Coenzyme Q10 production by Sphingomonas sp. ZUTE03 with novel precursors isolated from tobacco waste in a two-phase conversion system

Coenzyme Q10 (CoQ10) is a widely used supplement in heart diseases treatment or antioxidative dietary. The microbial production of CoQ10 was enhanced by addition of solanesol and novel precursors recovered from waste tobacco. The novel precursors were separated by silica gel and identified as alpha-linolenic acid (LNA) and butylated hydroxytoluene (BHT) based on the effect on CoQ10 production and GC-MS. The effects of novel precursors on CoQ10 production by Sphingomonas sp. ZUTE03 were further evaluated in a two-phase conversion system. The precursor's combination of solanesol (70 mg/l) with BHT (30 mg/l) showed the best effect on the improvement of CoQ10 yield. A maximal CoQ10 productivity (9.5 mg l-1 h-1) was achieved after 8 h conversion, with a molar conversion rate of 92.6% and 92.4% on BHT and solanesol, respectively. The novel precursors, BHT and LNA in crude extracts from waste tobacco leaves, might become potential candidates for application in the industrial production of CoQ10 by microbes.     

茄尼醇转化高产辅酶Q10菌株的分离鉴定与发酵条件的研究

采用以异戊二烯为唯一碳源的选择性平板筛选模型,从钱塘江沿岸杭州市九堡段土壤中新筛选到一株产辅酶Q10的细菌菌株E03,经形态、生理生化、Biolog碳源利用试验和16S rDNA序列分析,确定E03属于鞘氨醇属(Sphingomonas sp.),命名为Sphingomonas sp.ZUTE03.摇瓶试验确定了该菌发酵生产辅酶Q10的最佳碳源为葡萄糖15 g/L,氮源为硫酸铵10 g/L,初始pH8.0,发酵温度25℃,并考察了该菌转化茄尼醇产辅酶Q.0的发酵工艺,以合适溶剂为溶解体系,于发酵培养基中摇床培养12 h后,加入终浓度为0.75 g/L的茄尼醇粗品,转化12 h,辅酶Q10产值可达96.88 mg/L.     

Coenzyme Q<Subscript>10</Subscript> production directly from precursors by free and gel-entrapped <Emphasis Type="Italic">Sphingomonas</Emphasis> sp. ZUTE03 in a water-organic solvent,two-phase conversion system

In a water-organic solvent, two-phase conversion system, CoQ₁₀ could be produced directly from solanesol and para-hydroxybenzoic acid (PHB) by free cells of Sphingomonas sp. ZUTE03 and CoQ₁₀ concentration in the organic solvent phase was significantly higher than that in the cell. CoQ₁₀ yield reached a maximal value of 60.8 mg l⁻¹ in the organic phase and 40.6 mg g⁻¹-DCW after 8 h. CoQ₁₀ also could be produced by gel-entrapped cells in the two-phase conversion system. Soybean oil and hexane were found to be key substances for CoQ₁₀ production by gel-entrapped cells of Sphingomonas sp. ZUTE03. Soybean oil might improve the release of CoQ10 from the gel-entrapped cells while hexane was the suitable solvent to extract CoQ₁₀ from the mixed phase of aqueous and organic. The gel-entrapped cells could be re-used to produce CoQ₁₀ by a repeated-batch culture. After 15 repeats, the yield of CoQ₁₀ kept at a high level of more than 40 mg l⁻¹. After 8 h conversion under optimized precursor’s concentration, CoQ₁₀ yield of gel-trapped cells reached 52.2 mg l⁻¹ with a molar conversion rate of 91% and 89.6% (on PHB and solanesol, respectively). This is the first report on enhanced production of CoQ₁₀ in a two-phase conversion system by gel-entrapped cells of Sphingomonas sp. ZUTE03.     

