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.     

米根霉利用纯糖和不同预处理玉米秸秆酶解糖生产L-乳酸

通过单因素实验设计,优化米根霉摇瓶发酵产L-乳酸。在此基础上,以蒸气爆破和碱处理玉米秸秆酶解液为混合C源,与纯糖对比,研究不同预处理玉米秸秆混合C源对米根霉发酵产L-乳酸的影响。结果显示:在初始葡萄糖质量浓度100g/L、(NH4)2SO4质量浓度2g/L、接种量6%(体积分数)、转速170r/min、发酵12h后添加30g/LCaCO3的条件下,米根霉发酵产L-乳酸质量浓度为69.15g/L。米根霉发酵不同预处理玉米秸秆酶解混合C源,木糖的存在影响了米根霉的C代谢网络,降低L乳酸的产量。     

进化代谢选育高浓度NH_4~+耐受型产丁二酸大肠杆菌

利用大肠杆菌厌氧制备丁二酸过程中,采用氨水作为p H调节剂不仅可以中和酸性产物还可提供无机氮,被菌体利用,然而高浓度NH_4~+的积累会抑制菌体生长及代谢产酸的能力。为增强大肠杆菌对高浓度NH_4~+的耐受性,以(NH4)2HPO4为NH_4~+供体,通过在连续培养装置中不断提高(NH_4)_2HPO4浓度,以获得可耐受0.53 mol/L NH_4~+的产丁二酸大肠杆菌。结果表明:突变株在0.53 mol/L NH_4~+胁迫下,摇瓶厌氧发酵72 h,细胞干质量浓度(DCW)可达1.82 g/L,丁二酸产量为11.72 g/L,分别比出发菌株提高了1.6和4.6倍。进一步地,在5 L发酵罐上考察其利用氨水调节p H生产丁二酸的能力,厌氧发酵90 h,丁二酸质量浓度达到27.32 g/L,生产强度为0.30g/(L·h),比出发菌株分别提高88.1%和87.5%。     

耐铵型产琥珀酸放线杆菌的选育及铵离子对其生长代谢的影响

经硫酸二乙酯(DES)诱变,在含61～242mmol/LNH4+梯度平板中,筛选到一株耐铵型突变株YZ25,该菌株在含121mmol/LNH4+发酵培养基中,琥珀酸产量达32.68g/L,转化率为65.4%,比出发菌提高了180.5%。进一步考察了不同形态铵盐对YZ25生长的影响,结果表明添加少量铵盐能够提高突变菌的生长速率,但当超过一定量后菌株生长受到抑制,不同铵盐对菌株的抑制程度不同,硫酸铵、碳酸氢铵、氯化铵和硝酸铵对突变株YZ25的半抑制浓度分别为:215mmol/L、265mmol/L、235mmol/L、210mmol/L。为了考察铵离子对YZ25发酵产琥珀酸的影响过程,在3.0L发酵罐以氨水作为pH的调控剂发酵,结果表明在稳定期前菌株生长基本不受铵离子抑制,生物量能够达到正常水平,但是进入稳定期后铵离子抑制作用越来越明显,导致菌株生长提前结束,耗糖不完全,产酸受阻。最后结合产琥珀酸放线杆菌Actinobacillus succinogenes代谢途径分析了铵离子对菌株抑制作用的机理。     

不同pH调节剂对产琥珀酸放线杆菌NJ113发酵产丁二酸的影响

在3L发酵罐中分别采用不同的碱性物质作为pH调节剂,考察其对产琥珀酸放线杆菌Actinobacillus succinogenes NJ113厌氧发酵制备丁二酸的影响。结果表明:Ca2+、NH4+调节剂对菌体生长代谢有较大阻碍作用,丁二酸产量较低;采用含Na+调节剂,在发酵中后期菌体出现絮凝现象严重,且产丁二酸能力骤降;采用含Mg2+调节剂,整个发酵过程菌体代谢旺盛,发酵效果较佳。根据各碱性物质的调节能力以及对菌体生长代谢的影响,选择NaOH、Mg(OH)2和Na2CO3、Mg(OH)2分别作为混合碱组分调节pH,并对两组混合碱中各物质的质量比例进行优化。结果表明,以NaOH、Mg(OH)2混合,两者质量比为1:1时,发酵效果最好,丁二酸质量浓度高达到69.8g/L,质量收率74.5%。该种混合碱配比可有效替代碱式MgCO3调节pH,既达到高产丁二酸的目的,又可降低生物制备丁二酸的成本。     

