CN101220379A - Method for producing ethyl alcohol by using sorgo stalk - Google Patents
Method for producing ethyl alcohol by using sorgo stalk Download PDFInfo
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- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 title claims abstract description 105
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 32
- 235000019441 ethanol Nutrition 0.000 title description 52
- 235000011684 Sorghum saccharatum Nutrition 0.000 claims abstract description 95
- 244000138286 Sorghum saccharatum Species 0.000 claims abstract description 93
- 235000000346 sugar Nutrition 0.000 claims abstract description 51
- 235000011389 fruit/vegetable juice Nutrition 0.000 claims abstract description 36
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims abstract description 32
- 238000000034 method Methods 0.000 claims abstract description 22
- 239000002253 acid Substances 0.000 claims abstract description 20
- 238000000855 fermentation Methods 0.000 claims abstract description 17
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- 108010059892 Cellulase Proteins 0.000 claims abstract description 15
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- 235000014680 Saccharomyces cerevisiae Nutrition 0.000 claims description 29
- 239000002002 slurry Substances 0.000 claims description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 230000001476 alcoholic effect Effects 0.000 claims description 9
- 230000004913 activation Effects 0.000 claims description 8
- 239000002609 medium Substances 0.000 claims description 8
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- 238000003756 stirring Methods 0.000 claims description 8
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- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Chemical compound OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims description 6
- 230000002255 enzymatic effect Effects 0.000 claims description 6
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 5
- 239000004202 carbamide Substances 0.000 claims description 5
- 239000001888 Peptone Substances 0.000 claims description 4
- 108010080698 Peptones Proteins 0.000 claims description 4
- 238000004821 distillation Methods 0.000 claims description 4
- 238000001914 filtration Methods 0.000 claims description 4
- 239000008103 glucose Substances 0.000 claims description 4
- 239000002054 inoculum Substances 0.000 claims description 4
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- 238000011218 seed culture Methods 0.000 claims description 3
- 108090000790 Enzymes Proteins 0.000 claims description 2
- 102000004190 Enzymes Human genes 0.000 claims description 2
- 229940088598 enzyme Drugs 0.000 claims description 2
- 238000002203 pretreatment Methods 0.000 claims 5
- 239000006188 syrup Substances 0.000 claims 3
- 235000020357 syrup Nutrition 0.000 claims 3
- 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 claims 2
- 238000009835 boiling Methods 0.000 claims 2
- AIUDWMLXCFRVDR-UHFFFAOYSA-N dimethyl 2-(3-ethyl-3-methylpentyl)propanedioate Chemical class CCC(C)(CC)CCC(C(=O)OC)C(=O)OC AIUDWMLXCFRVDR-UHFFFAOYSA-N 0.000 claims 2
- 229940066779 peptones Drugs 0.000 claims 2
- 239000012492 regenerant Substances 0.000 claims 2
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- 238000004062 sedimentation Methods 0.000 claims 1
- 230000001954 sterilising effect Effects 0.000 claims 1
- 238000004659 sterilization and disinfection Methods 0.000 claims 1
- -1 β-glucose glycoside Chemical class 0.000 claims 1
- 239000000446 fuel Substances 0.000 abstract description 9
- 239000001913 cellulose Substances 0.000 abstract description 7
- 229920002678 cellulose Polymers 0.000 abstract description 7
- 240000006394 Sorghum bicolor Species 0.000 abstract description 2
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- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 2
- 108010089356 Novozym 188 Proteins 0.000 description 2
- 229940041514 candida albicans extract Drugs 0.000 description 2
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- 239000000706 filtrate Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000012138 yeast extract Substances 0.000 description 2
- 235000021558 10% juice Nutrition 0.000 description 1
- 241000282836 Camelus dromedarius Species 0.000 description 1
- 241000209140 Triticum Species 0.000 description 1
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- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
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- 229910021529 ammonia Inorganic materials 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
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- 238000006243 chemical reaction Methods 0.000 description 1
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- 238000003306 harvesting Methods 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- 125000004029 hydroxymethyl group Chemical group [H]OC([H])([H])* 0.000 description 1
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Classifications
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- 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
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- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Abstract
Description
技术领域technical field
本发明属于生物燃料的生产方法,具体地说涉及一种利用甜高粱茎秆生产乙醇的方法。The invention belongs to a biofuel production method, in particular to a method for producing ethanol by using sweet sorghum stalks.
