CN108203721A - A kind of method that zymomonas mobilis utilizes corn producing and ethanol - Google Patents
A kind of method that zymomonas mobilis utilizes corn producing and ethanol Download PDFInfo
- Publication number
- CN108203721A CN108203721A CN201611168633.9A CN201611168633A CN108203721A CN 108203721 A CN108203721 A CN 108203721A CN 201611168633 A CN201611168633 A CN 201611168633A CN 108203721 A CN108203721 A CN 108203721A
- Authority
- CN
- China
- Prior art keywords
- corn
- liquid
- zymomonas mobilis
- fermentation
- trichoderma reesei
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P7/00—Preparation of oxygen-containing organic compounds
- C12P7/02—Preparation of oxygen-containing organic compounds containing a hydroxy group
- C12P7/04—Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
- C12P7/06—Ethanol, i.e. non-beverage
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
- C12N9/14—Hydrolases (3)
- C12N9/24—Hydrolases (3) acting on glycosyl compounds (3.2)
- C12N9/2402—Hydrolases (3) acting on glycosyl compounds (3.2) hydrolysing O- and S- glycosyl compounds (3.2.1)
- C12N9/2405—Glucanases
- C12N9/2434—Glucanases acting on beta-1,4-glucosidic bonds
- C12N9/2437—Cellulases (3.2.1.4; 3.2.1.74; 3.2.1.91; 3.2.1.150)
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P19/00—Preparation of compounds containing saccharide radicals
- C12P19/14—Preparation of compounds containing saccharide radicals produced by the action of a carbohydrase (EC 3.2.x), e.g. by alpha-amylase, e.g. by cellulase, hemicellulase
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12Y—ENZYMES
- C12Y302/00—Hydrolases acting on glycosyl compounds, i.e. glycosylases (3.2)
- C12Y302/01—Glycosidases, i.e. enzymes hydrolysing O- and S-glycosyl compounds (3.2.1)
- C12Y302/01004—Cellulase (3.2.1.4), i.e. endo-1,4-beta-glucanase
-
- 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
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Zoology (AREA)
- Wood Science & Technology (AREA)
- Health & Medical Sciences (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Genetics & Genomics (AREA)
- General Health & Medical Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Biochemistry (AREA)
- Biotechnology (AREA)
- Microbiology (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Molecular Biology (AREA)
- Biomedical Technology (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Enzymes And Modification Thereof (AREA)
Abstract
本发明公开了一种运动发酵单胞菌利用玉米产乙醇的方法,属于微生物发酵技术领域。本发明方法包括如下步骤:(1)将玉米在脱胚机的击打下使玉米胚脱出得到玉米糁,玉米糁通过粉碎机粉碎得玉米粉,加水搅拌得到玉米浆;(2)玉米浆加水混匀后蒸煮液化,再加入糖化酶进行糖化得到玉米浆糖化液;(3)里氏木霉发酵液和黑曲霉菌发酵液按照体积比为1:1的条件进行混合离心,取上清液进行第二次离心,取上清液即得纤维素酶粗酶液;(4)往纤维素酶粗酶液中加入玉米浆糖化液,45‑55℃酶解3‑5天后接种运动发酵单胞菌,30‑35℃厌氧、静置发酵2‑3天。通过本发明方法运动发酵单胞菌利用玉米转化为乙醇的转化率为35%。The invention discloses a method for producing ethanol by Zymomonas mobilis using corn, and belongs to the technical field of microbial fermentation. The method of the present invention comprises the following steps: (1) degerming the corn embryos under the beating of a degerminator to obtain corn grits, and crushing the corn grits through a pulverizer to obtain corn flour, adding water and stirring to obtain corn steep liquor; (2) adding water to the corn steep liquor and mixing Homogenize, cook and liquefy, then add glucoamylase for saccharification to obtain corn syrup saccharification liquid; (3) Trichoderma reesei fermentation liquid and Aspergillus niger fermentation liquid are mixed and centrifuged according to the volume ratio of 1:1, and the supernatant is taken for Centrifuge for the second time, and take the supernatant to obtain the crude cellulase enzyme liquid; (4) Add corn syrup saccharification liquid to the crude cellulase enzyme liquid, enzymatically hydrolyze at 45-55°C for 3-5 days, and then inoculate motile zymounit cells Bacteria, anaerobic fermentation at 30-35°C for 2-3 days. The conversion rate of converting Zymomonas mobilis into ethanol by corn is 35% through the method of the present invention.
Description
技术领域technical field
本发明属于微生物发酵技术领域,具体涉及一种运动发酵单胞菌利用玉米产乙醇的方法。The invention belongs to the technical field of microbial fermentation, and in particular relates to a method for producing ethanol by Zymomonas mobilis using corn.