乙酸、糠醛和5-羟甲基糠醛对产酸克雷伯氏菌发酵生产2,3-丁二醇的影响

为了解产酸克雷伯氏菌对木质纤维素水解液中主要抑制物的耐受和代谢,考察了产酸克雷伯氏菌发酵生产2,3-丁二醇(2,3-butanediol,2,3-BDO)过程中对3种发酵抑制物乙酸、糠醛和5-羟甲基糠醛(5-hydroxymethylfurfural HMF)的耐受以及抑制物浓度的变化,检测了糠醛和HMF的代谢产物.结果表明:产酸克雷伯氏菌对乙酸、糠醛和HMF的耐受浓度分别为30 g/L、4 g/L和5 g/L.并且部分乙酸可作为生产2,3-丁二醇的底物,在0～30 g/L浓度范围内可提高2,3-丁二醇的产量.发酵过程中产酸克雷伯氏菌可将HMF和糠醛全部转化,其中约70％HMF被转化为2,5-呋喃二甲醇,30％HMF和全部糠醛被菌体代谢.研究表明在木质纤维素水解液生产2,3-丁二醇的脱毒过程中可优先考虑脱除糠醛,一定浓度的乙酸可以不用脱除.     

L-缬氨酸产生菌的选育及其发酵培养基的优化

以黄色短杆菌(Brevibacterium flavum)NJ-237为出发菌株,通过梯度传代适应性培养及同浓度药物平板富集培养的方式,逐步提高菌体的抗药物性能,获得了1株耐高糖和耐高浓度α-氨基丁酸(-αAB)的菌株NJ-2372。在单因素实验的基础上,利用响应面分析法对影响该菌株L-缬氨酸(L-Val)产量的3个重要因素玉米浆、生物素(VH)、硫胺素(VB1)的添加量进行优化。结果表明:当玉米浆、VH、VB1最佳添加量分别为11 g/L、35μg/L和101μg/L时,摇瓶发酵72 h,L-Val摇瓶发酵产量达到52.9 g/L。     

高糖和氮源对鼠李糖乳杆菌(Lactobacillus rhamnosus)L-乳酸发酵的影响

鼠李糖乳杆菌经实验室耐高糖高酸选育,能够在高糖浓度下高效高产L-乳酸。以酵母粉为氮源和生长因子,葡萄糖初始浓度分别为120 g/L和146 g/L,摇瓶培养120h,L-乳酸产量分别为104g/L和117.5g/L,L-乳酸得率分别为86.7%和80.5%。高葡萄糖浓度对菌的生长和乳酸发酵有一定的抑制。增加接种量,在高糖浓度发酵条件下,可以缩短发酵时间,但对增加乳酸产量效果不明显。乳酸浓度对鼠李糖乳杆菌生长和产酸有显著的影响。初始乳酸浓度到达70g/L以上时,鼠李糖乳杆菌基本不生长和产酸,葡萄糖消耗也被抑制。酵母粉是鼠李糖乳杆菌的优良氮源,使用其它被测试的氮源菌体生长和产酸都有一定程度的下降。用廉价的黄豆粉并补充微量维生素液,替代培养基中的酵母粉,可以使产酸浓度和碳源得率得以基本维持。     

4-氯乙酰乙酸乙酯羰基还原酶产生菌的筛选及产酶条件研究

从实验室保藏的菌株中,筛选到一株立体选择性较高的产4-氯乙酰乙酸乙酯(COBE)羰基还原酶的菌株———出芽短梗霉(Aureobasidiumpullulans)SW0202,菌体产酶条件研究表明,最佳的发酵培养基配方为:麦芽糖30.0g/L,酵母膏20.0g/L,蛋白胨3.0g/L,(NH4)2SO45.0g/L,KH2PO42.0g/L,MgSO4.7H2O0.7g/L,最适发酵温度及初始pH分别为:28°C和pH6.0。该菌在此条件下发酵培养24h,产菌丝体生物量16.78g干菌体/L,COBE羰基还原酶酶活力达到1007U/L。在COBE的转化反应中,产物S-CHBE的浓度达到10.12g/L,光学纯度>97%e.e.。     