背景技术Background technique
石油、天然气、煤炭的过量开采和使用,使世界面临严重的能源危机和环境危机,寻找替代的可持续的环保的绿色能源,成为世界能源战略的重点。而生物燃料乙醇是一种可行的替代途径,目前中国主要以陈化粮为原料生产燃料乙醇,不但与人争粮争地,难以广泛解决交通能源问题,而且从能源利用的整个生命周期来看,粮食乙醇的CO2释放量并没有降低,不能达到环保目的,同时利用粮食生产燃料乙醇,不但成本高,还造成粮食的浪费。因此需要寻找新的生产生物燃料的植物原料,甜高粱茎秆富含糖分和纤维,是一种比较理想的生产燃料乙醇的原料。Excessive exploitation and use of oil, natural gas, and coal have caused the world to face serious energy and environmental crises. Finding alternative, sustainable, environmentally friendly green energy has become the focus of the world's energy strategy. Biofuel ethanol is a feasible alternative. At present, China mainly produces fuel ethanol with aged grains as raw materials. , the CO 2 release of grain ethanol has not been reduced, and the purpose of environmental protection cannot be achieved. At the same time, the use of grain to produce fuel ethanol not only costs high, but also causes waste of grain. Therefore, it is necessary to find new plant raw materials for the production of biofuels. Sweet sorghum stalks are rich in sugar and fiber, and are an ideal raw material for the production of fuel ethanol.
与其他能够生产酒精的能源作物相比,甜高粱具有不可比拟的优势:第一,在生物量能源系统中,甜高粱是第一位的竞争者,每公顷能收获2250~7500千克的籽粒,茎秆富含糖分,且产量极高,一般每公顷鲜秸秆的产量在75吨左右。第二,甜高粱是高能作物。生长旺盛时期,每公顷甜高粱每天合成的碳水化合物可产48升酒精,而玉米只有15升,小麦为3升,粒用高粱才9升。第三,甜高粱不仅产量高,而且其适应性很广,抗旱、耐涝、耐盐碱,是作物中的“骆驼”。甜高粱在pH值5~8.5的各种类型的土壤均可栽培,在含盐量达到0.36%~0.53%的盐碱土地上,甜高粱能正常生长,产量能达到4~5.5吨。因为我国的可耕地面积有限,所以盐碱土地,特别是海滨滩涂的盐碱性土壤,是发展燃料酒精产业最理想的区域,而甜高粱就是生产燃料酒精最适宜的原料作物之一。Compared with other energy crops that can produce alcohol, sweet sorghum has incomparable advantages: first, in the biomass energy system, sweet sorghum is the first competitor, and can harvest 2250-7500 kilograms of seeds per hectare, The stalks are rich in sugar, and the yield is extremely high. Generally, the yield of fresh stalks per hectare is about 75 tons. Second, sweet sorghum is a high-energy crop. During the vigorous growth period, the carbohydrates synthesized by sweet sorghum per hectare can produce 48 liters of alcohol per day, while that of corn is only 15 liters, that of wheat is 3 liters, and that of sorghum for grain is only 9 liters. Third, sweet sorghum not only has high yield, but also has wide adaptability, drought resistance, waterlogging tolerance, and salt-alkali tolerance. It is the "camel" among crops. Sweet sorghum can be cultivated in various types of soil with a pH value of 5-8.5. On saline-alkali soil with a salt content of 0.36%-0.53%, sweet sorghum can grow normally, and the output can reach 4-5.5 tons. Due to the limited area of arable land in our country, saline-alkali land, especially the saline-alkaline soil of coastal tidal flats, is the most ideal area for the development of fuel ethanol industry, and sweet sorghum is one of the most suitable raw material crops for the production of fuel ethanol.