背景技术Background technique
运动发酵单胞菌(Z. mobilis)是一种革兰氏阴性菌,是发酵单胞菌属的一个种,因具有很强的运动性而得名。大多呈直杆状,尾端呈圆形或卵圆形,常成对存在,但很少集结成短链状。兼性厌氧条件生长,在无氧条件下生长最佳,有氧条件下也可生存,高度耐酸,能在pH3.5~7.5之间生长。运动发酵单胞菌利用Entner-Doudomff 途径代谢生产乙醇,这种途径耗能较少,产量较高。运动发酵单胞菌作为乙醇生产菌株具有一定优良的特性:如较高的乙醇产率,较强的乙醇耐受性,以及高度发酵底物专一性。与酵母相比,运动发酵单胞菌乙醇产量比酵母要高5%~10%,可达理论值的97%,乙醇转化率是酵母的5倍。但是,运动发酵单胞菌也有自身的局限性,底物利用范围较窄,只能利用葡萄糖、果糖和蔗糖。近来已有人利用基因工程的方法对其不利因素进行了改造,使其能够利用多种底物。Zymomonas mobilis ( Z. mobilis ) is a Gram-negative bacterium, a species of Zymomonas, named for its strong motility. Most of them are straight rods with round or oval tails, often in pairs, but rarely assembled into short chains. It grows under facultative anaerobic conditions, grows best under anaerobic conditions, and can survive under aerobic conditions. It is highly acid-resistant and can grow between pH 3.5 and 7.5. Zymomonas mobilis uses the Entner-Doudomff pathway to metabolize ethanol, which requires less energy and produces higher yields. As an ethanol producing strain, Zymomonas mobilis has certain excellent characteristics: such as high ethanol yield, strong ethanol tolerance, and high specificity of fermentation substrate. Compared with yeast, the ethanol yield of Zymomonas mobilis is 5% to 10% higher than that of yeast, which can reach 97% of the theoretical value, and the ethanol conversion rate is 5 times that of yeast. However, Zymomonas mobilis also has its own limitations, and its substrate utilization range is narrow, and it can only utilize glucose, fructose and sucrose. Recently, some people have used genetic engineering methods to modify its unfavorable factors, so that it can use a variety of substrates.
由于传统能源的可开采量不足、污染环境等弊端,燃料乙醇被认为最有可能代替化石燃料的能源。Due to the disadvantages of insufficient mining of traditional energy sources and environmental pollution, fuel ethanol is considered to be the most likely energy source to replace fossil fuels.
发明内容Contents of the invention
本发明的在于提供一种运动发酵单胞菌利用玉米浆产乙醇的方法,该方法以玉米浆为基质,将玉米加工成适合发酵的糖液后用运动发酵单胞菌发酵产生乙醇。The present invention provides a method for producing ethanol by Zymomonas mobilis using corn steep liquor. The method takes corn steep liquor as a substrate, processes corn into sugar solution suitable for fermentation, and then uses Zymomonas mobilis to ferment to produce ethanol.
本发明的目的通过下述技术方案实现:The object of the present invention is achieved through the following technical solutions:
一种运动发酵单胞菌利用玉米浆产乙醇的方法,包括如下步骤:A method for producing ethanol by Zymomonas mobilis using corn steep liquor, comprising the steps of:
(1)玉米的脱胚、粉碎和调浆:将玉米在脱胚机的击打下使玉米胚脱出得到玉米糁,玉米糁通过粉碎机粉碎得玉米粉,加水搅拌得到玉米浆。(1) Degerming, crushing and pulping of corn: The corn is beaten by the degerminator to remove the corn germ to obtain corn grits, and the corn grits are crushed by a grinder to obtain corn flour, which is then stirred with water to obtain corn steep liquor.
(2)玉米浆的液化和糖化:将玉米浆与水按质量比1:3.5-4混合均匀,加热至100±5℃蒸煮至液化完成得到液化液。液化液降温至55℃-65℃时加入糖化酶,并加盐酸调pH至4.1-4.3,进行糖化得到玉米浆糖化液。所述的水优选为45℃-55℃的水。(2) Liquefaction and saccharification of corn steep liquor: Mix corn steep liquor and water evenly at a mass ratio of 1:3.5-4, heat to 100±5°C and cook until liquefaction is complete to obtain liquefied liquid. Add glucoamylase when the temperature of the liquefied solution is lowered to 55°C-65°C, and add hydrochloric acid to adjust the pH to 4.1-4.3 for saccharification to obtain corn syrup saccharified liquid. The water is preferably water at 45°C-55°C.
(3)纤维素酶粗酶液的制备:里氏木霉发酵液和黑曲霉菌发酵液按照体积比为1:1的条件进行混合,将两者的混合液离心,取上清液进行第二次离心,第二次离心的上清液即为纤维素酶粗酶液。(3) Preparation of crude cellulase enzyme liquid: Trichoderma reesei fermentation liquid and Aspergillus niger fermentation liquid were mixed according to the volume ratio of 1:1, the mixture of the two was centrifuged, and the supernatant was taken for the second The second centrifugation, the supernatant of the second centrifugation is the cellulase crude enzyme liquid.
