Mn2+对必特螺旋霉素产生菌代谢和必特螺旋霉素合成的影响

通过在必特螺旋霉素产生菌WSJ1195发酵过程中添加金属离子Mn²⁺发现：发酵前期（24h左右）添加Mn²⁺可以明显提高生物效价,加入的Mn2+浓度以5mmol/L为最佳。实验显示添加Mn2+后发酵液pH逐渐下降,整个产素期间 pH一直低于对照;与对照相比添加Mn²⁺摇瓶菌体浓度也较低。通过研究必特螺旋霉素发酵过程有机酸的变化趋势发现：24h添加5mmol/L Mn2+后发酵过程中有机酸含量已经发生变化,其中丙酸浓度的增长最为显著,84h时其浓度为对照的6倍。通过丙酸盐的添加实验证实了发酵前期添加Mn²⁺可以促进产物合成的原因之一是促进了丙酸等前体酸的合成,丰富了大环内酯合成的前体库。     

铵离子对必特螺旋霉素组分生物合成的调控作用

通过考察铵离子浓度对必特螺旋霉素组分的影响,证实低浓度铵离子的培养条件可以有效提高必特螺旋霉素中异戊酰螺旋霉素Ⅲ的比例。在此基础上进一步测定了高铵(62·5mmol/L)和低铵(2·5mmol/L)培养条件下的糖、铵离子、相关有机酸、缬氨酸脱氢酶酶活等中间代谢数据,结果表明高浓度铵离子培养条件下,必特螺旋霉素产生菌中亮氨酸分解代谢途径的关键酶——缬氨酸脱氢酶的活性低于低铵对照试验,造成异戊酰螺旋霉素合成过程中酰基转移反应的底物——异戊酰CoA的相对不足,从而导致异戊酰螺旋霉素组分的降低。大幅度降低铵离子浓度至2·5mmol/L,使异戊酰螺旋霉素Ⅲ的比例从5·43%提高至28·59%。但氮源的不足影响了必特螺旋霉素的产量,低铵条件下的效价为107μg/mL,相对高铵条件下降了14·4%。在低铵培养条件的基础上添加亮氨酸,可以进一步改善必特螺旋霉素的组分,异戊酰螺旋霉素Ⅲ的比例增至37·84%。     

高效液相色谱法测定必特螺旋霉素发酵液中有机酸

必特螺旋霉素是运用基因工程技术获得的工程茵产生的一组以异戊酰螺旋霉素为主要成分的多组分新型抗生素,其前体为乙酸、丙酸、丁酸和异戊酸等有机酸。本研究利用高效液相色谱法以0．01mol／L磷酸缓冲液（pH2．3）和甲醇为流动相,分别在反相C8（α-酮戊二酸、乙酸、柠檬酸、琥珀酸、丙酸）和C18（丁酸、异戊酸）柱上定量测定了必特螺旋霉素前体酸和三羧酸循环相关有机酸。所建立的测定方法的相对标准偏差为0．10％～0．42％,回收率为93．19％～102．08％。     

外源有机酸对红树林内生真菌发酵生产1403C的影响

本文主要研究了外源有机酸对红树林内生真菌No.1403发酵生产1403C的影响,并且分别在摇瓶和5 L反应器进行柠檬酸(钠)的间歇性补加实验。研究发现在新培养基条件下添加丙二酸前体对1403C产量无促进作用。摇瓶发酵前期添加的柠檬酸对1403C合成代谢有轻微抑制效应,中后期补加的柠檬酸很可能被用于维持菌体的初级代谢。而反应器发酵的1403C产量比对照产量提高8.6%,达到0.81 g/L;碳饥饿时期,在pH7.0且菌体稳定存在条件下,添加外源柠檬酸可促进1403C的合成。     

3-羟基丙酸分批发酵过程中的pH控制策略研究

本文利用重组大肠杆菌以甘油为底物发酵合成3．羟基丙酸,考察了不同pH对3．羟基丙酸产量及菌体生长的影响,发现在pH6．5条件下,细胞比生长速率达到最大值,延迟期也相对较短;而pH7．0有利于3-羟基丙酸的合成,控制pH7．0可以使3-羟基丙酸产量达到7．39g／L。基于不同pH条件下对细胞比生长速率和3-羟基丙酸比生成速率的分析,提出3．羟基丙酸分批发酵过程中的pH控制策略,即在发酵过程前5h将pH控制在6．5,5h～15h控制pH为7．0,此时有利于细胞生长;而后在15h-25h控制pH为7．5,25h后控制pH为7．0,从而使细胞具有较高的3．羟基丙酸比合成速率。在此控制策略下经过34h发酵3-羟基丙酸的终产量达到8．76g／L,比pH7．0条件下的3-羟基丙酸产量提高了18．54％。     