目前,利用甜高粱茎秆生产燃料乙醇主要是利用甜高粱茎秆的汁液或者籽粒加汁液进行发酵生产,如专利申请《甜高粱茎秆汁液生产乙醇的方法》(申请号:200510076833.7)、《利用甜高粱茎秆制造乙醇液体发酵技术》(申请号为:200410035604.6)、《甜高粱茎秆生产乙醇工艺方法》(申请号为:02151719.3)、《一种燃料乙醇及其制取工艺》(申请号为:2007100022972.4)、《以甜茎玉米或甜高粱的干秸秆为原料制取乙醇的工艺》(申请号为:200610134397.9)等中主要利用甜高粱茎秆汁液生产乙醇,《利用甜高粱秸秆及其籽粒制取乙醇的方法》(申请号为:200710057584.6)、《用甜高粱秸秆制取乙醇的方法》(申请号为:200710010720.6)等利用甜高粱茎秆汁液和籽粒生产乙醇,这些发明利用茎秆汁液发酵仅仅利用了甜高粱茎秆中部分可溶性糖,而将甜高粱渣中与可溶性糖几乎等量的,以纤维素和半纤维素形式存在的结构糖弃去或燃烧,不但造成大量浪费,原料利用率低,而且造成了空气和环境污染。随着纤维素预处理技术的提高,美国生物质加工应用创新联合体(CAFI)在酸预处理,氨爆破预处理都取得了很大成果;国际先进酶制剂公司,如诺维信和杰能科将纤维素酶价格的降低;使充分利用甜高粱茎秆中的非结构糖和结构糖生产燃料乙醇成为可能,这将大大提高原料利用率和乙醇得率。At present, the production of fuel ethanol from sweet sorghum stalks is mainly carried out by fermenting the sap of sweet sorghum stalks or grains plus juice, such as the patent application "Method for Producing Ethanol from Sweet Sorghum Stalk Juice" (Application No.: 200510076833.7), "Using Sweet sorghum stalk production ethanol liquid fermentation technology" (application number: 200410035604.6), "sweet sorghum stalk production ethanol process method" (application number: 02151719.3), "a kind of fuel ethanol and its production process" (application number No.: 2007100022972.4), "Technology for Producing Ethanol Using Sweet Sorghum Stalk or Sweet Sorghum Dry Straw as Raw Material" (Application No.: 200610134397.9), etc., mainly utilize sweet sorghum stalk juice to produce ethanol, "Use Sweet Sorghum Straw and its The method for producing ethanol from grains" (application number: 200710057584.6), "method for producing ethanol with sweet sorghum stalks" (application number: 200710010720.6), etc. utilize sweet sorghum stalk juice and grains to produce ethanol, and these inventions use the stalk Juice fermentation only utilizes part of the soluble sugar in the sweet sorghum stalk, and discards or burns the structural sugar in the form of cellulose and hemicellulose that is almost equal to the soluble sugar in the sweet sorghum dregs, which not only causes a lot of waste, Raw material utilization rate is low, and has caused air and environmental pollution. With the improvement of cellulose pretreatment technology, the US Biomass Processing Application Innovation Consortium (CAFI) has achieved great results in acid pretreatment and ammonia blast pretreatment; international advanced enzyme preparation companies, such as Novozymes and Genen The reduction of the price of cellulase will make it possible to make full use of non-structural and structural sugars in sweet sorghum stalks to produce fuel ethanol, which will greatly increase the utilization rate of raw materials and the yield of ethanol.
发明内容Contents of the invention
本发明的目的是提供一种利用甜高粱茎秆生产乙醇的方法,此方法可充分利用甜高粱茎秆中的非结构糖和结构糖,原料利用率高,且乙醇得率高。The object of the present invention is to provide a method for producing ethanol by using sweet sorghum stalks, which can make full use of non-structural sugars and structural sugars in sweet sorghum stalks, has high raw material utilization rate and high ethanol yield.
为实现上述目的,本发明所采取的技术方案为:In order to achieve the above object, the technical scheme adopted in the present invention is:
利用甜高粱茎秆生产乙醇的方法,包括如下步骤:The method for producing ethanol from sweet sorghum stalks comprises the steps of:
(1)将成熟的甜高粱茎秆进行压榨,得茎秆汁液和甜高粱渣;(1) Squeezing mature sweet sorghum stalks to obtain stalk juice and sweet sorghum slag;
(2)对甜高粱渣进行稀酸爆破预处理;(2) Carry out dilute acid blasting pretreatment to sweet sorghum slag;
(3)用纤维素酶将甜高粱渣酶解糖化;(3) Enzymolysis and saccharification of sweet sorghum residue with cellulase;
(4)混合糖液并调节糖汁浓度;(4) mixing the sugar solution and adjusting the concentration of the sugar juice;
(5)酵母活化;(5) Yeast activation;
(6)发酵,即得乙醇。(6) fermentation to obtain ethanol.
