补料培养提高真养产碱杆菌产3-羟基丁酸和3-羟基戊酸共聚物生产强度的研究

对Alcaligeneseutrophus进行高密度培养 ,研究表明在发酵过程中进行有效控制 ,可以较大幅度地提高 3-羟基丁酸和 3 羟基戊酸共聚物 [P(3HB-co-3HV) ]的生产强度。实验中选择使用限氮的方法积累P(3HB-co-3HV) ,分别采用丙酸和戊酸为 3HV前体 ,对摇瓶种子生长状态 ,停氮时机对菌体生产P(3HB-co-3HV)的影响以及补酸 (3HV前体 )策略进行了研究 ,在 6.6L罐中 ,以葡萄糖为碳源 ,以丙酸为 3HV前体培养 5 0h ,细胞干重 ,PHA产量 ,PHA含量分别达到 149.9g L ,12.49g L ,83.3% (其中 3HV组分占PHA的 12 4mol% ) ,生产强度达到 2.50 (g·h^-1·L^-1) ;以戊酸为3HV前体培养 45h ,细胞干重 ,PHA产量 ,PHA含量分别达到 16.02g L、119 0g L、74.2 % (其中 3HV组分占PHA的17.7mol% ) ,生产强度达到 2.64(g·h^-1·L^-1)     

真养产碱杆菌合成3-羟基丁酸与3-羟基戊酸共聚物发酵条件研究

在摇瓶条件下,对真养产碱杆菌（Ａｌｃａｌｉｇｅｎｅｓｅｕｔｒｏｐｈｕｓ）的３羟基丁酸与３羟基戊酸共聚物（ＰＨＢＶ）发酵过程中ＨＶ组分的前体物质———丙酸的加入时间和加入量进行了研究,结果表明,ＰＨＢＶ中ＨＶ组分含量与丙酸的加入时间和加入量有密切的关系,丙酸的最佳加入时间为菌体生长阶段结束后的多聚物合成初期;尽管高浓度丙酸下可获得较高的ＨＶ组分含量,但会明显抑制菌体的生长和产物的合成。通过对２Ｌ小罐中ＰＨＢＶ合成阶段流加不同糖／酸比混合液所得的发酵结果的比较,并在综合考虑ＰＨＢＶ浓度、ＨＶ组分含量、生产强度和生产成本等基础上,提出了在ＰＨＢＶ合成期流加液的糖／酸比应随菌体对丙酸利用能力的下降而不断增加的流加策略,在此条件下,细胞干重、ＰＨＢＶ浓度和ＰＨＢＶ含量和ＨＶ摩尔分率分别达到５２１ｇ／Ｌ、４０８ｇ／Ｌ、７８３％和１６２ｍｏｌ％,ＨＶ组分对丙酸的产率系数为０５ｇ／ｇ,ＰＨＢＶ的生产强度达到０７４ｇ／（Ｌ／ｈ）。     

真养产碱杆菌合成3-羟基丁酸与3-羟基戊酸共聚物发酵条件研究

在摇瓶条件下,对真养产碱杆菌（Ａｌｃａｌｉｇｅｎｅｓｅｕｔｒｏｐｈｕｓ）的３羟基丁酸与３羟基戊酸共聚物（ＰＨＢＶ）发酵过程中ＨＶ组分的前体物质———丙酸的加入时间和加入量进行了研究,结果表明,ＰＨＢＶ中ＨＶ组分含量与丙酸的加入时间和加入量有密切的关系,丙酸的最佳加入时间为菌体生长阶段结束后的多聚物合成初期;尽管高浓度丙酸下可获得较高的ＨＶ组分含量,但会明显抑制菌体的生长和产物的合成。通过对２Ｌ小罐中ＰＨＢＶ合成阶段流加不同糖／酸比混合液所得的发酵结果的比较,并在综合考虑ＰＨＢＶ浓度、ＨＶ组分含量、生产强度和生产成本等基础上,提出了在ＰＨＢＶ合成期流加液的糖／酸比应随菌体对丙酸利用能力的下降而不断增加的流加策略,在此条件下,细胞干重、ＰＨＢＶ浓度和ＰＨＢＶ含量和ＨＶ摩尔分率分别达到５２１ｇ／Ｌ、４０８ｇ／Ｌ、７８３％和１６２ｍｏｌ％,ＨＶ组分对丙酸的产率系数为０５ｇ／ｇ,ＰＨＢＶ的生产强度达到０７４ｇ／（Ｌ／ｈ）。     

