Fed-batch culture ofAeromonas hydrophila for the production of poly(3-hydroxubutyrate-co-3-hydroxyhexanoate) using two carbon sources

To produce polyhydroxyalkanoate (PHA) copolymer which consists of 3-hydroxy-butyrate (3HB) and 3-hydroxyhexanoate (3HHx) by cultivation ofAeromonas hydrophila, fed-batch cultures were done under several nutrient limiting conditions. With the results from flask cultures, fed-batch cultures were carried out to produce large amounts of PHA. In the fed-batch culture, firstly glucose was fed to grow cell, and then, oleic acid fed to stimulate PHA in the cell. The final cell concentration, PHA content, PHA concentration, and 3-hydroxy-hexanoate fraction in 38 hr were 48.9 g/L, 15.05 wt%, 7.36 g/L and 12.2 wt%, respectively, resulting in the productivity of 0.19 g/L-h under phosphate-limiting condition.     

几种营养物质对烟草细胞生长和CoQ10含量的影响

研究了蔗糖、KH₂PO₄、NH₄NO₃比对烟草细胞生长和CoQ₁₀量的影响,结果表明,当蔗糖浓度为30g/L时,CoQ₁₀总量最高,此时细胞产量、CoQ₁₀含量和总量分别为19.8g/L、414.7μg/g(dwt)、8212μg/L。在上述蔗糖浓度下,当KH₂PO₄起始浓度为340mg/L、NH₄NO₃为12时,细胞产量、CoQ₁₀含量和总量分别最高,高于此比例时有利于CoQ₁₀形成 ,但不利于细胞生长。     

Production of poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) by high-cell-density cultivation of Aeromonas hydrophila

The newly screened Aeromonas hydrophila produces copolymer consisting of 3-hydroxybutyrate (3HB) and 3-hydroxyhexanoate (3HHx). The characteristics of cell growth and polymer accumulation were examined using various carbon sources. P(3HB-co-3HHx) was produced from lauric acid and oleic acid only. P(3HB-co-3HHx) content can be increased by limitation of phosphorus. A maximal P(3HB-co-3HHx) content of 28.8 wt% could be obtained in flask culture. By applying the optimally designed nutrient feeding strategy, cell dry weight, P(3HB-co-3HHx) content, and 3HHx fraction obtained over the course of 43 h were 95.7 g/L, 45.2 wt%, and 17 mol%, respectively, resulting in a productivity of 1.01 g polyhydroxyalkanoate (PHA)/L. h.     

Production of poly(3-hydroxybutyrate) by high cell density fed-batch culture of Alcaligenes eutrophus with phospate limitation

High cell density fed-batch fermentation of Alcaligenes eutrophus was carried out for the production of poly(3-hydroxybutyrate) (PHB) in a 60-L fermentor. During the fermentation, pH was controlled with NH(4)OH solution and PHB accumulation was induced by phosphate limitation instead of nitrogen limitation. The glucose feeding was controlled by monitoring dissolved oxygen (DO) concentration and glucose concentration in the culture broth. The glucose concentration fluctuated within the range of 0-20 g/L. We have investigated the effect of initial phosphate concentration on the PHB production when the initial volume was fixed. Using an initial phosphate concentration of 5.5 g/L, the fed-batch fermentation resulted in a final cell concentration of 281 g/L, a PHB concentration of 232 g/L, and a PHB productivity of 3.14 g/L . h, which are the highest values ever reported to date. In this case, PHB content, cell yield from glucose, and PHB yield from glucose were 80, 0.46, and 0.38% (w/w), respectively. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 28-32, 1997.     

High cell density cultivation ofPseudomonas oleovorans for the production of poly(3-hydroxyalkanoates)

Fed-batch culture ofPseudomonas oleovorans was carried out for the production of medium-chain-length polyhydroxyalkanoates (MCL-PHAs) using octanoate as a carbon source. Octanoate and the salt solution containing ammonium sulfate and magnesium sulfate were intermittently fed in the course of fermentation. Cell mass and PHA concentrations of 42.8 and 16.8 g/L, respectively, could be obtained in 40 h. The PHA content and the PHA productivity were 39.2% and 0.42 g PHA/L-h, respectively. The yields of cell mass and PHA were 0.71 g dry cell mass/goctanoate and 0.28 g PHA/g octanoate, respectively. Therefore, octanoate can be used for the production of MCL-PHAs to a high, concentration with high productvity.     