上述生产乙醇的方法步骤(1)中所述的压榨是指将成熟的甜高粱茎秆粉碎切割成10mm~25mm的丝状小段,然后进行压榨,再向所得甜高粱渣中加10~20%的水进行二次压榨,得茎秆汁液和甜高粱渣;再将所得茎秆汁液在85~100℃蒸煮30~45min,然后离心、过滤,去沉淀,得澄清的茎秆汁液。The pressing described in step (1) of the method for producing ethanol refers to crushing and cutting the mature sweet sorghum stalks into filamentous segments of 10 mm to 25 mm, then pressing, and then adding 10 to 20% Squeeze the fresh water twice to obtain stalk juice and sweet sorghum slag; then cook the obtained stalk juice at 85-100°C for 30-45 minutes, then centrifuge, filter, and remove sediment to obtain clarified stalk juice.
上述生产乙醇的方法步骤(2)中所述的对甜高粱渣进行稀酸爆破预处理是指将上述所得甜高粱渣风干或者在30~45℃下烘干,然后将甜高粱渣在0.1~0.5%H2SO4溶液中浸泡8~12小时,再置于蒸汽爆破罐中,升压,在1.3~1.9MPa压力下保持6~10min,瞬间泄压,收集汽爆后所得的甜高粱渣;用水洗涤经酸爆破处理后的甜高粱渣,得预处理浆液和固体回收物,向所得浆液中加入Ca(OH)2调节pH值到9.5~10.5,搅拌1~1.5h,沉淀过滤,得澄清的预处理浆液。The dilute acid blasting pretreatment of the sweet sorghum slag described in step (2) of the above method for producing ethanol refers to air-drying the sweet sorghum slag obtained above or drying at 30-45°C, and then drying the sweet sorghum slag at 0.1- Soak in 0.5% H 2 SO 4 solution for 8-12 hours, then place it in a steam explosion tank, increase the pressure, keep it under 1.3-1.9MPa pressure for 6-10 minutes, release the pressure instantly, and collect the sweet sorghum slag obtained after steam explosion Wash the sweet sorghum slag after the acid blasting treatment with water to obtain the pretreated slurry and solid reclaimed product, add Ca(OH) 2 to the obtained slurry to adjust the pH value to 9.5-10.5, stir for 1-1.5h, and precipitate and filter to obtain Clarified pretreatment slurry.
上述生产乙醇的方法步骤(3)中所述的用纤维素酶将甜高粱渣酶解糖化是指加水浸没上述所得固体回收物,调节pH值为4.8~5.5,按甜高粱渣干重添加纤维素酶15~30FPU/g,β-葡萄糖糖苷酶20~30CBU/g,于45~50℃酶解72~108h,期间每隔5~8h搅拌一次,过滤,获得酶解糖液。Enzymatic hydrolysis and saccharification of sweet sorghum slag with cellulase as described in step (3) of the above method for producing ethanol refers to adding water to immerse the above-mentioned obtained solid recovery, adjusting the pH value to 4.8-5.5, adding fiber according to the dry weight of sweet sorghum slag Sulfase 15-30 FPU/g, β-glucosidase 20-30 CBU/g, enzymolysis at 45-50°C for 72-108 hours, stirring once every 5-8 hours during this period, filtering to obtain enzymolysis sugar solution.
上述生产乙醇的方法步骤(4)中所述的调节糖汁浓度是指将上述所得茎秆汁液、预处理浆液和酶解糖液混合,然后将混合糖液进行蒸煮浓缩,得糖汁浓度为16~24%的混合糖液。The adjustment of sugar juice concentration described in step (4) of the method for producing ethanol above refers to mixing the above-mentioned obtained stalk juice, pretreated slurry and enzymatic sugar solution, and then cooking and concentrating the mixed sugar solution to obtain a sugar juice concentration of 16-24% mixed sugar solution.
上述生产乙醇的方法步骤(5)中所述的酵母活化是指按照通常的方法制备酵母菌种子液,即将4℃斜面保藏的酵母菌株接种到酵母活化培养基中,于28~32℃、100~120rpm条件下恒温摇床中培养16~20h;然后再按5%的接种量转接入种子培养基中,于28~32℃、100~120rpm条件下恒温摇床中培养18~24h;依次扩大培养即可;其中所述的活化培养基的组成成分及其重量百分比为:1.5~2%葡萄糖,1.5~2%蛋白胨,0.8~1%酵母浸提物,0.15~0.2%KH2PO4,0.05~0.1%MgSO4,pH值5.0;其中所述的种子培养基的组成成分及其重量百分比为:1.5~2%葡萄糖,1.5~2%蛋白胨,0.8~1%酵母浸提物。The yeast activation described in step (5) of the method for producing ethanol above refers to preparing yeast seed liquid according to the usual method, that is, inoculating the yeast strains preserved on a slope at 4°C into the yeast activation medium, and inoculating them at 28-32°C, 100 Cultivate in a constant temperature shaker at ~120rpm for 16~20h; then transfer to the seed medium according to the inoculum amount of 5%, and cultivate in a constant temperature shaker at 28~32°C and 100~120rpm for 18~24h; Expanded cultivation is enough; the composition and weight percentage of the activated medium are: 1.5-2% glucose, 1.5-2% peptone, 0.8-1% yeast extract, 0.15-0.2% KH 2 PO 4 , 0.05-0.1% MgSO 4 , pH value 5.0; wherein the composition and weight percentage of the seed medium are: 1.5-2% glucose, 1.5-2% peptone, 0.8-1% yeast extract.
