产脂肪酶菌株筛选及柠檬酸杆菌产酶条件优化

脂肪酶可以催化甘油三酯水解成脂肪酸和甘油,已广泛应用在工业领域,而获得产酶微生物是研究的基础。采用油脂平板法筛选出1株脂肪酶产生菌。经16S rRNA序列分析可知,该菌株属于柠檬酸杆菌(Citrobacter werkman and Gillen)。单因素试验对其进行产酶条件优化,优化后产酶条件（g/L）：淀粉2.0,KH₂PO₄ 1.0,K₂HPO₄·3H₂O 2.2,(NH₄)₂SO₄ 1.0,MgSO₄·7H₂O 0.1,牛肉膏2.0,橄榄油10.0 mL,pH 7.5,接种量1.5%(v/v),37 ℃培养43 h。获得最大酶活为384 U/mL,是优化前的13倍。可以利用该菌制备脂肪酶。     

响应面法优化重组大肠杆菌产蔗糖异构酶发酵培养基

通过碳氮源的不同浓度对重组大肠杆菌E.coil BL21(DE3)发酵产蔗糖异构酶(SIase)的影响,并借助于数学分析软件Design Expert,结合Plackett-Burman试验设计和中心复合试验设计分析法,对蔗糖异构酶的产生菌进行了发酵培养基的优化研究。实验表明,最佳培养基组分为甘蔗糖蜜10.65 g/L,玉米浆22.22 g/L,NaCl 7.57 g/L ,MgSO₄·7H₂O 0.52 g/L, KH₂PO₄ 4.46g/L,优化后的蔗糖异构酶活力达到29.1U/ml,比LB培养基培养重组大肠杆菌(15U/ml),蔗糖异构酶活力提高了94%,与原始菌大黄欧文菌NX-5相比提高了21.4倍(1.3U/ml)。     

产低温脂肪酶菌株CZW001发酵培养基优化研究

【目的】研究产低温脂肪酶菌株CZW001发酵培养基。【方法】在单因素试验的基础上, 采用Plackett-Burman (P-B)设计, Box-Behnken (B-B)设计和响应面试验设计(RSM), 在20 °C、pH 8.0、160?r/min发酵2 d条件下, 对发酵培养基进行优化。【结果】该菌株最适产酶培养基为(g/L): 葡萄糖7.68, 橄榄油21.93, 硫酸铵2.0, 磷酸二氢钾1.0, 硫酸镁0.27, 氯化钙0.3, 氯化钠20.0, 吐温-80 1.0。其最高酶活为62.8 U/mL, 比优化前提高了3.14倍。【结论】通过对产低温脂肪酶菌株CZW001发酵培养基优化研究, 明显提高低温脂肪酶活力。     

硫酸镁对枯草芽胞杆菌发酵的影响

为明确工业配方中不同MgSO₄添加量对枯草芽胞杆菌B201发酵过程及菌液保存的影响,采用单因素法设置5个MgSO₄添加量梯度(质量分数,下同)( 0.13%、0.24%、 0.46%、0.87%、1.70%)。分别记录不同梯度MgSO₄处理的发酵液灭菌前后pH值,以及发酵过程中的菌体形态的变化,统计发酵结束后细菌的发酵周期、活菌数和芽肥率,测量发酵结束后发酵液pH以及残糖和残氮含量。实验表明,MgSO₄的不同添加量对菌株B201发酵及菌液保存均有显著影响。添加量为0.87%和1.70%处理组灭菌后培养基的pH较灭菌前升高,培养基由中性变为弱碱性。接种后12 h取样观察,菌体明显变形,视野内菌数较少,且随着MgSO₄添加量的增加发酵液活菌数下降,残糖和残氮升高,不利于保存。MgSO₄相对合适的添加量为0.13%、0.24%和0.46%,三种MgSO₄添加量的发酵液活菌数、残氮含量无显著差异;MgSO₄添加量为0.24%时菌株B201芽肥率最高为89.33%,而MgSO₄添加量为0.13%和0.46%时,芽肥率分别为80%和82.67%;0.46%MgSO₄添加量可加速菌株B201发酵进程,发酵周期较其他两个处理缩短45.8%。为提高菌株B201的发酵水平,降低其生产成本,综合考虑MgSO₄的添加量以0.46%为宜。研究结果不仅为实验室菌株B201的发酵优化提供参考,还为培养基的优化拓宽了思路。     