真养产碱杆菌突变株65—7产羟基丁酸与羟基戊酸共聚物的研究

研究了真养产碱杆菌突变株６５－７,以葡萄糖为主原料,添加丙酸或戊酸,采用二步发酵积累共聚物聚β－羟基丁酸－β－羟基戊酸（ＰＨＢＶ）。摇瓶总发酵时间为５０ｈ,细胞干重达７－１１ｇ／Ｌ,共聚物含量占细胞干重的７０％以上,其中β－羟基戊酸（３ＨＶ０含量占ＰＨＢＶ的１０－７２％,主要取决于不同碳源的组成,丙酸和戊酸对ＨＶ的转化率分别为０．４１－０．６３ｇＨＶ／ｇ丙酸和０．４０－０．７４ｇＨＶ／ｇ戊酸,制得     

真养产碱杆菌积累聚-β-羟基丁酸发酵条件的研究

对Ａｌｃａｌｉｇｅｎｅｓ ｅｕｔｒｏｐｈｕｓ培养过程的研究表明,氮源的限制或缺乏刺激细胞大量积累聚－β－羟基丁酸（ＰＨＢ）,但ＰＨＢ合成期氮源的完全缺乏,会导致细胞的ＰＨＢ合成速率迅速下降,氧的限制也可刺激Ａ．ｅｕｔｒｏｐｈｕｓ合成ＰＨＢ,但胞内ＰＨＢ的积累远小于氮源控制下的情况。在细胞的不同生长期限制氮源的供应会明显影响ＰＨＢ的发酵过程,当残留菌体浓度达到２０ｇ／Ｌ至３０ｇ／Ｌ时停止流加氮水,可     

真养产碱杆菌积聚-β-羟基丁酸发酵条件的研究

igenes eutrophus培养过程的研究表明,氮源的限制或缺乏可刺激细胞大量积累聚-β-羟基丁酸(PHB),但PHB合成期氮源的完全缺乏,会导致细胞的PHB合成速率迅速下降;氧的限制也可刺激A.eutrophus合成PHB,但胞内PHB的积累量远小于氮源控制下的情况。在细胞的不同生长期限制氮源的供应会明显影响PHB的发酵过程,当残留菌体浓度达到20g/L至30g/L时停止流加氨水,可以得到较好的发酵水平,细胞干重,PHB含量和PHB浓度可分别达到61.9g/L、80.5%和49.0g/L。     

自养黄杆菌合成羟基丁酸和羟基戊酸共聚体的发酵研究

采用本实验室从土壤中分离到的一株自养黄杆菌进行了羟基丁酸和羟基戊酸共聚体〔P(HB-co-HV)〕的发酵试验。实验结果表明,该菌株是自养黄杆菌葡萄糖运输突变株,可以葡萄糖、果糖、蔗糖、麦芽糖、乙酸盐、乳酸盐和苹果酸盐作为唯一碳源,尤以葡萄糖和果糖效果最佳。硫酸铵、氯化铵和蛋白胨等不同氮源不影响其生长,却影响细胞中P(HB-co-HV)的含量和P(HB-co-HV)中HV/HB的比例。应用两阶段控制方式,经42h的补料分批发酵,细胞浓度达34.9g·L~(-1),P(HB-co-HV)浓度达25.28g·L~(-1)。细胞和P(HB-co-HV)生产速率系数分别为0.83g·L~(-1)”·h~(-1)和0.61g·L~(-1)·h~(-1)。以基质为基准的细胞得率系数(Yx/s)、产物得率系数(Yp/s)和以干细胞为基准的产物得率系数(Yp/x)分别为0.283(g/g)、0.174(g/g)和0.73(g/g)。改变培养基中碳氮源组分可将P(HB-co-HV)中HB的含量调节在24％～78％之间。     