(4)酶解玉米淀粉:往步骤(3)得到的纤维素酶粗酶液中加入步骤(2)得到的玉米浆糖化液,45-55℃酶解3-5天后接种运动发酵单胞菌,30-35℃厌氧、静置发酵2-3天。(4) Enzymatic hydrolysis of corn starch: Add the corn syrup saccharification solution obtained in step (2) to the crude cellulase solution obtained in step (3), and inoculate Zymomonas mobilis after enzymatic hydrolysis at 45-55°C for 3-5 days , 30-35 ℃ anaerobic, static fermentation for 2-3 days.
步骤(1)优选为:将玉米在脱胚机的击打下使玉米胚脱出得到玉米糁,玉米糁通过粉碎机粉碎成200目细微粉末。按照50g玉米粉加20g水的比例加到拌料罐,加热至63-68℃搅拌得到玉米浆。Step (1) is preferably: the corn is beaten by a degerminator to remove the corn germ to obtain corn grits, and the corn grits are crushed into 200-mesh fine powder by a pulverizer. Add 50g of corn flour to 20g of water into a mixing tank, heat to 63-68°C and stir to obtain corn steep liquor.
步骤(2)中所述的糖化酶的终浓度(在体系中的浓度)优选为1μg/L,糖化的时间优选为20分钟。The final concentration (concentration in the system) of the saccharification enzyme described in step (2) is preferably 1 μg/L, and the saccharification time is preferably 20 minutes.
步骤(3)中所述的里氏木霉菌和黑曲霉菌培养、活化和发酵的操作方法一样,里氏木霉发酵液或黑曲霉菌发酵液优选通过包括如下步骤的方法制备得到:The Trichoderma reesei and Aspergillus niger culture, activation and fermentation methods described in step (3) are the same, and the Trichoderma reesei fermentation liquid or Aspergillus niger fermentation liquid is preferably prepared by a method comprising the following steps:
1)将里氏木霉菌或黑曲霉菌接种在PDA固体培养基中,在28℃恒温条件下密封培养3-5天后,用灭菌处理过的生理盐水将生成的孢子从培养基上洗涤下来,并用移液枪将成团状存在的孢子打碎,使之完全分散,并稀释至至107个/mL的浓度,得到里氏木霉孢子悬浮液或黑曲霉孢子悬浮液。1) Inoculate Trichoderma reesei or Aspergillus niger in PDA solid medium, culture in a sealed container at a constant temperature of 28°C for 3-5 days, then wash the generated spores from the medium with sterilized physiological saline , and use a pipette gun to break up the spores existing in agglomerates to completely disperse them, and dilute to a concentration of 107 /mL to obtain Trichoderma reesei spore suspension or Aspergillus niger spore suspension.
2)将里氏木霉孢子悬浮液或黑曲霉孢子悬浮液以10%(V/V)的接种量接种于种子培养基中,在摇床中28℃、150rpm培养48h后得到活化的里氏木霉菌液或活化的黑曲霉菌液。所述的种子培养基包含下述浓度的原料:玉米糁10g/L,吐温-80为5mL /L,Mandles 微量元素盐溶液1mL/L,Mandles营养盐浓溶液100mL/L,pH为4.8的浓度为1mol/L的柠檬酸缓冲液50mL/L。2) Inoculate the spore suspension of Trichoderma reesei or Aspergillus niger in the seed medium at an inoculation amount of 10% (V/V), and culture it in a shaker at 28°C and 150rpm for 48 hours to obtain activated Lisler Trichoderma liquid or activated Aspergillus niger liquid. Described seed culture medium comprises the raw material of following concentration: corn grits 10g/L, Tween-80 is 5mL/L, Mandles trace element salt solution 1mL/L, Mandles nutrient salt concentrated solution 100mL/L, pH is 4.8 Concentration of 1mol/L citrate buffer 50mL/L.
3)将上述活化的里氏木霉菌液或活化的黑曲霉菌液按10%的接种量接种到发酵培养基中28℃、150rpm培养7d得到里氏木霉发酵液或黑曲霉菌发酵液。所述的发酵培养基包含下述浓度的原料:玉米糁30g/L,吐温-80为5mL/L,Mandles微量元素盐溶液1mL/L,Mandles营养盐浓溶液100mL/L,pH为4.8的浓度为1mol/L的柠檬酸缓冲液50mL/L。3) Inoculate the above-mentioned activated Trichoderma reesei liquid or activated Aspergillus niger liquid into the fermentation medium at 10% inoculum amount and culture at 28° C. and 150 rpm for 7 days to obtain Trichoderma reesei fermentation liquid or Aspergillus niger fermentation liquid. The fermentation medium contains raw materials of the following concentrations: corn grits 30g/L, Tween-80 5mL/L, Mandles trace element salt solution 1mL/L, Mandles nutrient salt concentrated solution 100mL/L, pH 4.8 Concentration of 1mol/L citrate buffer 50mL/L.
