固液态发酵中橄榄油对Rhizopus chinensis全细胞脂肪酶的影响*

主要对华根霉全细胞脂肪酶固态和液态两种发酵过程进行比较,并着重探讨不同培养方式下橄榄油对其合成活力和水解活力的影响。结果表明:液态培养较有利于菌体生长,对脂肪酶的生产也有一定的促进作用。橄榄油的加入不仅有利于菌体生长、提高脂肪酶水解活力,更可使脂肪酶的合成活力显著增加,液态发酵下的效果更为明显。橄榄油在整个发酵过程中可能既作为碳源又是脂肪酶的诱导物。另外,全细胞脂肪酶的水解活力和合成活力在固液态发酵条件下均存在不对应性,表明华根霉可能产性质不同的脂肪酶同功酶。     

华根霉脂肪酶有机相合成酶活的研究

通过比较7种微生物脂肪酶的有机相合成酶活、水相水解酶活及在正庚烷中催化己酸乙酯合成的能力,证明了合成酶活与水解酶活相关性不高,合成酶活比水解酶活更能反映脂肪酶的合成能力。通过比较两株华根霉(Rhizopus chinensis)脂肪酶酶活,发现合成酶活相差较大,表明相同种属微生物的脂肪酶合成酶活存在不同。对．Rhizopus chinensis-2液态发酵产脂肪酶进程研究发现,水解酶活高峰先于合成酶活高峰大约12h。将不同培养时间的Rhizopus chinensis-2全细胞脂肪酶用于催化己酸乙酯合成,具有高合成酶活的全细胞脂肪酶催化己酸乙酯合成反应较快。因此,全细胞脂肪酶用于催化有机相酯合成反应时,具有高脂肪酶合成酶活的菌体具有较好的催化酯合成能力。     

华根霉液态培养生产脂肪酶不同形态菌体的转录组差异分析

【背景】作为发酵工业中一类重要的生产菌株,丝状真菌目的产物的形成与菌体形态有着紧密的联系。华根霉(Rhizopus chinensis)CCTCC M201021是从我国传统酿造浓香型白酒大曲中筛选到的一株丝状真菌,其生成的包括脂肪酶在内的酶蛋白具有较高的工业应用价值。【目的】华根霉(Rhizopus chinensis)CCTCC M201021在脂肪酶液态发酵中形成两种不同形态菌体,发酵表现差异明显。本研究考察华根霉不同菌体形态及其细胞代谢在转录组水平的内在差异。【方法】基于RNA-Seq高通量转录组测序,分别对液态培养获得的不同形态华根霉菌体高表达和显著差异表达的转录基因进行功能分析。【结果】两种形态菌体转录组存在明显的差异。利用RPKM值对表达量最高的前20个基因进行分析,聚集态菌体高表达基因主要为不同类别的核糖体蛋白,而分散态菌体中与细胞形态相关的几丁质酶及与信号传导相关的基因也是高表达基因。在两种形态菌体显著差异表达的20个基因中,除了涉及代谢的基因有明显不同外,分散态菌体中也有一些涉及"细胞过程与信号"的基因上调表达显著。两种形态菌体中独有表达基因总体表达量均较低,但聚集态菌体独有表达基因在基因种类和表达量上都要明显高于分散态菌体。同时,转录分析表明,华根霉脂肪酶在聚集菌体中较高的生产水平与脂肪酶基因的高水平转录有关。【结论】菌体形态的差异显著影响了华根霉的转录组,不仅不同形态菌体高表达基因和显著差异表达基因有明显不同,而且功能相同的蛋白在不同菌体形态下也多是由不同基因表达,它们可能承担着不同的作用。总体而言,华根霉聚集态菌体中存在更为复杂的生理过程,而分散菌体中受到信号的传导和调控似乎更多。菌体形态的改变可能是细胞分化的结果,伴随着菌体对细胞微环境改变的一种响应。研究结果为深入了解丝状真菌形态分化的内在机制及其影响提供了一些线索。     