真养产碱杆菌突变株65－7产聚－β－羟基丁酸的研究

本文对真养产碱杆菌突变株６５－７在台式２Ｌ发酵罐中利用葡萄糖积累ＰＨＢ进行了碳源和氮源补料分批培养的研究。结果表明７２ｈ发酵液中细胞干重达５０ｇ／Ｌ,ＰＨＢ占细胞干重的７７％,糖对ＰＨＢ的转化率为２５％。制得的ＰＨＢ产品纯度与Ｓｉｇｍａ公司的相当,熔点１７４℃。     

真养产碱菌利用甜菜糖蜜发酵产聚β－羟基丁酸的研究

探讨了以廉价原料甜菜糖蜜培养真养产碱菌（Ａｌｃａｌｉｇｅｎｅｓｅｕｔｒｏｐｈｕｓ）Ｈ１６生产聚β－羟基丁酸（ＰＨＢ）的可行性。对培养基优化试验表明,菌体产量可达２０ｇ／Ｌ,ＰＨＢ产量达９．８ｇ／Ｌ,糖转化率为２７．５％。用２升自控发酵罐进行验证,在良好的供氧条件和特定的ｐＨ值自控条件下发酵周期从４８小时缩短到４０－４２小时,菌体和ＰＨＢ量都有提高。菌体最高产量２６ｇ／Ｌ,ＰＨＢ最高产量１３ｇ／Ｌ,糖转化率为２０．４％。ＰＨＢ占细胞的含量,摇瓶和罐上结果都在５０％左右。     

Production of poly(D-3-hydroxybutyrate) from CO(2), H(2), and O(2) by high cell density autotrophic cultivation of Alcaligenes eutrophus

Hydrogen-oxidizing bacterium, Alcaligenes eutrophus autotrophically produces biodegradable plastic material, poly(D-3-hydroxybutyrate), P(3HB), from carbon dioxide, hydrogen, and oxygen. In autotrophic cultivation of the microorganism, it is essential to eliminate possible occurrence of gas explosions from the fermentation process. We developed a bench-plant scale, recycled-gas, closed-circuit culture system equipped with several safety features to perform autotrophic cultivation of A. eutrophus by maintaining the oxygen concentration in the substrate gas phase below the lower limit for a gas explosion (6.9%). The culture vessel utilized a baskettype agitator, resulting in a K(L) a value of 2970 h(-1). Oxygen gas was also directly fed to the fermentor separately from the other gases. As a result, 91.3 g . dm(-3) of the cells and 61.9 g . dm(-3) of P(3HB) were obtained after 40 h of cultivation under this oxygen-limited condition. The results compared favorably with those reported for mass production of P(3HB) by heterotrophic fermentation. (c) 1995 John Wiley & Sons, Inc.     

Turnover of poly(3-hydroxybutyrate) (PHB) and its influence on the molecular mass of the polymer accumulated by Alcaligenes eutrophus during batch culture

Abstract Radiolabelled glucose was added to a batch culture of Alcaligenes eutrophus during the accumulation of poly(3-hydroxybutyrate) (PHB) to label newly synthesized polymer. The specific radioactivity of the polymer continued to increase, by approximately 30%, after the cessation of PHB accumulation, indicating that turnover of PHB was occurring. Fractionation of PHB showed that high molecular mass polymer was gradually replaced by PHB of lower molecular mass. Turnover of PHB is the cause of the slow decline in the molecular mass of PHB following the cessation of polymer accumulation but is unlikely to be the sole reason for the more rapid decrease in the molecular mass of PHB during the accumulation phase.     

Effects of Low Dissolved-Oxygen Concentrations on Poly-(3-Hydroxybutyrate-co-3-Hydroxyvalerate) Production by Alcaligenes eutrophus