铁改性沸石对Clostridium acetobutylicum XY16固定效率及发酵性能的影响

考察4种无机铁盐改性沸石对丁醇生产菌Clostridium acetobutylicum XY16的固定效率及其发酵产丁醇性能的影响。结果表明:铁改性沸石对菌体的固定效率均优于未改性沸石,而Fe3+改性效果优于Fe2+,经FeCl3改性的沸石对菌体具有良好的吸附作用,当Fe3+-zeolite用量为180 g/L时,细胞的固定效率达到87%。在此基础上,比较了沸石负载的铁离子量对丁醇发酵性能的影响,沸石负载的铁离子量为6.0 mg/g时可显著提高丁醇发酵性能,当葡萄糖质量浓度为60 g/L时进行发酵,丁醇产量为13.5 g/L,总溶剂可达20 g/L,总溶剂的生产速率为0.385g/(L.h),比游离细胞发酵分别提高了9.5%、10.3%和40%。     

Purification of an inducible L-valine dehydrogenase of Streptomyces coelicolor A3(2)

Valine dehydrogenase (VDH) from Streptomyces coelicolor A3(2) was purified from cell-free extracts to apparent homogeneity. The enzyme had an Mr 41,000 in denaturing conditions and an Mr 70,000 by gel filtration chromatography, indicating that it is composed of two identical subunits. It oxidized L-valine and L-alpha-aminobutyric acid efficiently, L-isoleucine and L-leucine less efficiently, and did not act on D-valine. It required NAD+ as cofactor and could not use NADP+. Maximum dehydrogenase activity with valine was at pH 10.5 and the maximum reductive amination activity with 2-oxoisovaleric acid and NH4Cl was at pH 9. The enzyme exhibited substrate inhibition in the forward direction and a kinetic pattern with NAD+ that was consistent with a sequential ordered mechanism with non-competitive inhibition by valine. The following Michaelis constants were calculated from these data: L-valine, 10.0 mM; NAD+, 0.17 mM; 2-oxoisovalerate, 0.6 mM; and NADH, 0.093 mM. In minimal medium, VDH activity was repressed in the presence of glucose and NH4+, or glycerol and NH4+ or asparagine, and was induced by D- and L-valine. The time required for full induction was about 24 h and the level of induction was 2- to 23-fold.     

重要环境因子对小球藻去除污水中氮磷的影响

对小球藻去除污水中氮磷的性能进行了研究,考察了初始氮磷浓度、氮磷比、光照条件和pH等因素对其去除效率的影响。结果表明,在初始氮磷浓度分别在35 mg/L和7 mg/L以下时去除率接近100%;氮磷比为5∶1和10∶1,小球藻第4 d基本完全去除了污水中的氨态氮,而氮磷比对小球藻的除磷能力没有显著影响;在初始氨态氮或总磷浓度相同的条件下,光照条件(L/D为24 h∶0 h和12 h∶12 h)对氮磷去除效果的无明显差异性（P＞0.05）,而随着氮磷浓度的增加,连续光照条件逐渐展现出去除氮磷的优势;小球藻在pH 7～8范围内对氨态氮的去除率最佳,pH 5～7范围内,对总磷的去除率最佳。     

Resistance of Maize Calli to Herbicide Basta and Its Relevant Effect by Some Amino Acids

Maize (Zea mays L. ) embryogenic calli were cultured on N6 medium and treated respectively with different concentrations of herbicide Basra and amino acids. The NH4+ concentrations and weight increase of maize calli were measured. Statistical analysis revealed that callus weight increased less when cultured on N6 medium with 4 mg/L of Basta while Nih+ concentration reached its peak when cultured on N6 with 8 mg/L of Basta. Therefore 6 mg/L of Basta was considered as the optional dosage for selection of transgenic calli L-arginine and L-glutamic acid significantly reduced the NH4+ concentration in maize calli while L-proline had little effects on NH4+ concentration even though it enhanced callus weight enormously.     

High-yield production of L-valine in engineered Escherichia coli by a novel two-stage fermentation

L-valine is an essential amino acid and an important amino acid in the food and feed industry. The relatively low titer and low fermentation yield currently limit the large-scale application of L-valine. Here, we constructed a chromosomally engineered Escherichia coli to efficiently produce L-valine. First, the synthetic pathway of L-valine was enhanced by heterologous introduction of a feedback-resistant acetolactate acid synthase from Bacillus subtilis and overexpression of other two enzymes in the L-valine synthetic pathway. For efficient efflux of L-valine, an exporter from Corynebacterium glutamicum was subsequently introduced. Next, the precursor pyruvate pool was increased by knockout of GTP pyrophosphokinase and introduction of a ppGpp 3′-pyrophosphohydrolase mutant to facilitate the glucose uptake process. Finally, in order to improve the redox cofactor balance, acetohydroxy acid isomeroreductase was replaced by a NADH-preferring mutant, and branched-chain amino acid aminotransferase was replaced by leucine dehydrogenase from Bacillus subtilis. Redox cofactor balance enabled the strain to synthesize L-valine under oxygen-limiting condition, significantly increasing the yield in the presence of glucose. Two-stage fed-batch fermentation of the final strain in a 5 L bioreactor produced 84 g/L L-valine with a yield and productivity of 0.41 g/g glucose and 2.33 g/L/h, respectively. To the best of our knowledge, this is the highest L-valine titer and yield ever reported in E. coli. The systems metabolic engineering strategy described here will be useful for future engineering of E. coli strains for the industrial production of L-valine and related products.     