Bioconversion of farnesol and 1,4-dihydroxy-2-naphthoate to menaquinone by an immobilized whole-cell biocatalyst using engineered <Emphasis Type="Italic">Elizabethkingia meningoseptica</Emphasis>

Menaquinone (MK) has important applications in the pharmaceutical and food industries. To increase the production rate (Q_P) of MK-4, we developed a straightforward biotransformation method for MK-4 synthesis directly from its precursors 1,4-dihydroxy-2-naphthoate (DHNA) and farnesol using whole cells of genetically engineered Elizabethkingia meningoseptica. Results showed that MK-4 can be produced directly from farnesol and DHNA using both free and immobilized FM-D198 cells. MK-4 yield peaked at 29.85?±?0.36 mg/L in the organic phase and 24.08?±?0.33 mg/g DCW after 12 h of bioconversion using free cells in a two-phase conversion system. MK-4 yield reached 26.34?±?1.35 mg/L and 17.44?±?1.05 mg/g DCW after 8 h using immobilized cells. Although this yield was lower than that using free cells, immobilized cells can be re-used for MK-4 production via repeated-batch culture. After ten batch cultures, efficient MK-4 production was maintained at a yield of more than 20 mg/L. After optimizing the catalysis system, the MK-4 yield reached 26.91?±?1.27 mg/L using the immobilized cells and had molar conversion rates of 58.56 and 76.90% for DHNA and farnesol, respectively.     

The effect of dissolved oxygen on PHB accumulation in activated sludge cultures

Nitrogen removal from wastewater is often limited by the availability of reducing power to perform denitrification, especially when treating wastewaters with a low carbon:nitrogen ratio. In the increasingly popular sequencing batch reactor (SBR), bacteria have the opportunity to preserve reducing power from incoming chemical oxygen demand (COD) as poly-beta-hydroxybutyrate (PHB). The current study uses laboratory experiments and mathematical modeling in an attempt to generate a better understanding of the effect of oxygen on microbial conversion of COD into PHB. Results from a laboratory SBR with acetate as the organic carbon source showed that the aerobic acetate uptake process was oxygen-dependent, producing higher uptake rates at higher dissolved oxygen (DO) supply rates. However, at the lower DO supply rates (k(L)a 6 to 16 h(-1), 0 mg L(-1) DO), a higher proportion of the substrate was preserved as PHB than at higher DO supply rates (k(L)a 30, 51 h(-1), DO >0.9 mg L(-1)). Up to 77% of the reducing equivalents available from acetate were converted to PHB under oxygen limitation (Y(PHB/Ac) 0.68 Cmol/Cmol), as opposed to only 54% under oxygen-excess conditions (Y(PHB/Ac) 0.48 Cmol/Cmol), where a higher fraction of acetate was used for biomass growth. It was calculated that, by oxygen management during the feast phase, the amount of PHB preserved (1.4 Cmmol L(-1) PHB) accounted for an additional denitrification potential of up to 18 mg L(-1) nitrate-nitrogen. The trends of the effect of oxygen (and hence ATP availability) on PHB accumulation could be reproduced by the simulation model, which was based on biochemical stoichiometry and maximum rates obtained from experiments. Simulated data showed that, at low DO concentrations, the limited availability of adenosine triphosphate (ATP) prevented significant biomass growth and most ATP was used for acetate transport into the cell. In contrast, high DO supply rates provided surplus ATP and hence higher growth rates, resulting in decreased PHB yields. The results suggest that oxygen management is crucial to conserving reducing power during the feast phase of SBR operation, as excessive aeration rates decrease the PHB yield and allow higher biomass growth.     

Batch cultivation of Methylosinus trichosporium OB3b: V. Characterization of poly-beta-hydroxybutyrate production under methane-dependent growth conditions