The bacterial copolyester poly-(3-hydroxybutyrate-co-3-hydroxyvalerate) was produced with Alcaligenes eutrophus DSM 545 from glucose and sodium propionate in a fed-batch fermentation with both nitrogen limitation and low dissolved-oxygen concentrations. When the dissolved-oxygen content was kept between 1 and 4% of air saturation during the polymer accumulation phase, the yield of 3-hydroxybutyrate (3HB) monomer from glucose was not affected, but the propionate-to-3-hydroxyvalerate (3HV) monomer yield was two to three times (0.48 to 0.73 mol of 3HV mol of propionate consumed(sup-1)) that observed in a control experiment (0.25 mol mol(sup-1)), where the accumulation-phase dissolved-oxygen concentration was 50 to 70% of air saturation. The overall polymer productivity of the fermentation was somewhat decreased by low dissolved-oxygen contents, owing to a slower 3HB production rate. The effect of a low dissolved-oxygen concentration is probably attributable to a reduction of the oxygen-requiring decarbonylation of propionyl-coenzyme A (CoA) to acetyl-CoA.     

Production of poly(3-hydroxybutyric acid) by fed-batch culture of Alcaligenes eutrophus with glucose concentration control

Alcaligenes eutrophus NCIMB 11599 was cultivated to produce poly(3-hydroxybutyric acid) (PHB) from glucose by the automatic fed-batch culture technique. The glucose concentration of the culture broth was controlled at 10 to 20 g/L by two methods: using exit gas data obtained from a mass spectrometer and using an on-line glucose analyzer. The effect of ammonium limitation on PHB synthesis at different culture phases was studied. The final cell concentration, PHB concentration, and PHB productivity increased as ammonia feeding was stopped at a higher cell concentration. High concentrations of PHB (121 g/L) and total cells (164 g/L) were obtained in 50 h when ammonia feeding was stopped at the cell concentration of 70 g/L. The maximum PHB content reached 76% of dry cell weight and the productivity was 2.42 g/L h with the yield of 0.3 g PHB/g glucose.     

Characterization of two 3-ketothiolases possessing differing substrate specificities in the polyhydroxyalkanoate synthesizing organism Alcaligenes eutrophus

Abstract Two constitutive acetyl-CoA acetyltransferases (3-ketothiolases A and B) were purified from Alcaligenes eutrophus . Enzyme A was active with only acetoacetyl-CoA and 3-ketopentanoyl-CoA, whereas enzyme B was active with all the 3-ketoacyl-CoAs (C₄−C₁₀) tested. Enzyme A appeared to be a tetramer ( M _r 70 000) with identical subunits ( M _r 44 000) and enzyme B had a similar M _r of 168 000 (containing M _r 46 000 subunits). Enzymes A and B had isoelectric points of 5.0 and 6.4, respectively. The stoichiometry of the reactions catalysed by each enzyme was confirmed. K _m values of 44 μM and 394 μM for acetoacetyl-CoA, and 16 μM and 93 μM for CoA, were determined with enzymes A and B, respectively. Enzymes A and B gave K _m values of 1.1 mM and 230 μM, respectively, for acetyl-CoA. The condensation reaction was potently inhibited by CoA in both cases.     

Localization of the membrane-bound hydrogenase in Alcaligenes eutrophus by electron microscopic immunocytochemistry

Abstract The membrane-bound hydrogenase was localized in cells of Alcaligenes eutrophus by electron microscopic immunocytochemistry. Post-embedding labeling performed on ultrathin sections revealed that the enzyme was located predominantly (80%) at the cell periphery in autotrophically and heterotrophically grown bacteria harvested from the exponential phase of growth. In the stationary growth phase, however, only 50% of the enzyme was found at the cell periphery; the remaining 50% was distributed over the cytoplasm. The relative amount of electron microscopic label per cell as seen by application of the protein A—gold technique was higher in cells grown autotrophically as compared to cells grown heterotrophically on fructose. Derepression of the enzyme was followed electron microscopically in a substrate-shift experiment (growth on fructose, followed by a shift to glycerol). Major amounts of the enzyme appeared to undergo a reattachment to the cytoplasmic membrane under these conditions, starting with a reduced location of the enzyme in the cytoplasm and an accumulation in cell areas close to the cytoplasmic membrane. These findings indicate that the 'membrane-bound' hydrogenase (i.e., that material enriched as membrane-bound enzyme according to the appropriate activity test) is not, in fact, membrane bound or membrane integrated but membrane associated. It may or may not interact with the cytoplasmic face of the cytoplasmic membrane, depending on the growth phase and conditions.     