碎米荠及富硒产品中无机硒提取方法的建立

采用不同浓度的HCl、NaOH、KH_2PO_4、NaHCO_3、KCl、流动相及超纯水作浸提液提取富硒产品中的无机硒后,用高效液相色谱-原子荧光光谱(HPLC-AFS)联用仪测定Se(IV)和Se(VI),并对浸提时间、浸提温度、振荡频率、液料比等条件进行系统研究,建立了富硒植物碎米荠及富硒产品中无机硒的提取方法:无机硒的最佳提取剂为0.1mol/L KH_2PO_4溶液,提取方法为:称取样品0.10g于离心管中,加入0.1mol/L KH_2PO_4溶液至3mL,于70℃、1 500r/min条件下振荡提取30min,以3 000r/min转速离心10min,0.45μm滤膜过滤后上机测定,样品加标回收率为86.14%~117.60%,Se(IV)和Se(VI)均能定性定量检测,为富硒产品中无机硒测定方法标准的制定奠定了基础。     

休哈塔假丝酵母HDYXHT-01利用木糖生产乙醇的发酵工艺优化

采用Plackett-Burman (PB) 方法和中心组合设计 (Ccentral composit design,CCD) 对休哈塔假丝酵母Candida shehataeHDYXHT-01利用木糖发酵生产乙醇的工艺进行优化。PB试验设计与分析结果表明：硫酸铵、磷酸二氢钾、酵母粉和接种量是影响木糖乙醇发酵的4个关键因素,以乙醇产量为响应目标,采用CCD和响应面分析法 (Response surface methodology,RSM),确定了木糖乙醇发酵的最佳工艺为：硫酸铵1.73 g/L、磷酸二氢钾3.56 g/L、酵母粉2.62 g/L和接种量5.66％,其他发酵条件为：木糖80 g/L,MgSO4·7H2O 0.1 g/L,pH 5.0,培养温度30 ℃,装液量100 mL/250 mL,摇床转速140 r/min,发酵时间48 h,在该条件下发酵液中乙醇产量可以达到26.18 g/L,比未优化前提高了1.15倍。     

Production of polyhydroxyalkanoates by <Emphasis Type="Italic">Azotobacter vinelandii</Emphasis> UWD using swine wastewater: Effect of supplementing glucose,yeast extract,and inorganic salts

This study examined the effect of adding glucose, yeast extract, and inorganic salts to swine wastewater (SWW) in a batch culture on the production of a biodegradable plastic, polyhydroxyalkanoate (PHA). A bacterial strain, Azotobacter vinelandii UWD, was used to produce PHA without limiting the non-carbon nutrients. The addition of glucose (30 g/L) to the SWW medium increased the level of cell growth (4.4∼7.0 times) and PHA production (3.8∼8.5 times) depending upon the dilution of SWW. A 50% dilution of SWW was found to be optimal considering the dry cell weight (9.40 g/L), PHA content (58 wt%), and hydroxyvalerate (HV) mol fraction in the PHA (4.3 mol%). A 75% SWW medium was more advantageous for producing PHA with a higher HV fraction (7.1 mol%) at the expense of losing 22% of PHA production. The undiluted SWW medium produced less than one third of the PHA compared with the 50% SWW medium, but the HV fraction was the highest (10.8 mol%). Regarding the effect of the glucose concentration, at 20 g/L glucose, the dry cell weight and level of PHA production increased to 9.34 g/L (0.63 g PHA/g dry cell weight) and 5.90 g/L, respectively. At 50 g/L glucose, there was no significant increase in PHA production. For the glucose-supplemented (30 g/L) 50% SWW medium, the addition of a nitrogen source (1 g/L of yeast extract) did not increase the level of cell growth or PHA production because the C:N ratio (23:1) was already close to the optimal value (22:1). Better aeration increased the productivity of PHA. External nitrogen supplements (1 g/L of yeast extract) and other essential mineral salts was not necessary for bacterial growth because they were contained in the SWW. These results suggest that SWW is an excellent feedstock for producing larger amounts of the value-added material, PHA, if it is combined with carbohydrate-rich organic waste.     