螺旋霉素生物合成中的分子、基因及发酵调控技术

螺旋霉素(spiramycin,SPM)是十六元环大环内酯类抗生素,在临床上占有重要的地位,其产生菌为生二素链霉菌(S.ambofaciens)。螺旋霉素由福洛氨糖(forosamine)、碳霉氨糖(mycaminose)和碳霉糖(mycarose)3个部分组成。简要介绍了螺旋霉素的理化性质和药理作用,以及生物合成途径与发酵工艺等方面的研究状况,根据螺旋霉素生物合成途径,分别从分子水平、基因水平及发酵工艺等3个方面对通过添加前体或对前体有利的物质及定向过量表达某些重要基因等提高螺旋霉素产量的技术进行了简要概述。     

丙酸积累对薛氏丙酸杆菌生长及产酸的影响*

报道丙酸积累对维生素B12产生菌Propionibacterium shermanii生长及丙酸产生的影响,在初糖浓度6％,pH6.5的批次发酵条件下,测定了该菌的耗糖、产酸和茵体生长曲线。发酵24h后,培养基中添加1％、3％和6％的丙酸,发酵结束时菌体干重只有对照的75．2％、65．4％和52.9％,产酸是对照的79.3％、69．2％和39．3％。加入6％的丙酸不能完全抑制耗糖和产酸。部分解除丙酸抑制可使菌体干重增加60％。     

弱酸（盐）对植物乳杆菌耐酸性的影响

目的探讨弱酸（盐）对植物乳杆菌耐酸性的影响。方法在植物乳杆菌发酵过程中,添加50mmol／L乙酸、10mmol／L丙酸、20mmol／L正丁酸、50mmol／L乙酸钾及2mmol/L柠檬酸钾。结果添加剂量均可使植物乳杆菌耐酸性得到较大的提高,在pH2、37℃下90min,细胞残存率都较对照提高80倍以上,尤以乙酸（盐）、正丁酸为好,而三聚磷酸钾则对细胞耐酸性提高具有较小的作用,细胞残存率较对照约提高5倍。结论在发酵培养基中添加弱酸（乙酸、丙酸及正丁酸）或弱酸盐（乙酸钾、柠檬酸钾及三聚磷酸钾）均可不同程度地提高植物乳扦菌细胞耐酸性。     

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。     

高产表面活性素的重组枯草芽孢杆菌构建及培养优化

表面活性素是一种新型生物表面活性剂,因其具有良好的表面活性、可生物降解及抗菌活性,在石油开采、医药、农业和食品化妆品等领域具有广阔的应用前景。高产表面活性素菌株的获得和发酵过程优化是其商业化生产的关键。文中考察了脂肪酸合成途径对表面活性素合成的影响,强化脂肪酸生物合成关键基因以及该途径全部基因分别构建了高产表面活性素枯草芽孢杆菌Bacillus subtilis THBS-2和THBS-8,并对发酵过程中氨基酸种类及添加量、诱导剂异丙基-β-D-硫代半乳糖苷 (IPTG) 添加时间和添加量等条件对产物合成的影响进行考察,获得优化的两阶段前体添加方案：发酵3 h,加入IPTG和L-亮氨酸,使其终浓度分别为1.25 mmol/L、5 g/L;发酵24 h,添加L-亮氨酸 (终浓度5 g/L) 和浓缩培养基5 mL。优化条件下,枯草芽孢杆菌THBS-2摇瓶发酵48 h,表面活性素产量高达24 g/L;30 L发酵罐中发酵68 h,产物产量最高达到34 g/L。研究结果为表面活性素的工业化生产及应用奠定基础。     

产酸丙酸杆菌生长特性及5L罐发酵动力学研究

论文在摇瓶水平对产酸丙酸杆菌基本生长特性（温度、pH、摇床转速、接种量、种龄等）、碳源、氮源利用情况、产物抑制及5 L罐发酵动力学进行了研究。结果表明,该菌在32℃,初始pH 6．5,摇床转速150 r/min,接种24 h的种子液,接种量为5％条件下,产酸丙酸杆菌生长及产酸水平达最高值;该菌可利用碳源十分广泛,但对氮源要求比较高,只可利用有机氮源;在不同初始葡萄糖浓度下,产酸丙酸杆菌生长及产酸水平差异不大,无明显底物抑制现象;在2g/L的初始丙酸盐浓度下,该菌生长受到明显抑制;在5L发酵罐中,初始葡萄糖浓度为58．8 g/L,发酵72 h,葡萄糖消耗完全,丙酸终浓度达22．4 g/L,丙酸得率和产率分别达0．381 g/g和0．295 g/（L·h）,丙酸占总酸比例达72．10％。     

