S6:小麦生长至第七天,收获小麦,测量数据。S6: Wheat grows to the seventh day, harvests the wheat, and measures the data.
表1为实施例1、实施例2和实施例3在实验例下的测定数据。Table 1 shows the measurement data of Example 1, Example 2 and Example 3 under experimental examples.
表1。Table 1.
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| US4090016A (en) * | 1975-06-17 | 1978-05-16 | Sumitomo Chemical Company, Limited | Carboxylated pullulan and method for producing same |
| CN103570842A (en) * | 2013-11-07 | 2014-02-12 | 镇江东方生物工程设备技术有限责任公司 | Extracting method of pullulan |
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Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4090016A (en) * | 1975-06-17 | 1978-05-16 | Sumitomo Chemical Company, Limited | Carboxylated pullulan and method for producing same |
| CN103570842A (en) * | 2013-11-07 | 2014-02-12 | 镇江东方生物工程设备技术有限责任公司 | Extracting method of pullulan |
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