Production of poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) by Ralstonia eutropha in high cell density palm oil fermentations

Improved production costs will accelerate commercialization of polyhydroxyalkanoate (PHA) polymer and PHA-based products. Plant oils are considered favorable feedstocks, due to their high carbon content and relatively low price compared to sugars and other refined carbon feedstocks. Different PHA production strategies were compared using a recombinant strain of Ralstonia eutropha that produces high amounts of P(HB-co-HHx) when grown on plant oils. This R. eutropha strain was grown to high cell densities using batch, extended batch, and fed batch fermentation strategies, in which PHA accumulation was triggered by nitrogen limitation. While extended batch culture produced more biomass and PHA than batch culture, fed batch cultivation was shown to produce the highest levels of biomass and PHA. The highest titer achieved was over 139 g/L cell dry weight (CDW) of biomass with 74% of CDW as PHA containing 19 mol% HHx. Our data suggest that the fermentation process is scalable with a space time yield (STY) better than 1 g PHA/L/h. The achieved biomass concentration and PHA yield are among the highest reported for the fermentation of recombinant R. eutropha strains producing P(HB-co-HHx).     

拉曼被孢霉产γ-亚麻酸的发酵条件优化

对影响发酵产γ-亚麻酸的因素（温度、N源、P源等）进行单因素考察。结果发现,各因素对拉曼被孢霉（Mortierella ramanniana NBRC 8187）产γ-亚麻酸均有不同程度的影响。通过正交试验设计对KH2PO4、NaNO3、酵母膏和温度进行了L9（34）试验设计,以γ-亚麻酸产量为优化目标,直观分析得出影响产量的因素大小顺序为酵母膏、温度、KH2PO4、NaNO3,最终确定最佳的培养条件：酵母膏5 g/L、25℃、KH2PO41 g/L、NaNO33 g/L。在此条件下,检测得出在第5天γ-亚麻酸产量达到0.968 g/L,相比优化前（0.583 g/L）提高了66%。     

Utilization of UF-permeate for production of beta-galactosidase by lactic acid bacteria

Four lactobacilli strains (Lactobacillus bulgaricus, Lactobacillus acidophilus, Lactobacilus casei and Lactobacillus reuteri) were grown in MRS broth and three lactococci strains (Streptococcus thermophilus, Lactococcus lactis subsp. Lactis and Lactococcus lactis subsp. lactis biovar. diacetilactis) were grown in M17 broth. L. reuteri and S. thermophilus were chosen on the basis of the best mean beta-galactosidase activity of 10.44 and 10.01 U/ml respectively, for further studies on permeate-based medium. The maximum production of beta-galactosidase by L. reuteri was achieved at lactose concentration of 6%, initial pH 5.0-7.5, ammonium phosphate as nitrogen source at a concentration of 0.66 g N/L and incubation temperature at 30 degrees C/24 hrs to give 6.31 U/ml. While in case of S. thermophilus, maximum beta-galactosidase production was achieved at 10% lactose concentration of permeate medium, supplemented with phosphate buffer ratio of 0.5:0.5 (KH2PO4:K2HPO4, g/L), at initial pH 6.0-6.5, ammonium phosphate (0.66g N/L) as nitrogen source and incubation temperature 35 degrees C for 24 hrs to give 7.85 U/ml.     