Monovalent Cation Activation of Plant Pyruvate Dehydrogenase Kinase

The pyruvate dehydrogenase kinase-catalyzed inactivation of the pyruvate dehydrogenase complex was studied using dialyzed, soluble proteins from mitochondria purified from green leaf tissue of Pisum sativum L. seedlings. At subsaturating ATP concentrations, K+ or NH4+, but not Na+, stimulated the pyruvate dehydrogenase kinase by lowering the Km(ATP). Micromolar concentrations of NH4+ were required to produce the same effect as millimolar concentrations of K+. This is apparent from the observations that the activation constant (Kact) for NH4+ was 0.1 mM, whereas the Kact(K+) was 0.7 mM. Maximal pyruvate dehydrogenase kinase velocities attained with NH4+ were higher than those with K+, and, therefore, NH4+ was able to stimulate PDH kinase further in the presence of saturating K+. This result supports our conclusion that photorespiratory NH4+ production in plant mitochondria may be involved in regulating the entry of carbon into the Krebs cycle by way of the pyruvate dehydrogenase complex.     

K+ and NH4(+) modulate gill (Na+, K+)-ATPase activity in the blue crab, Callinectes ornatus: fine tuning of ammonia excretion

To better comprehend the mechanisms of ionic regulation, we investigate the modulation by Na+, K+, NH4(+) and ATP of the (Na+, K+)-ATPase in a microsomal fraction from Callinectes ornatus gills. ATP hydrolysis obeyed Michaelis-Menten kinetics with KM=0.61+/-0.03 mmol L(-1) and maximal rate of V=116.3+/-5.4 U mg(-1). Stimulation by Na+ (V=110.6+/-6.1 U mg(-1); K0.5=6.3+/-0.2 mmol L(-1)), Mg2+ (V=111.0+/-4.7 U mg(-1); K0.5=0.53+/-0.03 mmol L(-1)), NH4(+) (V=173.3+/-6.9 U mg(-1); K0.5=5.4+/-0.2 mmol L(-1)) and K+ (V=116.0+/-4.9 U mg(-1); K0.5=1.5+/-0.1 mmol L(-1)) followed a single saturation curve, although revealing site-site interactions. In the absence of NH4(+), ouabain (K(I)=74.5+/-1.2 micromol L(-1)) and orthovanadate inhibited ATPase activity by up to 87%; the inhibition patterns suggest the presence of F0F1 and K+-ATPases but not Na+-, V- or Ca2+-ATPase as contaminants. (Na+, K+)-ATPase activity was synergistically modulated by K+ and NH4(+). At 10 mmol L(-1) K+, increasing NH4(+) concentrations stimulated maximum activity to V=185.9+/-7.4 U mg(-1). However, at saturating NH4(+) (50 mmol L(-1)), increasing K+ concentrations did not stimulate activity further. Our findings provide evidence that the C. ornatus gill (Na+, K+)-ATPase may be particularly well suited for extremely efficient active NH4(+) excretion. At elevated NH4(+) concentrations, the enzyme is fully active, regardless of hemolymph K+ concentration, and K+ cannot displace NH4(+) from its exclusive binding sites. Further, the binding of NH4(+) to its specific sites induces an increase in enzyme apparent affinity for K+, which may contribute to maintaining K+ transport, assuring that exposure to elevated ammonia concentrations does not lead to a decrease in intracellular potassium levels. This is the first report of modulation by ammonium ions of C. ornatus gill (Na+, K+)-ATPase, and should further our understanding of NH4(+) excretion in benthic crabs.     

Purification and catalytic properties of L-valine dehydrogenase from Streptomyces cinnamonensis.