上述生产乙醇的方法步骤(6)中所述的发酵是指按照重量百分比向上述所得混合糖液中加入0.1~0.3%尿素、0.15~0.25%MgSO4·7H2O和0.25~0.5%CaCl2·2H2O,然后在100~120℃下灭菌10~15min,再按汁液体积比5~10%的接入酿酒酵母种子液,于32~35℃密封发酵32~48小时;然后蒸馏收集乙醇,得乙醇。The fermentation described in step (6) of the method for producing ethanol refers to adding 0.1 to 0.3% urea, 0.15 to 0.25% MgSO 4 ·7H 2 O and 0.25 to 0.5% CaCl 2 to the mixed sugar solution obtained above according to the weight percentage 2H 2 O, then sterilize at 100-120°C for 10-15min, then insert the Saccharomyces cerevisiae seed liquid according to the juice volume ratio of 5-10%, seal and ferment at 32-35°C for 32-48 hours; then collect by distillation Ethanol, get ethanol.
上述方法步骤(1)中所述的压榨可通过压榨机进行。The pressing described in the above-mentioned method step (1) can be carried out by a pressing machine.
上述方法步骤(4)中所述的纤维素酶是指耐高温纤维素酶、β-葡萄糖苷酶或羟甲基纤维素酶等;所述的纤维素酶均可从市场上购买,如从湖南尤特尔生化有限、杰能科公司、Sigma公司等公司购买。The cellulase described in above-mentioned method step (4) refers to high temperature resistant cellulase, β-glucosidase or hydroxymethyl cellulase etc.; Described cellulase can be purchased from the market, as from Purchased by Hunan Youtel Biochemical Co., Ltd., Genencor Corporation, Sigma Corporation and other companies.
上述步骤(6)中所述的酿酒酵母可从市场上购买,也可从中国微生物菌种保藏管理委员会普通微生物中心购买,如耐酒精酵母菌(Saccharomycescerevisiae 2.119)。The Saccharomyces cerevisiae described in the above step (6) can be purchased from the market, and can also be purchased from the General Microbiology Center of China Microbiological Culture Collection Management Committee, such as alcohol-resistant yeast (Saccharomycescerevisiae 2.119).
上述方法步骤(6)中所述的尿素的作用是作为氮源。The effect of the urea described in the above method step (6) is as a nitrogen source.
上述方法步骤(6)中所述的MgSO4·7H2O和0.5%CaCl2·2H2O的作用是作为营养盐。The MgSO 4 .7H 2 O and 0.5% CaCl 2 .2H 2 O described in step (6) of the above method are used as nutrient salts.
上述方法步骤(6)所述的发酵时间可根据发酵过程中排放CO2引起的失重控制发酵时间。The fermentation time described in the above method step (6) can be controlled according to the weight loss caused by discharging CO in the fermentation process.
上述方法中没有具体指出的部分应理解为通常所用的方法或者设备。Parts not specifically indicated in the above methods should be understood as commonly used methods or equipment.