步骤(3)中所述的离心的条件优选为4℃、8000rpm离心10min。The centrifugation conditions described in step (3) are preferably 4° C., 8000 rpm for 10 min.
步骤(4)中所述的运动发酵单胞菌优选为活化后的菌液,优选通过包括如下步骤的方法制备得到:用ZM种子培养基活化运动发酵单胞菌,按10%(v/v)的接种量接入ZM种子培养基,置于32℃的恒温摇床中,静置培养10h。取生长10h后的种子液按10%的接种量接种ZM种子培养基中,置于32℃的恒温摇床中,二次静置活化,当菌液OD600达到10左右时,即得到最终活化的菌液,用于接种到上述粗酶液酶解的玉米浆糖化液中。The Zymomonas mobilis described in step (4) is preferably an activated bacterial liquid, preferably prepared by a method comprising the following steps: activating Zymomonas mobilis with ZM seed culture medium, at 10% (v/v ) into the ZM seed medium, placed in a constant temperature shaker at 32°C, and cultured statically for 10 hours. Take the seed solution grown for 10 hours and inoculate it into the ZM seed medium at an inoculation amount of 10%, place it in a constant temperature shaker at 32°C, and let it stand for the second time to activate. When the OD 600 of the bacterial solution reaches about 10, the final activation will be obtained. The bacterium solution is used to inoculate into the corn syrup saccharification solution enzymatically hydrolyzed by the above crude enzyme solution.
步骤(4)中粗酶液与玉米浆糖化液之间量的关系优选为:每12mL粗酶液添加1g玉米粉按步骤(1)、(2)得到的玉米浆糖化液。The relationship between the amount of the crude enzyme solution and the corn syrup saccharification solution in step (4) is preferably: add 1 g of corn flour to every 12 mL of crude enzyme solution and obtain the corn syrup saccharification solution in steps (1) and (2).
步骤(4)优选为:按每12mL粗酶液添加1g玉米粉按步骤(1)、(2)得到的玉米浆糖化液的比例将玉米浆糖化液加入到粗酶液中,50℃酶解4天后接种运动发酵单胞菌,在32℃摇床中厌氧、静置发酵60h。Step (4) is preferably: add 1g of corn flour per 12mL of crude enzyme solution, add corn syrup saccharification solution to the crude enzyme solution in proportion to the corn syrup saccharification solution obtained in steps (1) and (2), and enzymatically hydrolyze at 50°C After 4 days, Zymomonas mobilis was inoculated, anaerobically and statically fermented in a shaker at 32° C. for 60 h.
本发明的作用机理为:运动发酵单胞菌作为乙醇生产菌株具有一定优良的特性,如较高的乙醇产率,较强的乙醇耐受性。但是,运动发酵单胞菌也有自身的局限性,底物利用范围较窄,不能直接作用于淀粉。本发明中利用黑曲霉和木酶水解混合发酵玉米糁产生纤维素酶粗酶液,并对玉米浆进行酶解产生还原糖。通过将传统的黑曲霉和木霉混合发酵产纤维素酶改进为分别发酵再对粗酶液进行混合,有效地改善了因五碳糖的积累而产生的产物反馈抑制现象,提高淀粉糖化的效率。再将运动发酵单胞菌作用于还原糖,产生乙醇,进而提高运动发酵单胞菌利用玉米浆产乙醇的效率。解决了运动发酵单胞菌利用底物单一狭窄的问题。The action mechanism of the present invention is as follows: Zymomonas mobilis has certain excellent characteristics as an ethanol production strain, such as higher ethanol yield and stronger ethanol tolerance. However, Zymomonas mobilis also has its own limitations, the substrate utilization range is narrow, and it cannot directly act on starch. In the invention, aspergillus niger and wood enzyme are used to hydrolyze mixed fermented corn grits to produce crude cellulase enzyme liquid, and enzymatically hydrolyze corn steep liquor to produce reducing sugar. By improving the traditional mixed fermentation of Aspergillus niger and Trichoderma to produce cellulase by separate fermentation and then mixing the crude enzyme solution, the product feedback inhibition phenomenon caused by the accumulation of five-carbon sugars is effectively improved, and the efficiency of starch saccharification is improved. . Then, the Zymomonas mobilis acts on the reducing sugar to produce ethanol, thereby improving the ethanol production efficiency of the Zymomonas mobilis using corn steep liquor. Solve the problem of single narrow substrate utilization by Zymomonas mobilis.