Methanotrophs have promising applications in the bioremediation of chlorinated hydrocarbons and in the production of a biopolymer, poly-beta-hydroxybutyrate (PHB). Batch bioreactor culture conditions were studied for the accumulation of PHB by methane-grown Methylosinus trichosporium OB3b, and to evaluate the effect of PHB on the bacterial capacity to degrade trichloroethylene (TCE), a common groundwater contaminant. The PHB content of the washed and lyophilized cells was measured by gas chromatography (GC), after hydrochloric acid (HCl) propanolysis. A differential GC-based assay was developed for the monomer and the polymer of beta-hydroxybutyrate utilizing 1% and 10% HCl (v/v) reaction mixtures, respectively. During bioreactor growth in a Cu-deficient modified Higgins' medium, the cells accumulated PHB upon depletion of nitrate. A biomass yield of 3.2 g dry wt/L and a PHB accumulation of approximately 10% (w/w) were reached after 140 to 160 h, without adversely affecting the propene or TCE epoxidation specific rate given by whole cells containing soluble methane monooxygenase (sMMO). The TCE biotransformation capacity ( approximately 0.25 mg TCE oxidized/mg dry cell wt) of resting cells containing approximately 10% PHB was consistently approximately 1.6-fold greater than that of cells containing only approximately 2% PHB. Higher levels (>10%) of accumulated PHB did not enhance this biotransformation capacity further. By replacing the bioreactor inlet air + CO(2) mixture with pure O(2) at approximately 85 h of batch operation, a PHB accumulation of approximately 45% was achieved after 160 h, but the whole-cell sMMO activity was markedly decreased. In contrast, cells grown in a 10 muM Cu-supplemented Higgins' nitrate minimal salts medium (particulate MMO formation) accumulated up to 50% PHB in only 120 h, coupled with a very high biomass yield of 18 g dry cell wt/L. High PHB accumulations above approximately 20% by both the -Cu and the +Cu grown cells resulted in a decreased ratio of the electronic cell count to the absorbance at 660 nm, which is commonly used to monitor bacterial growth. (c) 1996 John Wiley & Sons, Inc.     

半导体激光和紫外线对辅酶Q10产生菌的复合诱变效应

采用紫外线、半导体激光及紫外线与半导体激光复合作用的方法,诱变产辅酶Q10红酵母菌SY-3,以提高辅酶Q10的产量。结果表明,紫外线和半导体激光单独作用,诱变效果不佳,而二者的复合作用却能产生很好的效果。用紫外照射120 s再经半导体激光辐射8 min,得到一株叠氮钠和维生素K3双抗性突变株,产辅酶Q10的量达到157.7 mg/L,比原始菌株提高了88.1%,并具有良好的遗传稳定性。     

Effect of high nitrate concentration on PHB storage in sequencing batch reactor under anoxic conditions

The study investigated effect of high influent nitrate concentration on poly-beta-hydroxybutyrate, (PHB), storage in a sequencing batch reactor, (SBR), under anoxic conditions. Acetate was fed as pulse during anoxic phase, sustained with external nitrate feeding. SBR operation involved three runs at steady state with COD/N ratios of 3.84, 2.93 and 1.54 gCOD/gN, where external nitrate concentrations gradually increased from 50 mg N/l to 114 mg N/l and 226 mg N/l, in 1st, 2nd and 3rd runs, respectively. In 1st run, acetate was fully converted into PHB with the storage yield value of 0.57-0.59 gCOD/gCOD, calculated both in terms of PHB formation and NO(X) utilization, confirming storage was the sole substrate utilization mechanism. In the following runs, PHB formation was reduced and the storage yield based on PHB dropped down to 0.40 and 0.33 gCOD/gCOD with increasing influent nitrate concentrations, indicating that higher portions of acetate were diverted to simultaneous direct growth. The observations suggested that nitrite accumulation detected at low COD/N ratios was responsible for inhibition of PHB storage.     

营养条件和流加发酵对放射型根瘤菌(Rhizobium radiobacter)产辅酶Q10的影响

利用放射型根瘤菌WSH2 6 0 1(RhizobiumradiobacterWSH2 6 0 1)重点考察了葡萄糖、蔗糖、玉米浆和蛋白胨、添加物以及流加发酵对细胞生长和产辅酶Q1 0 的影响 ,结果表明 ,葡萄糖和蔗糖适合于生产辅酶Q1 0 的最佳浓度分别为 30g L和 40g L ;辅酶Q1 0 发酵时玉米浆和蛋白胨的最适浓度分别为 11g L和 16g L ;添加蕃茄汁、玉米浆能提高发酵液的生物量 ,玉米浆、异戊醇、L 甲硫氨基酸等能促进辅酶Q1 0 的积累 ;与分批发酵相比 ,在 7L罐上流加蔗糖其细胞生物量 (DCW)和辅酶Q1 0 积累量增加 ,若在流加蔗糖的同时流加适当浓度的玉米浆能显著提高辅酶Q1 0 的产量 ,最大产量达到 5 2 .4mg L ;最大生物量 (DCW)和胞内辅酶Q1 0 含量 (C B值 )分别达到 2 6 .4g L和 2 .38mg g DCW ,比不流加的分批发酵分别提高 5 3 %和 33% ,比只流加蔗糖分别提高 2 4%和 2 6 %。     

