过表达氨基葡萄糖脱氨酶对大肠杆菌氨基葡萄糖合成及中心碳代谢的影响

考察过表达氨基葡萄糖脱氨酶对氨基葡萄糖合成及大肠杆菌（Escherichia coli）中心碳代谢的影响。实验结果表明：过表达氨基葡萄糖脱氨酶使得在36 g/L葡萄糖,pH为9.0的发酵条件下,发酵24 h后,重组菌发酵液中氨基葡萄糖、丙酮酸和乙酸的量分别是对照菌Rosetta的2.1、1.48和1.74倍;而乳酸的量为2.53 g/L,对照菌Rosetta发酵液中的乳酸含量未检测到,重组菌发酵液中柠檬酸及α-酮戊二酸的含量分别是Rosetta的2.99和2.73倍。     

氧载体对小白链霉菌发酵生产ε-聚赖氨酸的影响

为了有效改善发酵体系中的溶氧水平,提高小白链霉菌Streptomyces albulus PD-1发酵生产ε-聚赖氨酸的能力,文中通过对氧载体的种类、最佳添加浓度以及添加时间进行筛选,最终确定在0 h添加0.5%(V/V)的正十二烷促进ε-聚赖氨酸生产效果最佳。在5 L发酵罐0 h添加0.5%的正十二烷进行批次补料发酵,ε-聚赖氨酸的产量和菌体干重分别可以达到(30.8±0.46)g/L和(33.8±0.29)g/L,较之对照组分别提高了31.6%和20.7%。ε-聚赖氨酸的产量和菌体干重的提高归因于0.5%正十二烷的添加促进发酵液中溶氧水平从23.8%提高到32%,同时发酵液中的一种主要副产物(聚二氨基丙酸)的含量下降31%。实验结果表明,正十二烷的添加可以提高S.albulus PD-1发酵液中的溶氧水平,抑制副产物的生成,促进ε-聚赖氨酸的合成。     

菌丝桥在日本落叶松幼苗间磷传递和植株生长中的作用

 应用四室隔网系统研究了菌丝桥在日本落叶松(Larix kaempferi)幼苗间传递磷的作用。结果表明,供体接种卷缘桩菇(Paxillus involutus)和彩色豆马勃（Pisolithus tinctorius）后,其外延菌丝可以穿过隔离层侵染受体落叶松,在供体和受体落叶松间形成了菌丝桥。供体植株接种菌根真菌后生物量明显增加,但是对受体植株没有显著的影响。菌根真菌侵染的供体和受体植株的根、地上部吸磷量均分别显著高于对照,而且供体植株根、地上部吸磷量增加的程度明显高于受体。被卷缘桩菇和彩色豆马勃侵染的受体植株体内32P的放射性强度分别是对照的10倍和6倍,两者形成菌丝桥后传递到受体植株的32P分别为供体植株体内32P的1.10%和0.22%。供体植株吸收的32P可以通过菌丝桥传递给受体,但是绝对数量十分有限,对受体植株磷营养没有产生显著的影响,但P. involutus和P. tinctorius侵染受体植株后,促进了受体落叶松对磷的吸收,这是菌丝桥形成后,真菌帮助受体植株吸收磷引起的。     

氨茶碱与柠檬酸盐协同作用促进环磷酸腺苷发酵生产

目的: 探究通过抑制磷酸二酯酶活性促进cAMP发酵合成的工艺方法。方法: 在7 L发酵罐上进行添加氨茶碱的发酵实验,通过对发酵主要参数、关键酶活性、能量代谢水平等进行分析,针对性提出了氨茶碱与柠檬酸盐协同作用促进cAMP合成的发酵工艺。结果: 与对照相比,添加5 mg/L氨茶碱批次的cAMP产量提高25.9%,副产物腺苷浓度减少41.6%,两批次中腺苷酸环化酶和琥珀腺苷酸脱氢酶活性无显著改变,而磷酸二酯酶和5'-核苷酸酶活性明显下降。能量代谢分析结果表明,两批次的胞内ATP/AMP相比于对照批次明显降低,而AMP水平却显著上升,ATP合成水平成为限制产物积累的主要因素。氨茶碱与柠檬酸盐协同添加的cAMP发酵工艺中,cAMP产量达到4.48 g/L,比单独添加柠檬酸钠和氨茶碱分别提高22.1%和13.8%,副产物腺苷浓度仅为0.98 g/L,分别降低51.7%和25.3%。结论: 氨茶碱抑制了磷酸二酯酶和5'-核苷酸酶活性,减少cAMP分解和副产物合成,显著提高cAMP产量,然而ATP合成水平成为产物积累的限制因素。氨茶碱与柠檬酸盐协同添加工艺将抑制磷酸二酯酶活性和提高能量代谢水平相结合,进一步促进了产物发酵合成。     