二十碳五烯酸的菌种选育及发酵条件

利用含亚麻子油的斜面培养基连续传代和逐渐降低培养温度,诱导筛选的方法,从大量丝状真菌中选育到一株产二十碳五烯酸（all－cis－5、8、11、14、17－eicosopnthenoicacid）较高的被孢霉菌（Motierellasp．）SM481。研究得到最适培养基及最适培养条件。在最适培养及产二十碳五烯酸条件下,细胞干重和二十碳五烯酸产量分别为28．8g／L和0.127g／L。     

High cell density cultivation of Pseudomonas oleovorans: growth and production of poly (3-hydroxyalkanoates) in two-liquid phase batch and fed-batch systems

Pseudomonas oleovorans is able to accumulate poly(3-hydroxyalkanoates) (PHAs) under conditions of excess n-alkanes, which serve as sole energy and carbon source, and limitation of an essential nutrient such as ammonium. In this study we aimed at an efficient production of these PHAs by growing P. oleovorans to high cell densities in fed-batch cultures.To examine the efficiency of our reactor system, P. oleovorans was first grown in batch cultures using n-octane as growth substrate and ammonia water for pH regulation to prevent ammonium limiting conditions. When cell growth ceased due to oxygen limiting conditions, a maximum cell density of 27 g .L(-1) dry weight was obtained. When the growth temperature was decreased from the optimal temperature of 30 degrees -18 degrees C, cell growth continued to a final cell density of 35 g . L(-1) due to a lower oxygen demand of the cells at this lower incubation temperature.To quantify mass transfer rates in our reactor system, the volumetric oxygen transfer coefficient (k(L)a) was determined during growth of P. oleovorans on n-octane. Since the stirrer speed and airflow were increased during growth of the organism, the k(L)a also increased, reaching a constant value of 0.49 s(-1) at maximum airflow and stirrer speed of 2 L . min(-1) and 2500 rpm, respectively. This k(L)a value suggests that oxygen transfer is very efficient in our stirred tank reactor.Using these conditions of high oxygen transfer rates, PHA production by P. oleovorans in fed-batch cultures was studied. The cells were first grown batchwise to a density of 6 g . L(-1), after which a nutrient feed, consisting of (NH(4))(2)SO(4) and MgSO(4), was started. The limiting nutrient ammonium was added at a constant rate of 0.23 g NH(4) (+) per hour, and when after 38 h the feed was stopped, a biomass concentration of 37.1 g . L(-1) was obtained. The Cellular PHA content was 33% (w/w), which is equal to a final PHA yield of 12.1 g . L(-1) and an overall PHA productivity of 0.25 g PHA produced per liter medium per hour. (c) 1993 John Wiley & Sons, Inc.     

发酵法生产丁二酸的化学合成培养基的筛选

以产琥珀酸放线杆菌Actinobacillus succinogenes NJ113 为出发菌株,针对该菌株筛选出含有关键生长因子的化学合成培养基,其关键因子为谷氨酸（Glu）、蛋氨酸（Met）和生物素（VH）和烟酸（VPP）。结合原发酵培养基中的磷酸缓冲盐成分,最终得到的化学合成培养基配方（g/L）： CH3COONa 1.36,NaCl 1.0,MgCl2 0.2,CaCl2 0.2,Na2HPO4 0.31,NaH2PO4 1.6, KH2PO4 3,NH4HCO3 1.57,Glu 0.87,Met 0.11,VH 0.010,VPP 0.025。在3 L发酵罐上进行验证实验,50 g/L初始葡萄糖发酵70 h,丁二酸的质量浓度为45.2 g/L,丁二酸收率达到90.4%。与之前的半合成培养基发酵制备丁二酸相比,丁二酸的收率提高了25.2%,副产物也有很大幅度的减少。     

Industrial scale production of poly(3-hydroxybutyrate-co-3-hydroxyhexanoate)

Large scale production of poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) [P(3HB-co-3HHx)] by Aeromonas hydrophila 4AK4 was examined in a 20,000 l fermentor. Cells were first grown using glucose as a carbon source, and polyhydroxyalkanoate (PHA) biosynthesis was triggered by the addition of lauric acid under conditions of limited nitrogen or phosphorus. When cells first grown in a medium containing 50 g glucose l(-1) were further cultivated after the addition of 50 g lauric acid l(-1) under phosphorus limitation, a final cell concentration, PHA concentration and PHA content of 50 g l(-1), 25 g l(-1), and 50 wt%, respectively, were obtained in 46 h, equivalent to PHA productivity of 0.54 g l(-1)t h(-1). The copolymer produced was found to be a random copolymer, and the 3HHx fraction was 11 mol%.     