Bioconversion of acrylonitrile to acrylamide using polyacrylamide entrapped cells of <Emphasis Type="Italic">Rhodococcus rhodochrous</Emphasis> PA-34

The nitrile hydratase (NHase) of Rhodococcus rhodochrous PA-34 catalyzed the conversion of acrylonitrile to acrylamide. The resting cells (having NHase activity) (8 %; 1 mL corresponds to 22 mg dry cell mass, DCM) were immobilized in polyacrylamide gel containing 12.5 % acrylamide, 0.6 % bisacrylamide, 0.2 % diammonium persulfate and 0.4 % TEMED. The polyacrylamide entrapped cells (1.12 mg DCM/mL) completely converted acrylonitrile in 3 h at 10 °C, using 0.1 mol/L potassium phosphate buffer. In a partitioned fed batch reactor, 432 g/L acrylamide was accumulated after 1 d. The polyacrylamide discs were recycled up to 3×; 405, 210 and 170 g/L acrylamide was produced in 1st, 2nd and 3rd recycling reactions. In four cycles, a total of 1217 g acrylamide was produced by recycling the same mass of entrapped cells.     

玉米芯稀酸水解及L-乳酸发酵研究

对玉米芯稀硫酸水解条件及糖化液发酵L-乳酸进行了初步研究。结果表明,玉米芯木聚糖最适水解条件为2%H2SO_4、120℃、30 min、固液比1:10,糖化液还原糖含量可达40.8 g/L,主要成分为木塘。细菌A-19可以利用水解液中的葡萄糖和木糖产酸,最适发酵条件为45℃、pH 6.5,从45℃～51℃、pH 5.5～pH 6.5产量均较高。用未浓缩的水解液发酵24 h,L-乳酸产量为30.6g/L,残糖为1.6 g/L,糖酸转化率为82.6%;用浓缩1倍的水解液发酵48 h,L-乳酸产量为41.4 g/L,残糖4.1g/L,糖酸转化率为68.2%,在发酵48 h后继续补料发酵至72 h(补料液为浓缩3倍的水解液),L-乳酸产量为50.9 g/L,残糖6.3 g/L,糖酸转化率为71.8%。该研究为利用木质纤维素生产L-乳酸奠定了一定基础。     

代谢工程改造大肠杆菌生产辅酶Q10

辅酶Q10(CoQ10)是一种脂溶性抗氧化剂,具有提高人体免疫力、延缓衰老和增强人体活力等功能,广泛应用于制药行业和化妆品行业。微生物发酵法能可持续性生产辅酶Q10,具有越来越多的商业价值。本研究首先将来自类球红细菌的十聚异戊二烯焦磷酸合成酶基因(dps)整合到大肠杆菌ATCC 8739染色体上,敲除内源的八聚异戊二烯焦磷酸合成酶基因(ispB),使内源的辅酶Q8合成途径被辅酶Q10合成途径取代,得到稳定生产辅酶Q10的菌株GD-14,其辅酶Q10产量达0.68 mg/L,单位细胞含量达0.54 mg/g DCW。随后用多个固定强度调控元件在染色体上对MEP途径的关键基因dxs和idi基因以及ubiCA基因进行组合调控,将辅酶Q10单位细胞含量提高2.46倍(从0.54到1.87 mg/g)。进一步引入运动发酵单胞菌Zymomonas mobilis的Glf转运蛋白代替自身的磷酸烯醇式丙酮酸:碳水化合物磷酸转移酶系统(PTS),使辅酶Q10产量进一步提高16%。最后,对高产菌株GD-51进行分批补料发酵,辅酶Q10产量达433 mg/L,单位细胞含量达11.7 mg/g DCW。这是目前为止文献报道的大肠杆菌产辅酶Q10最高菌株。     