NAD+-dependent L-valine dehydrogenase was purified 180-fold from Streptomyces cinnamonensis, and to homogeneity, as judged by gel electrophoresis. The enzyme has an Mr of 88,000, and appears to be composed of subunits of Mr 41,200. The enzyme catalyses the oxidative deamination of L-valine, L-leucine, L-2-aminobutyric acid, L-norvaline and L-isoleucine, as well as the reductive amination of their 2-oxo analogues. The enzyme requires NAD+ as the only cofactor, which cannot be replaced by NADP+. The enzyme activity is significantly decreased by thiol-reactive reagents, although purine and pyrimidine bases, and nucleotides, do not affect activity. Initial-velocity and product-inhibition studies show that the reductive amination proceeds through a sequential ordered ternary-binary mechanism; NADH binds to the enzyme first, followed by 2-oxoisovalerate and NH3, and valine is released first, followed by NAD+. The Michaelis constants are as follows; L-valine, 1.3 mM; NAD+, 0.18 mM; NADH, 74 microM; 2-oxoisovalerate, 0.81 mM; and NH3, 55 mM. The pro-S hydrogen at C-4' of NADH is transferred to the substrate; the enzyme is B-stereospecific. It is proposed that the enzyme catalyses the first step of valine catabolism in this organism.     

Isolation and characterization of valine dehydrogenase from Streptomyces aureofaciens.

Valine dehydrogenase was purified to homogeneity from the crude extracts of Streptomyces aureofaciens. The molecular weight of the native enzyme was 116,000 by equilibrium ultracentrifugation and 118,000 by size exclusion high-performance liquid chromatography. The enzyme was composed of four subunits with molecular weights of 29,000. The isoelectric point was 5.1. The enzyme required NAD+ as a cofactor, which could not be replaced by NADP+. Sulfhydryl reagents inhibited the enzyme activity. The pH optimum was 10.7 for oxidative deamination of L-valine and 9.0 for reductive amination of alpha-ketoisovalerate. The Michaelis constants were 2.5 mM for L-valine and 0.10 mM for NAD+. For reductive amination the Km values were 1.25 mM for alpha-ketoisovalerate, 0.023 mM for NADH, and 18.2 mM for NH4Cl.     

Valine dehydrogenase from Streptomyces fradiae: purification and properties

Valine dehydrogenase (VDH) was purified to homogeneity from cell-free extract of Streptomyces fradiae, which produces tylosin. The enzyme was purified 1508-fold in a 17.7% yield using a combination of hydrophobic chromatography and ion-exchange fast protein liquid chromatography. The Mr of the native enzyme was determined to be 218,000 and 215,000, by equilibrium ultracentrifugation and size-exclusion high-performance liquid chromatography, respectively. The enzyme is composed of 12 subunits of Mr 18,000. Using analytical isoelectric focusing the isoelectric point of VDH was found to be 4.7. Oxidative deamination of L-valine was optimal at pH 10.6. Reductive amination of 2-oxoisovalerate was optimal at pH 8.8. The Michaelis constants (Km) were 1 mM for L-valine and 0.029 mM for NAD+. Km values for reductive amination were 0.80 mM for 2-oxoisovalerate, 0.050 mM for NADH and 22 mM for NH4+.     

金属离子对粪产碱杆菌C16的脱氮和亚硝酸盐积累的影响

【目的】研究不同金属离子对异养氨氧化细菌C16的生长和脱氮性能影响,探讨适于C16生长和脱氮的金属离子及其浓度。【方法】实验选用Mg2+、Mn2+、Fe2+、Cu2+、Zn2+5种金属离子,对C16的生长﹑脱氮性能﹑亚硝酸盐氮积累以及相关酶活性进行研究。【结果】Mg2+明显促进C16的生长和NH4+-N氧化速率;较高浓度Mn2+使得C16无法生长;原培养基中缺少Fe2+会抑制C16的生长和NH4+-N氧化速率;在原培养基中加入0.1 mmol/L的Cu2+对C16的生长和脱氮具有一定的促进作用,Cu2+使得培养基中基本无NO2--N和NH2OH的积累;不同浓度的Zn2+对C16的生长和氨氮去除有抑制作用。酶活实验结果显示,0.1 mmol/L Mg2+促进了羟胺氧化还原酶(HAO)的活性;0.1 mmol/L Cu2+促进了硝酸盐还原酶(Nar)和亚硝酸盐还原酶(Nir)的活性。【结论】Mg2+是C16生长和脱氮过程中的一种重要金属离子;加入Cu2+可避免过量亚硝酸盐积累。