响应面法优化洋葱假单胞菌产脂肪酶液体发酵工艺

用响应面法对洋葱假单胞菌G-63液体发酵产脂肪酶条件进行了优化。首先运用单因子试验筛选出麦芽糖和豆粉水解液为最适碳源和氮源。在此基础上,通过Plackett-Burman设计试验,对影响产酶条件的11个相关因子进行评估并筛选出具有显著效应的3个因子:橄榄油、豆饼粉水解液以及初始pH值。在用最陡爬坡实验逼近以上3个因子的最大响应区域后,采用响应面分析法,确定出橄榄油、豆粉水解液的最佳浓度和最佳初始pH值分别为4.337%,1.956%和8.38。优化后液体发酵培养基中脂肪酶活力提高到44.39 U/mL,比初始酶活13.45 U/mL提高了3.3倍。     

低温脂肪酶的产酶条件优化及其酶学性质

利用单因素筛选和正交试验对Burkholderia sp. SYBC LIP-Y发酵产酶的液体培养基和发酵条件进行了优化,其优化配方为：可溶性淀粉10 g/L、牛肉膏15 g/L、NaNO3 0.252 g/L、橄榄油40ml/L、Triton x-100 10ml/L、初始pH 7.5、接种量10%(V/V),脂肪酶酶活达到85.23U/ml,是优化前的3.63倍。通过对双水相纯化得到的脂肪酶进行酶学性质研究,确定该酶反应的最适pH为10.0,最适温度为30℃,40℃下保温60min酶活性还有80%以上,该脂肪酶为低温脂肪酶,热稳定性好,具有一定的耐醇性,应用前景广阔。     

脂肪酶产生菌的筛选、鉴定及其产酶条件优化

目的:寻找合适的产酶菌。方法:从富油土壤中分离到一株脂肪酶产生菌,并通过16S rRNA部分序列分析和系统发育分析将其鉴定为假单胞菌属,定名为:Pseudomonas sp.26-2。本研究进一步通过正交试验设计对该菌株的产脂肪酶条件进行了优化。结果:在摇瓶培养条件下,其最适产酶条件为:淀粉1.5%,酵母提取物3%,硫酸镁0.05%,K2HPO40.2%,橄榄油0.2%;反应起始pH值为7.0,发酵温度为30℃。在此条件下,发酵脂肪酶活力可达15.5U/ml。结论:所获得的假单胞菌26-2具有一定的脂肪酶生产能力,并为该菌株的菌种改良以及脂肪酶的高效基因工程菌的构建奠定了基础。     

带His-tag的解脂耶氏酵母脂肪酶Lip2在毕赤酵母中的表达及纯化

将去自身信号肽并且N-端带6×His标签的YlLip2基因克隆至表达载体pPIC9K中,电转化GS115获得高效表达脂肪酶His₆-YlLip2的基因工程菌。筛选到的阳性克隆子摇瓶发酵脂肪酶活力最高为400U/ml。对重组毕赤酵母在10 L发酵罐中表达His₆-YlLip2的分批补料发酵工艺进行了初步优化,探讨了培养基、pH、温度对生物量和重组蛋白表达量的影响。结果表明:采用FM22培养基,诱导温度为25℃,pH 5.0,甲醇诱导114 h后His₆-YlLip2的最高酶活力达到3160U/ml。SDS-PAGE分析表明,蛋白的分子量大约为38kDa。重组的His₆-YlLip2经镍柱一步纯化后的纯度达到95.43%,比酶活达到4250U/mg。     

重组大肠杆菌产角质酶-CBM摇瓶发酵优化及分泌表达研究

在TB培养基的基础上,通过单因素分析和正交设计对重组大肠杆菌产角质酶-CBM发酵进行优化,得到最适培养基的组分为:甘油5 g/L,蛋白胨 16 g/L,MgSO₄·7H₂O 2.5 mmol/L,K₂HPO₄ 13.7 g/L,KH₂PO₄ 1.53 g/L,菌体生长至对数前中期时添加终浓度为1 g/L乳糖 和0.75 g/L 甘氨酸,30℃发酵48 h,角质酶-CBM产量可达63 U/ml,较TB培养(20 U/ml)提高了近3倍。考察了热激作用、渗透调节物质及温度两控制对角质酶-CBM分泌表达的影响,在添加Lactose和Glycine后,发现在添加终浓度为75 mmol/L的L-脯氨酸,37℃热激1 h或47℃热激0.5 h,变温至25℃发酵,角质酶-CBM产量可达90 U/ml,较TB恒温培养提高了近四倍。     