本发明的有益技术效果为:(1)本发明中将黑曲霉和木霉分别发酵得到的纤维素酶粗酶液按1:1混合,有效地控制了产物反馈抑制,从而得到活性和产量更高的纤维素酶粗酶液并可以针对淀粉糖化作用。(2)将运动发酵单胞菌接种于酶解后的含还原糖的发酵液中,大大提高了运动发酵单胞菌利用玉米浆产无水乙醇的效率,解决了运动发酵单胞菌底物利用范围狭窄,不能有效利用玉米淀粉的弊端,通过本发明中的方法运动发酵单胞菌利用玉米转化为乙醇的转化率为35%,即100g玉米产生35g的乙醇。The beneficial technical effects of the present invention are: (1) In the present invention, the crude cellulase enzyme liquids fermented by Aspergillus niger and Trichoderma respectively are mixed at 1:1, which effectively controls the feedback inhibition of the product, thereby obtaining higher activity and yield. High cellulase crude enzyme solution and can target starch saccharification. (2) Inoculating Zymomonas mobilis in the fermentation broth containing reducing sugar after enzymolysis greatly improved the efficiency of Zymomonas mobilis in producing absolute ethanol from corn steep liquor, and solved the problem of Zymomonas mobilis substrates The utilization scope is narrow, and the drawback of cornstarch can not be effectively utilized. By the method of the present invention, Zymomonas mobilis converts corn into ethanol with a conversion rate of 35%, that is, 100g of corn produces 35g of ethanol.
具体实施方式Detailed ways
以下实施例用于进一步说明本发明的内容,但不应理解为对本发明的限制,在不背离本发明精神和实质的情况下,对本发明方法、步骤或条件所作的修改或替换均属于本发明的范围。若未特别指明,实施例中所用的技术手段为本领域技术人员所熟知的常规手段。The following examples are used to further illustrate the content of the present invention, but should not be interpreted as limiting the present invention, without departing from the spirit and essence of the present invention, the modifications or replacements made to the methods, steps or conditions of the present invention all belong to the present invention range. Unless otherwise specified, the technical means used in the embodiments are conventional means well known to those skilled in the art.
实施例1Example 1
1、材料1. Materials
(1)菌种:里氏木霉(T. reesei)RUT C30,黑曲霉(Aspergillus niger),运动发酵单胞菌(Z. mobilis)。(1) Strains: Trichoderma reesei ( T. reesei ) RUT C30, Aspergillus niger ( Aspergillus niger ), Zymomonas mobilis ( Z. mobilis ).
(2)PDA固体培养基:PDA即马铃薯葡萄糖琼脂培养基,将马铃薯洗净去皮,称取马铃薯200g切成小块,加入烧杯中,加水蒸煮直到马铃薯能被玻璃杯轻轻戳破,蒸煮约30min。用纱布过滤,往滤液中添加葡萄糖20g、琼脂20g,定容至1L。115℃高压灭菌30min,倒固体平板。(2) PDA solid medium: PDA is potato dextrose agar medium. Wash and peel the potatoes, weigh 200g of potatoes and cut them into small pieces, add them to a beaker, add water and cook until the potatoes can be gently pierced by a glass, and cook About 30min. Filter with gauze, add 20g of glucose and 20g of agar to the filtrate, and dilute to 1L. Autoclave at 115°C for 30 minutes, pour solid plate.
(3)种子培养基:玉米糁10g/L,吐温-80为5mL /L,Mandles 微量元素盐溶液1mL/L,Mandles营养盐浓溶液100mL/L,pH为4.8的浓度为1mol/L的柠檬酸缓冲液50mL/L。115℃高压灭菌30min,备用。(3) Seed medium: corn grits 10g/L, Tween-80 5mL/L, Mandles trace element salt solution 1mL/L, Mandles nutrient salt concentrated solution 100mL/L, pH 4.8 concentration 1mol/L Citric acid buffer 50mL/L. Autoclave at 115°C for 30 minutes and set aside.
(4)发酵培养基:玉米糁30g/L,吐温-80为5mL /L,Mandles微量元素盐溶液1mL/L,Mandles营养盐浓溶液100mL/L,pH为4.8的浓度为1mol/L的柠檬酸缓冲液50mL/L。115℃高压灭菌30min,备用。(4) Fermentation medium: corn grits 30g/L, Tween-80 5mL/L, Mandles trace element salt solution 1mL/L, Mandles nutrient salt concentrated solution 100mL/L, pH 4.8 concentration 1mol/L Citric acid buffer 50mL/L. Autoclave at 115°C for 30 minutes and set aside.
(5)ZM种子培养基:葡萄糖100g/L,尿素0.05g/L,酵母提取物1g/L,磷酸二氢钾0.05g/L,硫酸镁0.05g/L,加去离子水定容至1000mL,用HCL调节pH为6.0,在115℃灭菌30min。(5) ZM seed medium: glucose 100g/L, urea 0.05g/L, yeast extract 1g/L, potassium dihydrogen phosphate 0.05g/L, magnesium sulfate 0.05g/L, add deionized water to 1000mL , adjusted the pH to 6.0 with HCL, and sterilized at 115°C for 30min.