蓝色犁头霉深层发酵产壳低聚糖生长动力学研究

目的:研究蓝色犁头霉产壳低聚糖分批发酵动力学的模型.方法:在10L发酵罐中,将蓝色犁头霉分批发酵培养,对蓝色犁头霉菌丝体生长、产物形成和基质消耗的实验数据进行分析,根据Logistic和Luedeking-Piret方程分别建立蓝色犁头霉发酵过程菌体生长、壳低聚糖生成和基质消耗的动力学数学模型,并利用1stOpt软件对模型参数进行非线性曲线拟合.结果:研究得到了菌体生长、产物合成及基质消耗的动力学模型及参数,模型的拟合度分别为0.994、0.986、0.992.结论:研究表明蓝色犁头霉多糖合成和菌体生长呈生长偶联型,模型计算值与实验值有良好的拟合性,模型准确度较高.     

脂肪酶发酵过程中的油脂利用

对假丝酵母Candidasp．99—125发酵生产脂肪酶的过程中油脂代谢情况进行了研究。分析了发酵过程中甘油酯、油酸、棕榈酸等物质浓度随发酵时间的变化趋势,以及它们与菌体生长和产酶之间相互影响关系,结果发现油酸的消耗能够显著地促进脂肪酶的合成（油酸质量浓度从30g／L降低到10g／L）,并且细胞对油酸和棕榈酸的利用没有选择性,最终发酵脂肪酶活力可达8000U／mL。     

多拷贝毕赤酵母重组菌表达GCL摇瓶优化和高密度发酵

目的:构建高效表达白地霉脂肪酶的毕赤酵母重组菌株,并对筛选得到的菌株进行摇瓶发酵条件优化和分批补料高密度发酵工艺研究。方法:将诱导型表达载体pPIC9K-gcl电转化至毕赤酵母GS115。通过橄榄油-罗丹明B平板和摇瓶发酵筛选高脂肪酶活力的重组菌株,运用基于TaqMan探针的实时荧光定量PCR 法确定其拷贝数,并对菌株进行摇瓶发酵条件优化。在此基础上,研究重组菌在3L 发酵罐中的高密度发酵工艺。结果:筛选得到一株具有3 个白地霉脂肪酶基因拷贝的菌株GS115/pPIC9K-gcl 78#,初始酶活力为220 U/ml。当摇瓶发酵条件为甲醇诱导96 h,每24 h甲醇添加量1 %,接种量2 %,培养基初始pH 7.0,500 ml摇瓶装液量50 ml,甲醇诱导温度25℃ 时酶活力达735 U/ml。3L 发酵罐高密度发酵176.5 h,酶活力达到3360 U/ml,总蛋白含量达到4.30 g/L,且发酵过程中细胞活性一直保持在96 % 以上。结论:基因拷贝数与重组菌株的产酶水平呈正相关,摇瓶优化可显著提高重组菌株的产酶能力,为白地霉脂肪酶的工业化生产奠定了技术基础。     