High-Level Production of Poly(3-Hydroxybutyrate-co-3-Hydroxyvalerate) by Fed-Batch Culture of Recombinant Escherichia coli

Fermentation strategies for production of high concentrations of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [P(3HB-co-3HV)] with different 3-hydroxyvalerate (3HV) fractions by recombinant Escherichia coli harboring the Alcaligenes latus polyhydroxyalkanoate biosynthesis genes were developed. Fed-batch cultures of recombinant E. coli with the pH-stat feeding strategy facilitated production of high concentrations and high contents of P(3HB-co-3HV) in a chemically defined medium. When a feeding solution was added in order to increase the glucose and propionic acid concentrations to 20 g/liter and 20 mM, respectively, after each feeding, a cell dry weight of 120.3 g/liter and a relatively low P(3HB-co-3HV) content, 42.5 wt%, were obtained. Accumulation of a high residual concentration of propionic acid in the medium was the reason for the low P(3HB-co-3HV) content. An acetic acid induction strategy was used to stimulate the uptake and utilization of propionic acid. When a fed-batch culture and this strategy were used, we obtained a cell concentration, a P(3HB-co-3HV) concentration, a P(3HB-co-3HV) content, and a 3HV fraction of 141.9 g/liter, 88.1 g/liter, 62.1 wt%, and 15.3 mol%, respectively. When an improved nutrient feeding strategy, acetic acid induction, and oleic acid supplementation were used, we obtained a cell concentration, a P(3HB-co-3HV) concentration, a P(3HB-co-3HV) content, and a 3HV fraction of 203.1 g/liter, 158.8 g/liter, 78.2 wt%, and 10.6 mol%, respectively; this resulted in a high level of productivity, 2.88 g of P(3HB-co-3HV)/liter-h.     

Poly-3-hydroxybutyrate production by washed cells of Alcaligenes eutrophus; purification, characterisation and potential regulatory role of citrate synthase

Washed cells prepared from carbon-limited continuous cultures of Alcaligenes eutrophus synthesised poly-3-hydroxybutyrate (PHB) rapidly when supplied with glucose, dl-lactate or l-lactate. Unlike growing cultures, washed cells excreted significant amounts of pyruvate. The combined rates of PHB production (qPHB) and pyruvate excretion (qPyr) were linearly related to the rate of carbon substrate utilisation (qS), showing that washed cells behaved similarly to growing cultures when corrected for the absence of non-PHB biomass production. The addition of formate (as a potential source of NADH and/or ATP) significantly stimulated both qPHB and qPyr, but slightly decreased qS and substantially decreased the flux of carbon through the tricarboxylic acid cycle (qTCA). Citrate synthase activity of broken cells was inhibited by physiological concentrations of NADH, but not of ATP, in a manner that was not reversible by AMP. Citrate synthase was purified and shown to be a “large” form of the enzyme (M _r 227,000), comprising a single type of subunit (M _r 47,000) as found in several other gram-negative aerobes. The potential role of citrate synthase in the regulation of PHB production via its ability to control carbon flux into the tricarboxylic acid cycle is discussed. Received: 14 March 1997 / Accepted: 9 July 1997     

hoxX (hypX) is a functional member of the Alcaligenes eutrophus hyp gene cluster

The role of HoxX in hydrogenase biosynthesis of Alcaligenes eutrophus H16 was re-examined. The previously characterized hoxX deletion mutant HF344 and a newly constructed second hoxX mutant carrying a smaller in-frame deletion were studied. The second mutant was impaired in the activity of both the soluble and the membrane-bound hydrogenase. The two hydrogenase activities were reduced by approximately 50% due to delayed processing of the active-site-containing large subunits, while hydrogenase gene expression was not affected. We conclude that the mutation in mutant HF344 causes polarity resulting in the observed regulatory phenotype of this mutant. The data presented in this report point to an enhancing function of HoxX in the conversion of the soluble hydrogenase and of the membrane-bound hydrogenase large-subunit precursor. Thus, hoxX encodes a member of the Hyp proteins that are required for the formation of active hydrogenase and was accordingly renamed hypX. Received: 15 June 1998 / Accepted: 5 August 1998