利用纤维床反应器固定化发酵生产丙酸

构建了一种纤维床反应器(FBB), 并将其应用于丙酸的生产。将棉纤维绕成桶状, 固定于反应器中, 即可用于丙酸固定化发酵。以40 g/L的葡萄糖为碳源, 与游离细胞相比, 利用FBB生产丙酸, 丙酸产量由14.58 g/L提高至20.41 g/L, 发酵时间由120 h缩短至60 h。研究了不同糖浓度条件下FBB生产丙酸情况, 并将补料策略应用于丙酸发酵中。结果表明: 补料发酵能够有效改善Propionibacterium freudenreichii CCTCC M207015在高糖条件下丙酸对葡萄糖转化率较低、副产物较多的问题。经补料发酵280 h, 丙酸产量达45.91 g/L, 丙酸质量约占有机酸总质量比例为72.31%。     

利用纤维床反应器固定化发酵生产丙酸

构建了一种纤维床反应器(FBB), 并将其应用于丙酸的生产。将棉纤维绕成桶状, 固定于反应器中, 即可用于丙酸固定化发酵。以40 g/L的葡萄糖为碳源, 与游离细胞相比, 利用FBB生产丙酸, 丙酸产量由14.58 g/L提高至20.41 g/L, 发酵时间由120 h缩短至60 h。研究了不同糖浓度条件下FBB生产丙酸情况, 并将补料策略应用于丙酸发酵中。结果表明: 补料发酵能够有效改善Propionibacterium freudenreichii CCTCC M207015在高糖条件下丙酸对葡萄糖转化率较低、副产物较多的问题。经补料发酵280 h, 丙酸产量达45.91 g/L, 丙酸质量约占有机酸总质量比例为72.31%。     

Propionic acid fermentation of lactose by Propionibacterium acidipropionici: effects of pH

Batch propionic acid fermentation of lactose by Propionibacterium acidipropionici were studied at various pH values ranging from 4.5 to 7.12. The optimum pH range for cell growth was between 6.0 and 7.1, where the specific growth rate was approximately 0.23 h(-1). The specific growth rate decreased with the pH in the acids have been identified as the two major fermentation products from lactose. The production of propionic acid was both growth and nongrowth associated, while acetic acid formation was closely associated with cell growth. The propionic acid yield increased with decreasing pH; It changed from approximately 33% (w/w) at pH 6.1-7.1 to approximately 63% at pH 4.5-5.0. In contrast, the acetic acid yield was not significantly affected by the pH; it remained within the range of 9%-12% at all pH values. Significant amounts of succinic and pyruvic acids were also formed during propionic acid fermentation of lactose. However, pyruvic acid was reconsumed and disappeared toward the end of the fermentation. The succinic acid yield generally decreased with the pH, from a high value of 17% at pH 7.0 to a low 8% at pH 5.0 Effects of growth nutrients present in yeast ex-tract on the fermentation were also studied. In general, the same trend of pH effects was found for fermentations with media containing 5 to 10 g/L yeast extract. However, More growth nutrients would be required for fermentations to be carried out efficienytly at acidic pH levels.     

Enhanced propionic acid production from Jerusalem artichoke hydrolysate by immobilized Propionibacterium acidipropionici in a fibrous-bed bioreactor

Propionic acid is an important chemical that is widely used in the food and chemical industries. To enhance propionic acid production, a fibrous-bed bioreactor (FBB) was constructed and Jerusalem artichoke hydrolysate was used as a low-cost renewable feedstock for immobilized fermentation. Comparison of the kinetics of immobilized-cell fermentation using the FBB with those of fed-batch free-cell fermentation showed that immobilized-cell fermentation gave a much higher propionic acid concentration (68.5 vs. 40.6 g/L), propionic acid yield (0.434 vs. 0.379 g/g) and propionic acid productivity (1.55 vs. 0.190 g/L/h) at pH 6.5. Furthermore, repeated batch fermentation, carried out to evaluate the stability of the FBB system, showed that long-term operation with a high average propionic acid yield of 0.483 g/g, high productivity of 3.69 g/L/h and propionic acid concentration of 26.2 g/L were achieved in all eight repeated batches during fermentation for more than 200 h. It is thus concluded that the FBB culture system can be utilized to realize the economical production of propionic acid from Jerusalem artichoke hydrolysate during long-term operation.     