不同补料控制方式发酵生产头孢菌素C的性能比较

在7 L发酵罐下,对利用顶头孢霉菌(Cephalosporins acremonium)发酵生产头孢菌素C(CPC)过程的最优底物流加工艺进行了研究。提出了一种新式硫铵豆油耦联型的硫铵流加策略。该控制策略可将发酵液中的氨态氮浓度控制在3 6 g/L之间,同时满足了发酵前期细胞生长与CPC合成对氮源和硫源的需求,促进了顶头孢霉菌菌丝分化,为发酵后期的CPC高效生产奠定了前期基础。比较了CPC合成期内间歇、匀速和DO-Stat自动流加3种不同豆油流加方式的发酵性能。研究发现,耦联使用硫铵/后程通富氧空气DO-Stat法进行硫铵和豆油的同时补料和CPC发酵,可将碳源浓度与溶解氧浓度DO同时控制于适中水平,使CPC合成以高浓度和低副产物积累的方式进行,最终CPC浓度和得率分别达到35.77 g/L和13.3%。主代谢副产物脱乙酰氧头孢菌素C(DAOC)的积累量和DAOC/CPC分别仅有0.178 g/L和0.5%。     

解淀粉芽胞杆菌hemX基因缺失对血红素合成的影响

血红素是一种广泛存在于生物体中的卟啉类化合物,具有多种生理功能。解淀粉芽胞杆菌(Bacillus amyloliquefaciens)具有易于培养、分泌表达能力较强等特点,是一种重要的工业菌株。为了筛选血红素合成的最优出发菌株,以不添加和添加5-氨基乙酰丙酸(5-aminolevulinic acid, ALA)的方式,对实验室保藏菌株进行筛选,发现不添加ALA时,菌株BA、BAΔ6、BAΔ6ΔsigF的血红素产量无明显差别;然而添加ALA后,BAΔ6ΔsigF的血红素产量和比生产能力均为最高,分别达到200.77μmol/L和615.70μmol/(L·g DCW)。因此,以BAΔ6ΔsigF为出发菌株,敲除编码细胞色素组装蛋白HemX的hemX基因,探究其在血红素合成途径中的作用,发现敲除菌株发酵液明显变红,且生长未受到明显影响;摇瓶发酵12 h时ALA浓度最高,为82.13 mg/L,略高于对照的75.11 mg/L;不添加ALA时,血红素产量和比生产能力分别为对照的1.99倍和1.45倍;添加ALA后,血红素产量和比生产能力分别为对照的2.08倍和1.72倍;实时定量荧光PCR...     

低聚磷酸盐与次黄嘌呤偶合添加提高环磷酸腺苷发酵性能

环磷酸腺苷(cAMP)在微生物细胞内由ATP直接环化形成,而ATP的合成需要能量与前体的持续供应。通过添加次黄嘌呤激活补救途径,促进了cAMP的合成,与对照批次相比生产效率提高了39. 1%,但发酵进行至51h产物不再生成,而且产量未能得到提高。偶合添加次黄嘌呤和2g/L-broth六聚偏磷酸钠发酵批次的cAMP产量达到7. 24g/L,比单独添加次黄嘌呤和六聚偏磷酸钠的批次产量分别提高了125. 5%和93. 5%,生产效率也显著提高,达到了0. 101g/(L·h)。六聚偏磷酸钠和次黄嘌呤偶合添加工艺将低聚磷酸盐和补救途径的优势相结合,有效促进了cAMP合成与积累。     

油酸促进灵芝三萜液态深层发酵的工艺研究及规模化验证

灵芝三萜是灵芝中主要的活性成分之一,前期研究发现油酸可以促进灵芝三萜液态深层发酵下的发酵合成。本研究主要对油酸促进灵芝三萜液态深层发酵的工艺进行优化,并进行3L发酵罐规模的验证。通过单因素实验考察油酸的添加方式、添加时间和添加浓度对灵芝三萜的影响,结合响应面实验,获得最优工艺条件并进行验证：在发酵第32h添加1.21%高温灭菌油酸,最高灵芝三萜含量为42.69mg/g;在发酵第7h添加1.35%过滤除菌油酸,最高三萜含量为43.38mg/g,分别比对照提高2.04倍和2.08倍。在1 000mL摇瓶中添加高温灭菌油酸和过滤除菌油酸,灵芝三萜含量分别为32.18和32.48mg/g,为对照的1.96倍和1.95倍;在3L发酵罐规模下灵芝三萜含量分别为28.66和25.13mg/g,为对照的1.62倍和1.42倍。本研究系统优化了油酸促进灵芝三萜液态深层发酵的工艺条件,并在与工业生产相对应的3L发酵罐上进行验证。该研究可为灵芝三萜的规模化发酵提供重要参考和借鉴。     