(6)不含葡萄糖的ZM种子培养基:除不含葡萄糖外,其余成分及含量与ZM种子培养基相同。(6) ZM seed medium without glucose: Except for glucose, the other components and contents are the same as ZM seed medium.
2、具体步骤2. Specific steps
(1)玉米的脱胚、粉碎和调浆:将玉米在脱胚机的击打下使玉米胚脱出得到玉米糁,玉米糁通过粉碎机粉碎成200目细微粉末,一般粉碎粒度≥88%。按照50g玉米粉加20g水的比例加到拌料罐,加热至63-68℃搅拌得到玉米浆,pH值5.8-6.0。(1) Degerming, crushing and pulping of corn: The corn germs are degerminated by the degerming machine to obtain corn grits, and the corn grits are crushed into 200-mesh fine powder by a pulverizer, and the crushing particle size is generally ≥88%. Add 50g of corn flour to 20g of water into the mixing tank, heat to 63-68°C and stir to obtain corn steep liquor with a pH value of 5.8-6.0.
(2)玉米浆液化和糖化:将玉米浆与45℃-55℃的水按质量比1:3.5-4混合均匀,pH值为6.5-7.0,加热至100±5℃蒸煮100分钟左右,碘液试验为粉红色表明液化完成得到液化液。液化液降温至60℃左右时,加入糖化酶(终浓度1μg/L),并加盐酸调pH至4.1-4.3,糖化时间控制在20分钟,得到玉米浆糖化液。(2) Corn syrup liquefaction and saccharification: Mix corn steep liquor with water at 45°C-55°C in a mass ratio of 1:3.5-4, the pH value is 6.5-7.0, heat to 100±5°C and cook for about 100 minutes, iodine The liquid test is pink, indicating that the liquefaction is completed and the liquefied liquid is obtained. When the temperature of the liquefied solution is lowered to about 60°C, add glucoamylase (final concentration 1 μg/L), and add hydrochloric acid to adjust the pH to 4.1-4.3, and the saccharification time is controlled at 20 minutes to obtain corn syrup saccharification solution.
(3)纤维素酶粗酶液的制备:(3) Preparation of cellulase crude enzyme solution:
1)分别用接种环挑取少量保存的里氏木霉、黑曲霉的孢子,在不同PDA固体平板划线,封口膜密封,在28℃恒温箱中培养3-5天。1) Pick a small amount of preserved spores of Trichoderma reesei and Aspergillus niger with an inoculation loop, streak on different PDA solid plates, seal with a parafilm, and culture in a 28°C incubator for 3-5 days.
2)在恒温箱中培养3-5天后,里氏木霉和黑曲霉会产生一层孢子,用灭菌处理过的生理盐水将孢子从固体平板上洗涤下来,用移液枪将成团状存在的孢子打碎,使之完全分散,并稀释至107个/mL的浓度,分别得到里氏木霉孢子悬浮液和黑曲霉孢子悬浮液。2) After 3-5 days of cultivation in the incubator, Trichoderma reesei and Aspergillus niger will produce a layer of spores, wash the spores from the solid plate with sterilized saline, and use a pipette gun to form clumps The spores were crushed, dispersed completely, and diluted to a concentration of 107 /mL to obtain Trichoderma reesei spore suspensions and Aspergillus niger spore suspensions, respectively.
3)分别将上述里氏木霉孢子悬浮液和黑曲霉孢子悬浮液作为菌种,按10%(V/V)的接种量接种于不同的种子培养基,在摇床中28℃、150rpm培养48h,得到活化的里氏木霉菌液和活化的黑曲霉菌液。3) The above-mentioned Trichoderma reesei spore suspension and Aspergillus niger spore suspension were respectively used as strains, inoculated into different seed media at an inoculation amount of 10% (V/V), and cultured in a shaker at 28°C and 150rpm After 48 hours, the activated Trichoderma reesei liquid and the activated Aspergillus niger liquid were obtained.
4)将上述活化的里氏木霉菌液和活化的黑曲霉菌液分别按10%的接种量接种到装有50mL不同的发酵培养基的250mL摇瓶中,28℃、150rpm培养7d,得到里氏木霉发酵液或黑曲霉菌发酵液。4) Inoculate the above-mentioned activated Trichoderma reesei liquid and the activated Aspergillus niger liquid into 250 mL shake flasks containing 50 mL of different fermentation media according to the inoculum amount of 10%, and cultivate them at 28°C and 150 rpm for 7 days to obtain Li Trichoderma fermented liquid or Aspergillus niger fermented liquid.