白腐菌产锰过氧化物酶条件的研究

白腐菌Phanerochaeta chrysosporium MIG. 383降解桉木时具有显著的选择性,30天内降解37．23％Klason木素,7.29％综纤维素。该菌株产胞外锰过氧化物酶,并在高碳低氧培养基中显示较高酶活。静置液体培养的优化培养条件是(L^-1)：10g葡萄糖,2mmol酒石酸铵,10mmol pH4.5醋酸钠缓冲液,1g吐温80,2gK₂PO₄,0.5g MgSO₄·7H₂O,0.1g CaCl₂·2H₂O,lmg VB₁,70ml微量元素混合液：最适产酶温度是37℃。上述条件下,该菌接种后静置培养4天,产锰过氧化物酶活达1840U／L,酶作用最适温度是37℃,最适DH是3.5。     

脂肪酶产生菌的选育及产酶条件的优化

A lipase-producing bacterium strain was isolated from soil and was identified as Pseudomonas sp.. Its lipase yield was improved 2.25-fold by combined beatment of UV irradiation and NTG. The lipase fermentation condition for the mutant strain was optimized with Plackett-Burman design and Response Surface Analysis(RSA), and the formula of the optimum medium suitable for industrial scale fermentation was thereby established. A maximum yield of 87.5 U/ ml was obtained.     

卡门柏青霉-PG3脂肪酶的研究

从242株青霉属菌株中筛选出脂肪酶产生菌青霉-PG3。经鉴定,定名为卡门柏青霉(Penicillium camembertii Thom)。卡门柏青霉-PG3在由4％豆饼粉,0.5％糊精,0.75％橄榄油,0.5％K_2HPO_4,0.1％(NH_4)_2SO_4组成的液体培养基中,28℃,振荡培养96小时,发酵液脂肪酶活力(39℃,pH7.0)达60U/ml。PG3脂肪酶以橄榄油为底物,水解反应最适温度为48℃,最适pH为8.0。pH稳定范围6.0—11.0。Cu~(2+),Ca~(2+),Fe~(2+),Pb~(2+)等金属离子对酶活力有抑制作用。PG3脂肪酶对椰子油、菜籽油、亚麻油等油脂的水解率分别达到96％,94％和90％。     

假丝酵母菌GXU08产脂肪酶发酵条件的优化

以假丝酵母菌GXU08产脂肪酶催化合成麝香类香料—环十五内酯目前已备受关注,在一定条件下,环十五内酯的转化率与脂肪酶的水解酶活有直接关系,酶活越高其催化合成环十五内酯的能力越强。通过单因素试验和正交试验,对假丝酵母菌GXU08产脂肪酶的发酵条件进行优化。结果表明:最佳发酵培养基配方为蔗糖0.5%,淀粉0.5%,蛋白胨1.5%,K_2HPO_40.05%,MgSO_40.15%,(NH_4)_2SO_41%,茶油1.5%,菜籽油1.5%,pH=8,此培养基在28℃,180 r/min的条件下发酵培养48h,脂肪酶水解活力达到27.53 U/mL,是初始发酵培养基条件下所得脂肪酶酶活的3.74倍;其环十五内酯的转化率为16.6%,是优化前的4倍。     

低温脂肪酶产生菌的筛选、产酶发酵及粗酶性质研究

利用含有Tween 80的琼脂平板和摇瓶发酵法,从若尔盖高原土壤中筛选产脂肪酶菌株.通过菌落形态和菌体特征观察初步对菌种进行鉴定,得到一株产低温脂肪酶的适冷菌Pseudomonassp.DL-B,并设计正交试验对该菌株的产酶发酵培养条件进行了优化.摇瓶实验表明,该菌株最适产酶发酵培养基为:蔗糖10 g/L,蛋白胨20 ...     