疏棉状嗜热丝孢菌脂肪酶在毕赤酵母中的表面展示及酶学性质

【目的】构建疏棉状嗜热丝孢菌脂肪酶(Thermomyces lanuginosus lipase,TLL)在毕赤酵母GS115中的细胞表面展示体系,筛选展示成功且酶活力及展示率较高的重组子作为全细胞催化剂,并研究其酶学性质。【方法】克隆TLL基因tll,以酿酒酵母细胞壁蛋白Sed1p为锚定蛋白,构建表面展示载体pPICZαA-TLS。重组载体经SacⅠ线性化后转入毕赤酵母GS115中,经三丁酸甘油酯平板检测及摇甁发酵筛选获得高酶活力的毕赤酵母重组子,采用抗FLAG标签一抗和R-PE荧光素标记的二抗处理细胞后,进行荧光显微镜检测和流式细胞仪分析,并考察全细胞催化剂的最适反应温度和pH、金属离子耐受性等酶学性质。【结果】成功构建TLL毕赤酵母细胞表面展示体系,筛选到1株具有三丁酸甘油酯和橄榄油水解活力的克隆子,经1%的甲醇诱导发酵120 h后,水解橄榄油酶活力达257.8 U/g干细胞。经抗体处理后的重组菌发酵细胞在荧光显微镜下呈现强烈的红色荧光,流式细胞仪分析结果也证实脂肪酶被成功展示在酵母细胞表面,展示率达98.36%。展示的TLL作为全细胞催化剂水解对硝基苯酚丁酸酯(pNPB)的最适温度为30℃,最适pH为8.0,且具备良好的热稳定性和有机溶剂耐受性;K+、Ca2+、Mg2+对其有微弱的激活作用,Mn2+、Ni2+则有微弱的抑制作用,Cu2+的抑制作用较强,而EDTA、SDS、Tween 20对酶活力影响不明显。【结论】首次将TLL脂肪酶成功展示在毕赤酵母细胞表面,获得具有较高水解活力和良好酶学特性的全细胞催化剂,为表面展示TLL脂肪酶的规模化应用奠定了技术基础。     

培养条件对里氏木霉306菌体形态和t-PA生物合成的影响

里氏木霉（Trichoderrna reesei）306是能够生物合成组织型纤溶酶原激活剂（t-PA）的基因工程菌株。在对其液态深层培养时,发现随培养夸件和培养时间的变化,其菌体能以松散和菌丝球的两种形态存在。菌体形态和t-PA的产生密切相关。培养基中无机盐和表面活性剂的种类和添加量以及接种量和pH等培养条件是影响里氏木霉306菌体形态和t-PA合成的主要因素。在液态深层培养过程中,菌体以松散的菌丝体形态生长,形成纸浆状发酵液,利于t-PA的合成。     

影响被孢霉产生含r—亚麻酸油脂的几种因素

对培养条件,如氮源种类、Ｃ／Ｎ比率、ｐＨ、种子种龄与接种量对被孢霉（Ｍｏｒｔｉｅｒｅｌｌａ ｓｐ）Ｍ１４菌株的细胞生长和油脂形成的影响作了研究。结果表明,二级发酵优于一级发酵。Ｍ１４菌株二级发酵时,种子种龄以４９ｈ为适,接种量宜大（３０％）。无机氮源有利于不饱和脂肪酸的产生,有机氮源有利于细胞的增殖。低Ｃ／Ｎ比率有利于菌丝体产量的提高,提高Ｃ／Ｎ比率则能促进菌体细胞内的油脂合成。ｐＨ对菌体生长、油     

pH值对D-核糖发酵的影响及补料发酵的研究

研究了不同 pH值对D 核糖产量的影响。发酵初期pH自然下降时有利于菌体生长 ,菌体生长对数期较长 ,菌体质量浓度最高可达 15 .3g/L ;发酵中后期 pH值控制在 7.0时有利于D 核糖的持续合成 ,同时对D -核糖的流加补料发酵进行了初步研究 ,最终使菌体质量浓度最高达到 2 0 .1g/L ,D 核糖产量达到了 6 2 .5g/L。     

Culture condition improvement for whole-cell lipase production in submerged fermentation by Rhizopus chinensis using statistical method

Rhizopus chinensis CCTCC M201021 was a versatile strain capable of producing whole-cell lipase with synthetic activity in submerged fermentation. In order to improve the production of whole-cell lipase and study the culture conditions systematically, the combination of taguchi method and response surface methodology was performed. Taguchi method was used for the initial optimization, and eight factors viz., maltose, olive oil, peptone, K2HPO4, agitation, inoculum size, fermentation volume and pH were selected for this study. The whole-cell lipase activity yield was two times higher than the control experiment under initial optimal conditions, and four significant factors (inoculum, olive oil, fermentation volume and peptone) were selected to test the effect on the lipase production using response surface methodology. The optimal fermentation parameters for enhanced whole-cell lipase yield were found to be: inoculum 4.25 x 10(8) spores/L, olive oil 2.367% (w/v), fermentation volume 18 mL/250 mL flask, peptone 4.06% (w/v). Subsequent experimental trails confirmed the validity of the model. These optimal culture conditions in the shake flask led to a lipase yield of 13875 U/L, which 120% increased compare with the non-optimized conditions.     