5)将里氏木霉发酵液和黑曲霉菌发酵液按照体积比为1:1的比例进行混合,将两者的混合液于4℃、8000rpm离心10min;取其上清液并将其转移到另一离心管中在相同条件下进行第二次离心(离心条件同上),取上清液,即得纤维素酶粗酶液。5) Mix Trichoderma reesei fermentation broth and Aspergillus niger fermentation broth at a volume ratio of 1:1, centrifuge the mixture at 4°C and 8000rpm for 10min; take the supernatant and transfer it Centrifuge for the second time under the same conditions in another centrifuge tube (the centrifugation conditions are the same as above), and take the supernatant to obtain the crude cellulase enzyme solution.
(4)运动发酵单胞菌的准备:(4) Preparation of Zymomonas mobilis:
用ZM种子培养基活化运动发酵单胞菌,按10%(v/v)的接种量接入ZM种子培养基,置于32℃的恒温摇床中,静置培养10h。取生长10h后的种子液1.4mL按10%的接种量(v/v)接种到ZM种子培养基,置于32℃的恒温摇床中,二次静置培养,期间测量菌液OD600。当OD600达到10左右时,即为活化的运动发酵单胞菌,可作为菌种用于产乙醇。Zymomonas mobilis was activated with ZM seed culture medium, inoculated into ZM seed culture medium at an inoculation amount of 10% (v/v), placed in a constant temperature shaker at 32°C, and cultured statically for 10 h. Take 1.4 mL of the seed solution grown for 10 hours and inoculate it into the ZM seed medium at a 10% inoculation volume (v/v), place it in a constant temperature shaker at 32°C, and culture it for a second time, during which the OD 600 of the bacterial solution is measured. When the OD 600 reaches about 10, it is the activated Zymomonas mobilis, which can be used as a strain for ethanol production.
取活化的运动发酵单胞菌菌种1.4mL,采用离心、水洗的方式去除含有的葡萄糖以及乙醇,同时用1.4mL不含葡萄糖的ZM种子培养基将离心、水洗后的菌种悬起并混匀得运动发酵单胞菌悬液。Take 1.4 mL of activated Zymomonas mobilis strains, remove the glucose and ethanol contained in them by centrifugation and water washing, and at the same time use 1.4 mL of glucose-free ZM seed medium to suspend and mix the strains Homogenize Zymomonas mobilis suspension.
(5)酶解玉米浆:步骤(3)得到的纤维素酶粗酶液与玉米粉按体积质量比(mL/g)12:1的比例将步骤(2)得到的玉米浆糖化液加入到50mL粗酶液中,即每12mL粗酶液添加1g玉米粉按步骤(1)、(2)得到的玉米浆糖化液。在50℃的条件下,酶解4天后接种运动发酵单胞菌悬液1.4mL在32℃摇床中厌氧、静置发酵,发酵时间60h。发酵结束后,用气相色谱测发酵液中乙醇含量为35g/L。玉米转化为乙醇的转化率为35%,即100g玉米产生35g的乙醇。(5) Enzymatic hydrolysis of corn steep liquor: add the corn syrup saccharification liquid obtained in step (2) to the Into 50mL of crude enzyme solution, that is, every 12mL of crude enzyme solution, add 1g of corn flour saccharification solution obtained by steps (1) and (2). Under the condition of 50°C, after 4 days of enzymatic hydrolysis, 1.4 mL of Zymomonas mobilis suspension was inoculated and fermented anaerobically and statically in a shaker at 32°C for 60 hours. After the fermentation finished, the ethanol content in the fermented liquid measured by gas chromatography was 35g/L. The conversion rate of corn into ethanol is 35%, that is, 100g of corn produces 35g of ethanol.