Isolation and Screening of Alkaline Lipase-producing Fungi from Brazilian Savanna Soil

Summary Fifty-nine lipase-producing fungal strains were isolated from Brazilian savanna soil by employing enrichment culture tecniques. An agar plate medium containing bile salts and olive oil emulsion was employed for isolating and growing fungi in primary screening assay. Twenty-one strains were selected by the ratio of the lipolytic halo radius and the colonies radius. Eleven strains were considered good producers under conditions of submerged liquid fermentation (shaken cultures) and solid-state fermentation. The most productive strain, identified as Colletotrichum gloesporioides, produced 27,700 U/l of lipase under optimized conditions and the crude lipase preparation was capable of hydrolysing a broad range of substrates including lard, natural oils and tributyrin.     

Streptomyces sp. TEM 33 possesses high lipolytic activity in solid-state fermentation in comparison with submerged fermentation

Solid-state fermentation (SSF) is a bioprocess that doesn’t need an excess of free water, and it offers potential benefits for microbial cultivation for bioprocesses and product development. In comparing the antibiotic production, few detailed reports could be found with lipolytic enzyme production by Streptomycetes in SSF. Taking this knowledge into consideration, we prefer to purify Actinomycetes species as a new source for lipase production. The lipase-producing strain Streptomyces sp. TEM 33 was isolated from soil and lipase production was managed by solid-state fermentation (SSF) in comparison with submerged fermentation (SmF). Bioprocess-affecting factors like initial moisture content, incubation time, and various carbon and nitrogen additives and the other enzymes secreted into the media were optimized. Lipase activity was measured as 1.74 ± 0.0005 U/g dry substrate (gds) by the p-nitrophenylpalmitate (pNPP) method on day 6 of fermentation with 71.43% final substrate moisture content. In order to understand the metabolic priority in SSF, cellulase and xylanase activity of Streptomyces sp. TEM33 was also measured. The microorganism degrades the wheat bran to its usable form by excreting cellulases and xylanases; then it secretes the lipase that is necessary for degrading the oil in the medium.     

Enhancement of thermostable lipase production by a genotypically identified extremophilic Bacillus subtilis NS 8 in a continuous bioreactor

Bacillus strain NS 8, a lipase-producing bacterium isolated from a Malaysian hot spring, is able to tolerate a broad range of temperature and pH, which makes it beneficial for this study. It generated PCR products with molecular weight of 1,532 bp, and the 16S rRNA sequence analysis identified it as Bacillus subtilis with accession number AB110598. It showed a 71% similarity index with B. subtilis using Biolog Microstation System. Its lipase production was optimized using a shake flask system by changing the physical (agitation speed, pH and temperature) and nutritional (nitrogen, carbon and minerals) factors. The most suitable combination of the basal medium for lipase production was 2.5% olive oil (carbon), 1.5% peptone (nitrogen), 0.1% MgSO(4) (mineral) at an optimum temperature of 50°C, pH 7.5 and 150 rpm agitation, giving an enzyme yield of 4.23 U/ml. Statistical optimization using response surface methodology was carried out. An optimum lipase production of 5.67 U/ml was achieved when olive oil concentration of 3%, peptone 2%, MgSO(4)·7H(2)O 0.2% and an agitation rate of 200 rpm were combined. Lipase production was further carried out inside a 2-liter bioreactor, which yielded an enzyme activity of 14.5 U/ml after 15 h of incubation.     

Production of a Thermostable Lipase by Humicola lanuginosa Grown on Sorbitol-Corn Steep Liquor Medium

For thermostable lipase production by Humicola lanuginosa No. 3, a simple optimized medium consisting of (%, w/v): sorbitol, 1.0; corn steep liquor, 1.0; NaCl, 0.5; CaCl₂–2H₂0, 0.01; Silicone Km-70 (antifoamer), 0.2; and whale oil or castor oil as a lipase inducer, 0.3, was used. The yield of the lipase was about 80 — 120U/ml after 25 hr aerobic cultivation at 45°C when the pH was maintained at 7 to 8. The acetone powder preparation of the enzyme was most active at pH 7.0 and 45°C. The enzyme retained 100% activity on incubation for 20 hr at 60°C. The enzyme was able to hydrolyze almost all forms of natural fats tested (14 kinds), coconut oil being the most rapidly hydrolyzed.