Effect of nonionic surfactants on Rhizopus homothallicus lipase activity: a comparative kinetic study

Based on amino-terminal sequencing and mass spectrometry data on the Rhizopus homothallicus lipase extracted using solid (SSF) and submerged state fermentation (SmF) methods, we previously established that the two enzymes were identical. Differences were observed, however, in terms of the specific activity of these lipases and their inhibition by diethyl p-nitrophenyl phosphate (E600). The specific activity of the SSF lipase (10,700 μmol/min/mg) was found to be 1.2-fold that of SmF lipase (8600 μmol/min/mg). These differences might be the result of residual Triton X-100 molecules interacting with the SSF lipase. To check this hypothesis, the SmF lipase was incubated with submicellar concentrations of Triton X-100. The specific activity of the lipase increased after this treatment, reaching similar values to those measured with the SSF lipase. Preincubating SSF and SmF lipases with E600 at a molar excess of 100 for 1 h resulted in 80% and 60% enzyme inhibition levels, respectively. When the SmF lipase was preincubated with Triton X-100 for 1 h at a concentration 100 times lower than the Trition X-100 critical micellar concentration, the inhibition of the lipase by E600 increased from 60% to 80%. These results suggest that residual detergent monomers interacting with the enzyme may after the kinetic properties of the Rh. homothallicus lipase.     

Production and Regulation of Lipase Activity from <Emphasis Type="Italic">Penicillium restrictum</Emphasis> in Submerged and Solid-State Fermentations

Different carbon (C) sources, mainly carbohydrates and lipids, have been screened for their capacity to support growth and lipase production by Penicillium restrictum in submerged fermentation (SmF) and in solid-state fermentation (SSF). Completely different physiological behaviors were observed after the addition of easily (oleic acid and glucose) and complex (olive oil and starch) assimilable C sources to the liquid and solid media. Maximal lipolytic activities (12.1 U/mL and 17.4 U/g) by P. restrictum were obtained with olive oil in SmF and in SSF, respectively. Biomass levels in SmF (12.2–14.1 mg/mL) and SSF (7.0–8.0 mg/g) did not varied greatly with the distinct C sources used. High lipase production (12.3 U/g) using glucose was only attained in SSF, perhaps due to the ability of this fermentation process to minimize catabolite repression.     

Production and regulation of different lipase activities from Rhizopus chinensis in submerged fermentation by lipids

The fungal Rhizopus chinensis could produce several types of lipase, which were mainly intracellular. During the whole-cell lipase production by this strain in submerged fermentation, it was observed that two catalytic characteristics (hydrolytic and synthetic activity) of lipases were different with addition of lipids. The hydrolytic activity of the lipase was not induced by lipids efficaciously and could be detected regardless of whether substrate-related compounds were present. However, it was found that the induction of lipids for the synthetic activity lipase was significant, and that nearly no synthetic activity was detected while the medium contained no lipids. When only a little lipid (1 g/L) was added to medium, the synthetic activity increased sharply in the initial process of fermentation. Analysis of crude membrane-bound lipase by SDS-PAGE confirmed this induction. De novo biosynthesis of lipases, especially the lipase with synthetic activity occurred only when lipids existed. Cell growth and maltose repress the lipase production with synthetic activity, but have little influence on the lipase production with hydrolytic activity. Since the production process of mycelium-bound lipase with hydrolytic activity was different, it was reasonable to consider hydrolytic activity and synthetic activity for different application purposes. Whole-cell lipase obtained from fermentation process with high synthetic activity showed excellent catalytic ability in solvent free system on synthesis of ethylcaprylate and ethyloleate, the conversion could reach more than 90% in 5 h.     