本发明的优点:(1)本发明甜高粱秸秆利用率高,可将秸秆中的结构糖和非结构糖都得到充分的利用;(2)本发明乙醇产率高,由于利用了甜高粱的汁液和纤维素,因此其乙醇产率可达每100千克秸秆产7.3千克左右的乙醇;(3)本发明纤维素酶的糖化效率高,由于采用稀酸爆破处理技术,使半纤维素,木质素、纤维素结构分离,甜高粱渣结构空隙间隔增大,因此提高了纤维素酶的糖化效率,将甜高粱渣中以纤维素和半纤维素存在的结构糖最大程度水解,结构糖转化率可达85%以上;(4)本发明采用耐酒精的酒精酵母,可进行高密度发酵,缩短了发酵时间,提高了发酵效率,也可节省大量能源,提高设备利用率和生产效率;(5)本发明从根本上改变了以粮食为原料生产乙醇的现状。Advantages of the present invention: (1) the sweet sorghum stalk utilization rate of the present invention is high, and both the structural sugar and the non-structural sugar in the stalk can be fully utilized; (2) the ethanol yield of the present invention is high, due to utilizing the juice and cellulose, so its ethanol yield can reach about 7.3 kilograms of ethanol per 100 kilograms of straw; (3) the saccharification efficiency of the cellulase of the present invention is high, and due to the use of dilute acid blasting treatment technology, hemicellulose, woody Separation of cellulose and cellulose structure, increasing the interstitial interval of sweet sorghum dregs structure, thus improving the saccharification efficiency of cellulase, hydrolyzing the structural sugars existing in cellulose and hemicellulose in sweet sorghum dregs to the greatest extent, and improving the conversion rate of structural sugars Can reach more than 85%; (4) the present invention adopts alcohol-resistant alcoholic yeast, can carry out high-density fermentation, has shortened fermentation time, has improved fermentation efficiency, also can save a large amount of energy, improves equipment utilization rate and production efficiency; (5) ) The present invention fundamentally changes the present situation of producing ethanol with grain as raw material.
附图说明Description of drawings
图1为本发明工艺流程图。Fig. 1 is process flow chart of the present invention.
具体实施方式Detailed ways
实施例1Example 1
利用甜高粱茎秆生产乙醇,包括如下步骤:The production of ethanol using sweet sorghum stalks comprises the following steps:
(1)甜高粱茎秆榨汁 将含水量72.8%,含糖量13.9%,粗纤维含量9.6%的甜高粱茎秆100千克粉碎切割成10mm~25mm的丝状小段,用压榨机进行压榨,然后向所得甜高粱渣中加水进行二次压榨,得甜高粱汁液和残糖含量极低的丝状甜高粱渣;(1) Juicing of sweet sorghum stalks 100 kg of sweet sorghum stalks with a water content of 72.8%, a sugar content of 13.9%, and a crude fiber content of 9.6% are crushed and cut into filamentous segments of 10mm to 25mm, and squeezed with a press machine. Then adding water to the obtained sweet sorghum dregs for secondary pressing to obtain sweet sorghum juice and silky sweet sorghum dregs with extremely low residual sugar content;
(2)将甜高粱茎秆汁液100℃蒸煮30分钟,离心过滤,去沉淀,获得澄清的甜高粱汁液。(2) Cooking sweet sorghum stalk juice at 100° C. for 30 minutes, centrifuging and filtering, removing sediment to obtain clarified sweet sorghum juice.
(3)甜高粱渣稀酸爆破预处理 将甜高粱渣自然风干,用0.1%H2SO4溶液浸泡12小时,置入蒸汽爆破罐关闭装置;在1.5MPa压力下保持6min,瞬间泄压,收集汽爆原料;用水洗涤酸爆破处理的甜高粱渣,得预处理浆液和固体回收物,向预处理浆液中加入Ca(OH)2调节pH值到10.5,搅拌1h,沉淀过滤,弃沉淀,滤液用H2SO4中和到5.0,得澄清的预处理浆液;(3) Dilute acid blasting pretreatment of sweet sorghum slag Air-dried sweet sorghum slag naturally, soaked in 0.1% H 2 SO 4 solution for 12 hours, put in steam explosion tank closing device; kept at 1.5MPa pressure for 6 minutes, and released the pressure instantly, Collect steam explosion raw materials; wash the sweet sorghum slag treated by acid explosion with water to obtain pretreatment slurry and solid recovery, add Ca(OH) to the pretreatment slurry to adjust the pH value to 10.5, stir for 1h, precipitate and filter, discard the precipitate, The filtrate was neutralized to 5.0 with H 2 SO 4 to obtain a clear pretreatment slurry;
(4)甜高粱渣酶解糖化 加水浸没甜高粱渣预处理后的固体回收物,Ca(OH)2调节pH值到5.5,按甜高粱渣干重添加纤维素酶(湖南尤特尔生化有限公司生产)30FPU/g,β-葡萄糖糖苷酶(Novozym 188,诺维信公司生产)30CBU/g,于50℃酶解108h,每隔6h搅拌一次,过滤,得酶解糖液。(4) Enzymatic hydrolysis and saccharification of sweet sorghum slag Add water to immerse the solid recovery after sweet sorghum slag pretreatment, adjust the pH value to 5.5 with Ca(OH) 2 , add cellulase according to the dry weight of sweet sorghum slag (Hunan Youtel Biochemical Co., Ltd. Produced by the company) 30FPU/g, β-glucosidase (Novozym 188, produced by Novozymes) 30CBU/g, enzymatically hydrolyze at 50°C for 108h, stir once every 6h, filter to obtain enzymolyzed sugar solution.