促甲基化因子对西索米星发酵的影响

研究发现,发酵培养基中添加2．0—3．0g,／L蛋氨酸或7．5—10．0mg,／L氯化钴可明显促进西索米星的合成。蛋氨酸的添加时机和添加方式对西索米星产物合成的作用明显不同。在产物合成中前期（30-48h）添加蛋氨酸的效果最佳。当发酵液中蛋氨酸初始浓度为0．656g／L时,与在产物合成初期一次性添加相比,1．5g／L蛋氨酸在产物合成初期、中期和后期均分成3次添加的效果更优,当发酵至91h结束时,发酵液中西索米星浓度可达0．70g／L。     

粗甘油优化污泥脱水液培养小球藻过程的研究

污泥脱水液为污泥压缩过程产生的污水,因其含有N、P等营养物,可用于微藻的培养。但污泥脱水液碳氮比低,可利用碳源有限,影响微藻生长。本研究考察外加不同浓度(1 g/L,2 g/L,4 g/L,6 g/L)生物柴油副产物-粗甘油对污泥脱水液培养小球藻过程的影响。结果表明:1 g/L、2 g/L粗甘油浓度能促进小球藻生长,藻生物量为1.29 g/L、1.45 g/L;2 g/L粗甘油浓度下氨氮、总氮去除率达99.32%和97.52%。粗甘油被分解后易使培养体系pH降至7以下,使总磷去除率比对照组略低。外加1 g/L、2 g/L粗甘油组的COD去除量分别为553.00 mg/L和405.00 mg/L。藻细胞元素和傅里叶红外光谱分析表明补加粗甘油后藻细胞中C元素和H元素相对含量均明显增加,C元素含量约为对照组的1.5倍;2 g/L粗甘油组的蛋白质与脂类物质含量均高于对照组。MPBR半连续培养小球藻过程中,HRT为5 d时藻生物量维持在1.99~2.21 g/L,大约为批次生物量的1.50倍;氨氮、总氮、总磷、COD的去除率分别在96.26%~99.20%、92.44%~94.04%、53.63%~58.58%、59.44%~65.57%。     

Enhanced curdlan production in <Emphasis Type="Italic">Agrobacterium</Emphasis> sp. ATCC 31749 by addition of low-polyphosphates

A large amount of adenosine triphosphate with high energy phosphate bonds is required for uridine triphosphate regeneration during curdlan biosynthesis by Agrobacterium sp. ATCC 31749. To supply high energy for curdlan synthesis, three low-polyphosphates (Na₄P₂O₇, Na₅P₃O₁₀, and (NaPO₃)₆) with higher energy phosphate bonds were employed to substitute for KH₂PO₄-K₂HPO₄ in fermentation medium. Two genes encoding the polyphosphate metabolizing enzymes, polyphosphate kinase and exopolyphosphatase, were amplified and showed 95% homology to those in Agrobacterium sp. C58 by sequence analysis. The curdlan yields were enhanced by 23 and 134% when phosphate concentrations 0.024 mol/L of Na₅P₃O₁₀ and 0.048 mol/L of (NaPO₃)₆ respectively, were added in the medium. The maximum curdlan yield of 30 ± 1.02 g/L was obtained with the addition of 0.048 mol/L of (NaPO₃)₆ with 5 g/L CaCO₃ in the medium. When CaCO₃ was removed from the culture and the three lowpolyphosphates were added, the pH and biomass yield dropped remarkably and little or no curdlan was produced. The culture containing 0.048 mol/L of (NaPO₃)₆ was mixed with KH₂PO₄-K₂HPO₄ and CaCO₃ in the medium, but showed no effect on curdlan production. However, curdlan yield was improved by 49 ∼ 60% when CaCO₃ was removed from the medium and KH₂PO₄-K₂HPO₄ acted as a buffer. It appears that the positive effect of (NaPO₃)₆ on curdlan production required the buffering capacity of CaCO₃ and the absence of KH₂PO₄-K₂HPO₄ competing as a phosphate supplier.     