华根霉合成活性脂肪酶液态发酵菌体形态调控的研究

华根霉(CCTCC M201021)膜结合脂肪酶在非水相中具有突出的催化酯合成的能力,在生物香料、生物柴油生产等工业应用中具有良好的前景.与许多丝状真茵形态影响其初级及次级代谢产物的生产相类似,华根霉在液态发酵中也会形成不同的茵体形态,显著影响合成活性膜结合脂肪酶的发酵水平.本研究以华根霉菌体形态及脂肪酶合成活性为指标...     

Exopectinases produced by Aspergillus niger in solid-state and submerged fermentation: a comparative study

Exopectinase production by Aspergillus niger was compared in submerged fermentation (SmF) and solid-state fermentation (SSF). SSF was carried out using polyurethane foam (PUF) as the solid support. The purpose was to study the effect of sucrose addition (0 or 40 g/l) and water activity level (A _w=0.99 or 0.96) on the level of enzyme activity induced by 15 g/l of pectin. Mycelial growth, as well as extracellular protease production, was also monitored. Sucrose addition in SmF resulted in catabolite repression of exopectinase activity. However, in SSF, an enhancement of enzyme activity was observed. Protease levels were minimal in SSF experiments with sucrose and maximal in SmF without sucrose. Exopectinase yields (IU/g X) were negligible in SmF with sucrose. The high levels of exopectinase with sucrose and high A _w in SSF can be explained by a much higher level of biomass production without catabolite repression and with lower protease contamination. Journal of Industrial Microbiology & Biotechnology (2001) 26, 271–275. Received 05 July 2000/ Accepted in revised form 27 January 2001     

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.     

Lipase production and Penicillium simplicissimum morphology in solid-state and submerged fermentations

A comparative study of Penicillium simplicissimum morphology and lipase production was performed using solid-state (SSF) and submerged (SmF) fermentation. SSF was carried out on babassu cake as culture medium and SmF on a semi-synthetic medium and a medium based on suspended babassu cake grains. Yield of product on biomass, specific activity and conidia production were 3.3-, 1.3- and 2-fold higher in SSF. In SmF, the type of fungus growth differed according to the medium. Using the semi-synthetic medium, the fungus formed densely interwoven mycelial masses without conidia production, whereas using the babassu-based medium the fungus formed free mycelia and adhered to the surfaces of the grains, producing conidia. The results show that babassu cake induces conidiation in SmF. In SSF, the fungus not only grew on the surface of the grains, producing conidia abundantly, but also effectively colonized and penetrated the babassu particles. The high conidia production and lipase productivity in SSF may be related to the low availability of nutrients or to other stimuli associated with this type of fermentation. Thus, the high production of the thermostable P. simplicissimum lipase, using a non-supplemented, low-cost agro-industrial residue as the culture medium, demonstrates the biotechnological potential of SSF for the production of industrial enzymes.     

Laccase production in solid‐state and submerged fermentation by Pleurotus ostreatus

A solid‐state fermentation (SSF) system for production of an industrially important enzyme laccase by Pleurotus ostreatus was developed by using potato dextrose yeast extract medium and polyurethane foam as a supporting material. The maximum laccase production in the SSF system was as high as 3×10⁵ U/L. Addition of inducers, such as copper and ferulic acid, further enhanced the laccase production in SSF. Moreover, the time required for the maximum laccase production was reduced to 6 days compared to 10 days reported earlier. The improvement achieved by the SSF system was investigated by comparing it to a submerged fermentation system (SmF), both experimentally and by using a standard theoretical model along with a parameter sensitivity analysis. Laccase production in SSF was found to be twice of that in SmF. One of the main reasons for higher laccase production in SSF compared to SmF was possibly due to the presence of higher proteolytic activity in SmF. Strong proteolytic activity in SmF presumably caused subsequent laccase degradation, which lowered the ultimate laccase production in SmF compared to SSF.