(5)酵母培养 将在4℃斜面保藏的耐酒精酵母菌(Saccharomycescerevisiae 2.119,得自中国微生物菌种保藏管理委员会普通微生物中心)三环接种到20mL酵母种子活化培养基中,于32℃、120rpm恒温摇床中培养20h;然后再按5%的接种量转接入100ml的种子培养基中,于32℃、120rpm恒温摇床中培养20h;依次扩大培养;得酵母培养液。(5) Yeast culture Inoculate 20 mL of yeast seed activation medium with three rings of alcohol-resistant yeast (Saccharomycescerevisiae 2.119, obtained from the General Microbiology Center of China Microorganism Culture Collection Management Committee) preserved on a slope at 4°C, and inoculate at 32°C, 120rpm Cultivate in a constant temperature shaking table for 20 hours; then transfer 5% of the inoculum amount into 100 ml seed medium, and cultivate in a constant temperature shaking table at 32° C. and 120 rpm for 20 hours; expand the culture sequentially to obtain yeast culture solution.
(6)调节糖汁浓度 将步骤(2)所得甜高粱汁液、步骤(3)所得预处理浆液和步骤(4)所得酶解糖液混合,得混合糖液,将混合糖液进行蒸煮浓缩,得糖汁浓度为20%的混合糖液。(6) Adjusting the concentration of sugar juice Mix the sweet sorghum juice obtained in step (2), the pretreated slurry obtained in step (3) and the enzymatic sugar solution obtained in step (4) to obtain a mixed sugar solution, and cook and concentrate the mixed sugar solution, It is the mixed sugar liquid of 20% that the sugar juice concentration is obtained.
(7)发酵 向步骤(6)的混合糖液中添加0.3%尿素、0.25%MgSO4·7H2O和0.5%CaCl2·2H2O,于121℃灭菌15min,按汁液10%的比例将步骤(5)的耐酒精的酿酒酵母活化液添加到混合糖液中,然后于32℃密封发酵32h,发酵液中酒精浓度达8.3%(w/v),蒸馏收集乙醇,得乙醇7.56Kg。(7) Fermentation Add 0.3% urea, 0.25% MgSO 4 7H 2 O and 0.5% CaCl 2 2H 2 O to the mixed sugar solution in step (6), sterilize at 121°C for 15 minutes, and use 10% juice Add the alcohol-resistant Saccharomyces cerevisiae activation solution of step (5) into the mixed sugar solution, then seal and ferment at 32°C for 32 hours, the alcohol concentration in the fermentation solution reaches 8.3% (w/v), collect ethanol by distillation, and obtain 7.56Kg of ethanol .
实施例2Example 2
利用甜高粱茎秆生产乙醇,包括如下步骤:The production of ethanol using sweet sorghum stalks comprises the following steps:
(1)甜高粱茎秆榨汁 将含水量72.8%,含糖量13.9%,粗纤维含量9.6%的甜高粱茎秆100Kg粉碎切割成10mm~25mm的丝状小段,用压榨机进行压榨,然后向所得甜高粱渣中加水并进行二次压榨,得甜高粱汁液和残糖含量极低的丝状甜高粱渣。(1) Juicing of sweet sorghum stalks 100Kg of sweet sorghum stalks with a water content of 72.8%, a sugar content of 13.9%, and a crude fiber content of 9.6% are crushed and cut into filamentous segments of 10mm to 25mm, squeezed with a press, and then Adding water to the obtained sweet sorghum dregs and performing secondary pressing to obtain sweet sorghum juice and silky sweet sorghum dregs with very low residual sugar content.
(2)将步骤(1)所得甜高粱茎秆汁液100℃蒸煮30分钟,离心过滤,去沉淀,获得澄清的甜高粱汁液。(2) Cooking the sweet sorghum stalk juice obtained in step (1) at 100° C. for 30 minutes, centrifuging and filtering, and removing sediment to obtain clarified sweet sorghum juice.