不同发酵条件下产甘油假丝酵母有机酸代谢的研究

产甘油假丝酵母 (Candidaglycerolgenesis)发酵产生的有机酸对丙三醇产品质量和产率均有影响。发现在发酵其它条件恒定 ,装液比和玉米浆浓度增加时 ,发酵液总酸是递增的。在装液比为 0 2和玉米浆浓度为 8g L时 ,丙酮酸和乳酸在细胞生长期可分别积累达 4 1g L和 1 0g L ,比正常发酵时增加 2倍以上 ,丙三醇产率也低 ;然而 ,装液比为 0 0 8和玉米浆浓度为 4g L时 ,丙酮酸和乳酸产生较低 ,丙三醇产率较高 ,但乙酸积累比供氧不足时高 ,可达 2 6g L。发酵过程中有机酸被细胞代谢 ,含量逐渐下降 ,如在初糖浓度为 1 0 0g L时 ,有机酸在细胞生长期积累至高峰后 ,丙三醇和有机酸随之均降低至较低含量 ,并且丙酮酸或乳酸可以转化为乙酸。此外 ,在外加一些添加剂时对其产生有机酸也有影响 ,如添加 1 %油酸和VB1时可以降低乙酸的积累 ,同时增加丙酮酸的含量 ,丙三醇产量也有所增加 ;而丙酮酸结构类似物氟代丙酮酸和亚硫酸盐促进乙酸的产生 ,使酮戊二酸合成减少 ,丙三醇产量约增加 2 0 %。     

Growth engineering of Propionibacterium freudenreichii shermanii for organic acids and other value-added products formation

Propionic acid production from glucose was studied using Propionibacterium freudenreichii shermanii. Conditions were optimized for high yields of propionic acid and total organic acids by sequential optimization of parameters like pH, inoculum age, inoculum volume and substrate concentration. Near-theoretical yield (0.54?±?0.023?g/g) was achieved for propionic acid with fermentation of 1% glucose using 20% (v/v) of 48?hr old P. shermanii at 30°C, pH maintained at 5.5. Total organic acid yield under these conditions was 0.74?±?0.06?g/g. The study resulted in achieving 98% and 95% theoretical yields of propionic acid and total organic acids, respectively. Under optimized conditions, along with organic acids, P. shermanii also produced vitamin B12 and trehalose intracellularly, showing its potential to be used as a cell factory.     

In vitro simulation of rabbit cecal fermentation in a semi- continuous flow fermentor. I. Role of food substrate pretreatment]

A Rusitec semi-continuous flow fermentor was used to study the influence of enzyme pretreatment of food substrates on the fermentation profile over a 2-week period following inoculation with rabbit caecal contents. Three types of substrate were examined: 1) homogenized commercial rabbit feed; 2) the solid remains of this feed after digestion with alpha-amylase for 24 h; and 3) substrate 2 digested for 4 h with pepsin (double enzyme treatment). One of a pair of nylon pouches containing 15 g substrate was replaced each day, thus producing a uniform 48-h fermentation. Fermentation of the untreated feed (1) for 5-6 days produced a fermentation profile quite different from that obtained in vivo in the rabbit caecum: propionic acid accounted for over 35% of total volatile fatty acid (VFA), and butyric acid for about 15%. Amylase digestion (2) gave a stable ferment profile closer to the in vivo profile, except that propionic and butyric acids were similar at 15% of total VFA. Digestion with both amylase and pepsin (3) produced a stable fermentation profile very close to the in vivo profile: C2 > 60%, C3 < 11% and 17% < C4 < 21%. The rate at which membrane constituents (acid detergent fibre, ADF) were lost in 48 h was similar to the digestibility coefficient measured in vivo by others for the same basic feed. Lastly, there was a high percentage (about 5%) of volatile C5 fatty acids; this could be due to the discontinuous fermentor input of one pouch per 24 h. Thus, feed pretreated with both amylase and pepsin simulates, in vitro, rabbit caecal fermentation in a semi-continuous Rusitec type fermentor.     

Ethanol-type fermentation from carbohydrate in high rate acidogenic reactor

It has been found, in this study, that a new ethanol-type fermentation can be obtained in a continuous flow, high-rate acidogenic reactor receiving molasses as the feed. The operating pH must be maintained at about 4.5 to avoid onset of propionic fermentation. The acidogenic reactor had a VSS level of 20 g/L and its organic loading was as high as 80 to 90 kg COD/m(3) d. The operating ORP was around -250 mV. The ethanol-type fermentation was characterized by a simultaneous production of acetic acid and ethanol, while the yield of propionic was minimal even at a high organic loading rate of 80 to 90 kg COD/m(3) d, and also, the hydrogen partial pressure was as high as 50 kPa. Thus, this study has shown that the production of propionic acid is not always related to high hydrogen partial pressure. When the operating pH was increased to 5.5, the yield of propionic acid became significant. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54: 428-433, 1997.