氨水流加用于粪产碱杆菌热凝胶发酵

热凝胶是粪产碱杆菌(Alcaligenes faecalis)在氮源限制条件下生成的水不溶性胞外多糖,分泌到胞外后就附着在菌体外壁,因此在细胞生长期提高生物量对促进热凝胶合成有重要意义。热凝胶分批发酵时, 起始NH4Cl浓度提高到3.6 g/L时能促进菌体生长和热凝胶合成,但是过量NH4Cl会抑制热凝胶合成,且生物量提高不是很明显。为了进一步提高菌体浓度, 在菌体生长期, 氨水取代NaOH溶液进行流加控制pH为7.0, 随后又用2 mol/L NaOH控制pH 5.6。实验表明, 氨水流加使菌体浓度大大提高,流加24 h使菌体浓度达到18.8 g/L。但是菌体浓度过高也会抑制热凝胶的合成,在氨水流加14 h时,菌体浓度在11.9 g/L左右, 热凝胶产量最高（72 g/L）。     

氨水流加用于粪产碱杆菌热凝胶发酵

热凝胶是粪产碱杆菌(Alcaligenes faecalis)在氮源限制条件下生成的水不溶性胞外多糖,分泌到胞外后就附着在菌体外壁,因此在细胞生长期提高生物量对促进热凝胶合成有重要意义。热凝胶分批发酵时, 起始NH4Cl浓度提高到3.6 g/L时能促进菌体生长和热凝胶合成,但是过量NH4Cl会抑制热凝胶合成,且生物量提高不是很明显。为了进一步提高菌体浓度, 在菌体生长期, 氨水取代NaOH溶液进行流加控制pH为7.0, 随后又用2 mol/L NaOH控制pH 5.6。实验表明, 氨水流加使菌体浓度大大提高,流加24 h使菌体浓度达到18.8 g/L。但是菌体浓度过高也会抑制热凝胶的合成,在氨水流加14 h时,菌体浓度在11.9 g/L左右, 热凝胶产量最高（72 g/L）。     

pH控制对热凝胶发酵的影响

热凝胶 (Ｃｕｒｄｌａｎ)是一种直链结构的 β 1,3 葡聚糖 ,由Ａｌｃａｌｉｇｅｎｅｓｆａｅｃａｌｉｓｖａｒ.ｍｙｘｏｇｅｎｅｓ发酵生产而来 ,是一种新型的微生物胞外多糖[1 ] ,其分子量在 5 0万左右。热凝胶在中性条件下不溶于水 ,但能溶于碱溶液中。加热含有热凝胶的水浊液可形成两种类型的凝胶 ,一种是弹性较低的类似琼脂的可逆胶 ;另外一种是凝胶强度大、弹性好的热不可逆胶。由于热凝胶具有独特的热成胶性能 ,在食品工业 ,特别是高温制作的食品领域具有广阔的应用前景。热凝胶的胶体可以包容和控制药物的扩散 ,所以可以用来作为药物…     

Production of extracellular water insoluble β-1,3-glucan (curdlan) fromBacillus sp. SNC07

β-1,3-Glucan (curdlan) is a water-insoluble polysaccharide composed exclusively of β-1,3 linked glucose residues. Extracellular curdlan was mostly synthesized byAgrobacterium species andAlcaligenes faecalis under nitrogen-limiting conditions. In this study, we screened the microorganisms capable of producing extracellular curdlan from soil samples. For the first time, we reported Gram-positive bacteriumBacillus sp. SNC 107 capable of producing extracellular curdlan in appreciable amounts. The effect of different carbon sources on curdlan production was studied and found that the yield of curdlan was more when glucose was used as carbon source. It was also found that maximum production was achieved when the initial concentration of ammonium and phosphate in the medium was 0.5 and 1.9 g/L respectively. In this study the curdlan production was increased from 3 to 7 g/L in shake flask cultures.     