(3)甜高粱渣稀酸爆破预处理 将步骤(1)所得甜高粱渣风干,用0.5%H2SO4溶液浸泡8小时,置入蒸汽爆破罐中,关闭装置;迅速升压,在1.5MPa压力下保持6min,瞬间泄压,收集汽爆原料;用水洗涤酸爆破处理的甜高粱渣,得预处理浆液和固体回收物,浆液中加入Ca(OH)2调节pH值到10.5,搅拌1h,沉淀过滤,弃沉淀,滤液用H2SO4中和到5.0,得澄清的预处理浆液。(3) Dilute acid blasting pretreatment of sweet sorghum slag Air-dry the sweet sorghum slag obtained in step (1), soak in 0.5% H 2 SO 4 solution for 8 hours, put it into a steam explosion tank, and close the device; Keep the pressure under MPa for 6 minutes, release the pressure instantly, and collect steam explosion raw materials; wash the sweet sorghum slag treated by acid explosion with water to obtain pretreated slurry and solid recovery, add Ca(OH) 2 to the slurry to adjust the pH value to 10.5, and stir for 1 hour , filtered the precipitate, discarded the precipitate, and neutralized the filtrate to 5.0 with H 2 SO 4 to obtain a clear pretreatment slurry.
(4)甜高粱渣酶解糖化。加水浸没甜高粱渣预处理后的固体回收物,Ca(OH)2调节pH值到5.0,按甜高粱渣干重添加纤维素酶(Celluclast 1.5L,诺维信公司生产)15FPU/g,β-葡萄糖糖苷酶(Novozym 188,诺维信公司生产)30CBU/g,于50℃酶解72h,每隔6h搅拌一次。获得酶解糖液。(4) Enzymatic hydrolysis and saccharification of sweet sorghum residue. Add water to immerse the solid recovery after sweet sorghum slag pretreatment, Ca(OH) 2 adjust the pH value to 5.0, add cellulase (Celluclast 1.5L, produced by Novozymes) 15FPU/g according to the dry weight of sweet sorghum slag, β -Glucosidase (Novozym 188, produced by Novozymes) 30CBU/g, enzymolysis at 50°C for 72h, stirring once every 6h. Obtain enzymatic sugar solution.
(5)酵母活化 将4℃斜面保藏的耐酒精酵母菌(Saccharomycescerevisiae 2.119,得自中国普通微生物菌种保藏管理中心)接种到20ml酵母种子活化培养基中,于32℃、120rpm恒温摇床中培养20h。然后再按5%的接种量转接入100ml的种子培养基中,于32℃、120rpm恒温摇床中培养18h。依次扩大培养。(5) Yeast activation Inoculate 20ml yeast seed activation medium with alcohol-resistant yeast (Saccharomycescerevisiae 2.119, obtained from the China Common Microorganism Culture Collection and Management Center) preserved on a slope at 4°C, and culture it in a constant temperature shaker at 32°C and 120rpm 20h. Then transfer 5% of the inoculum into 100 ml of seed culture medium, and cultivate for 18 hours at 32° C. and 120 rpm in a constant temperature shaker. Sequentially expand the cultivation.
(6)调节糖汁浓度 将步骤(2)所得甜高粱汁液、步骤(3)所得预处理浆液和步骤(4)所得酶解糖液混合,,得混合糖液,将混合糖液进行蒸煮浓缩,得糖汁浓度为16%的混合糖液。(6) Adjusting the concentration of sugar juice Mix the sweet sorghum juice obtained in step (2), the pretreated slurry obtained in step (3) and the enzymatic sugar solution obtained in step (4) to obtain a mixed sugar solution, and cook and concentrate the mixed sugar solution , It is the mixed sugar liquid of 16% that the sugar juice concentration is obtained.
(7)发酵 向步骤(6)所得混合糖液中添加0.3%尿素,添加0.25%MgSO4·7H2O,0.5%CaCl2·2H2O,于121℃灭菌15min,再将酿酒酵母活化液按汁液10%添加到混合糖液中,于35℃密封发酵32h,发酵液中酒精浓度为6.6%(w/v),蒸馏收集乙醇,得乙醇7.28Kg。(7) Fermentation Add 0.3% urea, 0.25% MgSO 4 7H 2 O, 0.5% CaCl 2 2H 2 O to the mixed sugar solution obtained in step (6), sterilize at 121°C for 15 minutes, and then activate Saccharomyces cerevisiae Add 10% of the juice to the mixed sugar liquid, and seal and ferment at 35°C for 32 hours. The alcohol concentration in the fermentation liquid is 6.6% (w/v), and the ethanol is collected by distillation to obtain 7.28Kg of ethanol.
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