响应面法优化枯草芽孢杆菌产脂肪酶的合成培养基

对枯草芽孢杆菌(Bacillus subtilis)CICC20034利用合成培养基液体发酵产脂肪酶的条件进行了优化。首先采用单因子实验筛选出最适诱导剂为三丁酸甘油酯,氮源为尿素,碳源为葡萄糖,无机盐为MgSO4。在此基础上,利用Plackett-Burman设计对影响产酶因素的效应进行评价,筛选出具有显著效应的三丁酸甘油酯、尿素、KH2PO4和培养基起始pH值4个最显著的因素。用最陡爬坡路径逼近最大产酶区域后,利用响应面中心组合设计对显著因素进行优化,获得最适合成培养基组分为:葡萄糖8g/L,尿素8.57g/L,三丁酸甘油酯2.62%,KH2PO42.59g/L,MgSO4.7H2O0.5g/L,TritonX-1000.5g/L,pH9.47。优化后的B.subtilis CICC 20034胞外脂肪酶活力达0.483U/ml,比初始酶活力0.072U/ml提高了6.7倍。     

隐甲藻深层培养产生二十碳五烯酸的研究

二十碳五烯酸 (Ｃ2 0 :5 ,Ｅｉｃｏｓａｐｅｎｔａｅｎｏｉｃａｃｉｄ ,简称ＥＰＡ)是一种重要的ω 3系列人体必需多不饱和脂肪酸 (Ｐｏｌｙｕｎ ｓａｔｕｒａｔｅｄｆａｔｔｙａｃｉｄｓ,ＰＵＦＡ) [1～ 2 ] 。自从Ｄｙｅｒｂｅｒｇｅ等人报道了二十碳五烯酸对防止和治疗血栓、关节硬化、抗炎症、抗癌、促进脑组织发育等方面具有明显效果以来 ,人们对它的营养和医药价值及生产方法进行了广泛的研究[3～ 6] 。目前 ,二十碳五烯酸主要来源于深海鱼油 ,但其产量不稳定 ,纯化工艺复杂且含有难以消除的鱼腥味 ,难以满足市场的需求。由于二十碳五…     

被孢霉菌发酵产生花生四烯酸的研究

研究了温度、培养基初始pH、碳源、氮源对被孢霉(Mortierella sp.)产生花生四烯酸的影响。正交试验结果表明,Mortierella sp.M10最佳培养基组成为(g/L):葡萄糖100,酵母膏10,KNO_3 4.0,KH_2PO_4 2.0,CaCl_2·2H_2O 0.1,MgSO_4·7H_2O 0.5,FeCl_3·6H_2O0.015,ZnSO_4·7H_2O 0.0075,CuSO_4·5H_2O 0.0005。采用最佳培养基及发酵条件,细胞干重和花生四烯酸产量分别为33.51g/L和0.827g/L。同时对摇瓶发酵过程进行了分析。     

桑木层孔菌液体培养条件的研究

对桑木层孔菌(Phellinus mori)液体发酵条件进行了研究,以生物量和胞外多糖为指标,通过L16(45)和L9(34)正交表进行了两次正交试验,筛选出桑木层孔菌最适液体培养条件为:麦芽糖30 g/L,酵母浸粉和蛋白胨15 g/L(质量比2 1),KH2PO4和CaCl25.5 g/L(质量比1 1),初始pH6.0;通过单因素试验筛选出最适装液量为120 mL/250 mL,最适接种量为10%。在此条件下液体发酵培养7 d后,桑木层孔菌生物量达到23.375 g/L,胞外多糖产量达到3.993 g/L。