氮源NH4Cl浓度对粪产碱杆菌发酵生产热凝胶的影响

研究了利用粪产碱杆菌(Alcaligenes faecalis)发酵生产热凝胶的发酵条件,氮源是菌体生长的限制性底物,单纯地提高初始底物(氮源)浓度并不一定能促进细菌的生长和产物的合成.在分批发酵过程中,底物消耗导致培养环境pH的改变也是影响细菌进一步生长和产物合成的重要因素.通过增加培养基中初始氯化铵的浓度并同时控制发酵过程的pH条件,得到了较高的菌体浓度,热凝胶的合成水平也得到了显提高.当培养基中NH4Cl浓度提高到3.6g/L时,菌体浓度达到7.2g/L,热凝胶合成的产量可达30.5g/L,比原来NH4Cl浓度为1.1g/L时提高了51.7%.提高菌体浓度意味着需要提高溶氧水平来满足细菌的生长和代谢.初始氮源NH4Cl浓度的增加虽然能使菌体浓度得到提高,但发酵过程对溶氧的需求也相应增加,需要提高搅拌转速和通风以增加供氧水平.但高搅拌速率产生的高剪切力对热凝胶的凝胶性能将产生破坏作用,因此在发酵过程中需要综合考虑细菌培养密度对合成热凝胶产量和质量的影响.     

Production and characterization of curdlan by Agrobacterium sp.

Agrobacterium sp. was studied for the production of curdlan by conventional one-factor-at-a-time technique and response surface methodology. Factors such as initial pH, urea concentration, sucrose concentration having the greatest influence on the curdlan production were identified. By using response surface methodology (RSM), the curdlan production by Agrobacterium sp. was increased significantly by 109%, from 2.4 g/L to 5.02 g/L when the strain was cultivated in the optimal medium developed by RSM as compared to conventional one-factor-at-a-time technique. The curdlan production rate of 0.84 g/(L h) was obtained when Agrobacterium sp. was cultivated in the optimal medium developed by RSM, which was the highest curdlan production rate reported to date. The infrared (IR) and NMR spectra, the thermogram of DSC and pattern of X-ray diffraction for the curdlan of the present study were almost identical to those of the authentic curdlan sample (from Alcaligenes faecalis; Sigma). The purified curdlan was a linear polysaccharide composed of exclusively β-(1,3)-glucosidic linkages with the molecular weight of 160,000 Da by GPC. The crystalline melting point (T_m), glass transition temperature (T_g) and X-ray diffraction of the sample indicated low crystallinity in the structure.     

热凝胶的高产策略及功能研究进展

热凝胶（curdlan）又名β-（1→3）-D-葡聚糖,在食品、医药、保健品等领域具有重要的应用潜力。由粪产碱杆菌（Alcaligenes faecalis）或土壤杆菌（Agrobacterium sp．）生物合成的热凝胶以成本低廉、提取与纯化技术成熟而成为研究热点。笔者主要针对提高热凝胶产量的菌株改造和发酵控制策略以及热凝胶生物活性的研究进展和相关专利进行综述。     

Residual phosphate concentration under nitrogen-limiting conditions regulates curdlan production in Agrobacterium species

We investigated the influence of inorganic phosphate concentration on the production of curdlan by Agrobacterium species. A two-step culture method was employed where cells were first cultured, followed by curdlan production under nitrogen-limiting conditions. In the curdlan production step, cells did not grow but metabolized sugar into curdlan. Shake-flask experiments showed that the optimal phosphate concentration for curdlan production was in the range of 0.1–0.3 g l⁻¹. As the cell concentration increased from 0.42 to 1.68 g l⁻¹ in shake-flask cultures, curdlan production increased from 0.44 to 2.80 g l⁻¹. However, the optimal phosphate concentration range was not dependent upon cell concentration. The specific production rate was about 70 mg curdlan g-cell⁻¹ h⁻¹ irrespective of cell concentration. When the phosphate concentration was maintained at 0.5 g l⁻¹ under nitrogen-limiting conditions, as high as 65 g l⁻¹ of curdlan was obtained in 120 h. Journal of Industrial Microbiology & Biotechnology (2000) 25, 180–183. Received 25 October 1999/ Accepted in revised form 21 July 2000     

Effect of Tween 80 on the production of curdlan by Alcaligenes faecalis ATCC 31749

This study aims to investigate the effects of Tween 80 on curdlan production, cell growth, and glucosyltransferase activity. The addition of Tween 80 to the culture medium increased curdlan production. However, curdlan production did not increase further when excessive Tween 80 (>0.3% Tween 80) was added to the culture medium. The addition of Tween 80 to the culture medium did not affect cell growth. The glucosyltransferase activity involved in the curdlan synthesis increased with the increase of Tween 80 concentration. The glucosyltransferase activity did not increase further when excessive Tween 80 (>0.3% Tween 80) was added to the culture medium. Maximum curdlan was observed at day 5 and then levelled off. The biomass continued to increase until the end of the experimental period (6 d). Maximum glucosyltransferase activity was also observed at day 5 and decreased thereafter. The results indicate that the enhanced curdlan production by Tween 80 is highly correlated with glucosyltransferase activity.