Claims (8)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201611168633.9A CN108203721A (en) | 2016-12-16 | 2016-12-16 | A kind of method that zymomonas mobilis utilizes corn producing and ethanol |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201611168633.9A CN108203721A (en) | 2016-12-16 | 2016-12-16 | A kind of method that zymomonas mobilis utilizes corn producing and ethanol |
Publications (1)
Publication Number | Publication Date |
---|---|
CN108203721A true CN108203721A (en) | 2018-06-26 |
Family
ID=62602446
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201611168633.9A Pending CN108203721A (en) | 2016-12-16 | 2016-12-16 | A kind of method that zymomonas mobilis utilizes corn producing and ethanol |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN108203721A (en) |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63251056A (en) * | 1987-04-07 | 1988-10-18 | Nakano Vinegar Co Ltd | Preparation of paste food |
US20090117635A1 (en) * | 2007-11-05 | 2009-05-07 | Energy Enzymes, Inc. | Process for Integrating Cellulose and Starch Feedstocks in Ethanol Production |
CN105368882A (en) * | 2015-12-22 | 2016-03-02 | 湖北工业大学 | Method for producing ethyl alcohol through crop stalks by use of recombinant zymomonas mobilis |
CN105755057A (en) * | 2014-12-17 | 2016-07-13 | 中粮生化能源(肇东)有限公司 | Method for fermentative production of alcohol |
EP3268484B1 (en) * | 2015-03-12 | 2020-06-17 | Novozymes A/S | Multi-stage enzymatic hydrolysis of lignocellulosic biomass |
-
2016
- 2016-12-16 CN CN201611168633.9A patent/CN108203721A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63251056A (en) * | 1987-04-07 | 1988-10-18 | Nakano Vinegar Co Ltd | Preparation of paste food |
US20090117635A1 (en) * | 2007-11-05 | 2009-05-07 | Energy Enzymes, Inc. | Process for Integrating Cellulose and Starch Feedstocks in Ethanol Production |
WO2009061746A2 (en) * | 2007-11-05 | 2009-05-14 | Energy Enzymes, Inc. | Process for integrating cellulose and starch feedstocks in ethanol production |
CN105755057A (en) * | 2014-12-17 | 2016-07-13 | 中粮生化能源(肇东)有限公司 | Method for fermentative production of alcohol |
EP3268484B1 (en) * | 2015-03-12 | 2020-06-17 | Novozymes A/S | Multi-stage enzymatic hydrolysis of lignocellulosic biomass |
CN105368882A (en) * | 2015-12-22 | 2016-03-02 | 湖北工业大学 | Method for producing ethyl alcohol through crop stalks by use of recombinant zymomonas mobilis |
Non-Patent Citations (8)
Title |
---|
ALI MOHAGHEGHI等: "Performance of a newly developed integrant of Zymomonas mobilis for ethanol production on corn stover hydrolysate", 《BIOTECHNOLOGY LETTERS》 * |
SHIHUI YANG等: "Zymomonas mobilis as a model system for production of biofuels and biochemicals", 《MICROBIAL BIOTECHNOLOGY》 * |
刘桂林: "《生物技术概论》", 30 September 2010, 中国农业大学出版社 * |
刘艳等: "运动发酵单孢菌发酵生产乙醇研究进展", 《酿酒科技》 * |
李大鹏等: "双酶法生产玉米酒精液化及糖化工艺条件的研究", 《粮食与饲料工业》 * |
焦云鹏: "《酶制剂生产与应用》", 31 August 2015, 中国轻工业出版社 * |
石贵阳等: "玉米原料细菌酒精发酵的研究", 《无锡轻工大学学报》 * |
谢林等: "《玉米酒精生产新技术》", 31 January 2000, 中国轻工业出版社 * |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105368882A (en) | Method for producing ethyl alcohol through crop stalks by use of recombinant zymomonas mobilis | |
CN104140907B (en) | A kind of tea wine preparation technology | |
CN101100660B (en) | Method for producing cellulase through mixed fermentation of microorganisms | |
CN103436569B (en) | A kind of cassava wastes prepares the method for sugar and ethanol | |
CN104805136B (en) | A method of citric acid is produced using lignocellulosic material | |
CN101831416B (en) | Pullulanase and production method thereof | |
CN103421851B (en) | A kind of method preparing sugar and ethanol with sweet potato waste | |
CN102071224B (en) | Method for producing sorbitol and gluconate | |
CN104673675B (en) | A kind of green micro-ecological compound fertilizer and preparation method thereof | |
CN103013961A (en) | Method for producing neutral protease and feed additive by using fermentation of manioc wastes | |
CN101878308B (en) | A process for the preparation of ethanol from starch | |
CN103789360B (en) | A kind of corn cob fiber element fermentation that utilizes is for the method for fumaric acid fermented liquid | |
CN103614448B (en) | Method for preparing bioethanol by taking sodium alginate or algae as active ingredients | |
CN102533570A (en) | Aspergillus niger, application of Aspergillus niger and method for preparing citric acid by fermentation | |
CN103614299B (en) | A kind of Mucor circiniferus, method for preparing viscosity-reducing enzyme and application thereof | |
CN117587083A (en) | A kind of fermentation method of xanthan gum | |
CN112159762B (en) | Fusarium oxysporum SWH-3 and method for producing diosgenin by fermentation of fusarium oxysporum SWH-3 | |
CN104480086B (en) | A kind of preparation method of middle temperature alpha amylase | |
CN108203721A (en) | A kind of method that zymomonas mobilis utilizes corn producing and ethanol | |
CN103343151A (en) | Preparation method of liquid medium for bacterial cellulose film | |
CN103805578A (en) | Beta-dextranase with good heat stability | |
CN103820419B (en) | A kind of preparation method of the good beta glucan enzyme of heat endurance | |
CN102250857A (en) | Liquid fermentation technology capable to improve per unit of cellulose activity | |
CN115029264A (en) | A strain of acid-resistant Clostridium thermocellum and a method for degrading lignocellulose | |
CN103865908B (en) | Preparation method of neutral protease with strong thermal stability |
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 | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20180626 |