Denitrification with endogenous carbon source at low C/N and its effect on P(3HB) accumulation

The objective of the work reported here was to determine whether the ratio of COD/Nox has an impact on poly-beta-hydroxybutyrate (PHB) metabolism in activated sludge. Furthermore, it was tested if the ratio influenced the percentage use of organic compounds present in wastewater, for endogenous respiration, oxidation, accumulation and denitrification. Gas flow rate in SBR reactor was controlled by thermal mass flow controller (TMFC). Constant amount of air entering sequencing batch reactor was automatically adjusted to stable set-point 2mg O2 L(-1). It means that DO concentration in the reactor could change with oxygen uptake. During the filling period and part of the reaction time DO was nearly zero. Feast period of the external substrate availability and famine period of little amount or no external carbon availability were determined. At 23 h of the reaction time, and COD/Nox ratio 8, denitrification took place only during feast period. What was interesting, poly-beta-hydroxybutyrate degradation was observed in the feast period as well. However, at 11h of the reaction time and COD/Nox ratio 37, denitrification occurred in feast and famine period. In the feast period PHB was accumulated and in the famine period was used as the endogenous carbon source. COD consumption to reduce 1mg N-nitrate was ranging from 1.15 to 6.26 depending on carbon source and increased when exogenous and endogenous carbon were used by activated sludge. The increase in PHB content from 0.25 to 0.43 Cmol/Cmol resulted in a double increase in the amount of nitrogen removed due to denitrification was observed.     

Acute impact of tetracycline and erythromycin on the storage mechanism of polyhydroxyalkanoates

The study investigated acute impact of tetracycline and erythromycin on substrate storage under aerobic conditions. A fill and draw reactor fed with peptone mixture was maintained at steady-state at a sludge age of 10 days; the acclimated biomass was used in a series of batch runs. The first run served as control reactor with organic substrate alone and the others were started with antibiotic doses of 50 mg/L and 200 mg/L for assessing intracellular storage. Parallel batch reactors were also conducted for recording oxygen uptake rate profiles. Both antibiotics enhanced substrate storage, leading to higher levels of polyhydroxyalkanoates incorporated into biomass, but they impaired its internal utilization for microbial growth. The observed decrease in oxygen consumption under the acute effect of antibiotics could partially be related to substrate storage – except for 50 mg/L of erythromycin dosing – suggesting an additional substrate binding mechanism by antibiotics, leading to residual biodegradable substrate.     

Nitrogen removal from aquaculture pond water by heterotrophic nitrogen assimilation in lab-scale sequencing batch reactors

The potential use of sequencing batch reactors (SBRs) as an alternative bio-flocs technology (BFT) approach in aquaculture was explored. One SBR was dosed with glycerol and one with acetate for the decrease of the nitrogen concentration in simulated aquaculture water by microbial assimilation. At an optimal C/N ratio between 10 and 15, the nitrogen removal efficiency reached up to 98% (=110 mg N L(-1) reactor day(-1)) for both SBRs. The estimated biomass productivity reached 0.62-0.94 g C L(-1)r eactor day(-1) for the glycerol SBR and 0.54-0.82 g C L(-1) reactor day(-1) for the acetate SBR. The floc protein content, indicating biomass quality, reached up to 57% if grown on glycerol. With acetate, it attained a value of 61%. The highest average poly-beta-hydroxybutyrate (PHB) content was 16% on a dry weight basis for the acetate biomass.     

Nutrient removal from slaughterhouse wastewater in an intermittently aerated sequencing batch reactor

The performance of a 10 L sequencing batch reactor (SBR) treating slaughterhouse wastewater was examined at ambient temperature. The influent wastewater comprised 4672+/-952 mg chemical oxygen demand (COD)/L, 356+/-46 mg total nitrogen (TN)/L and 29+/-10 mg total phosphorus (TP)/L. The duration of a complete cycle was 8 h and comprised four phases: fill (7 min), react (393 min), settle (30 min) and draw/idle (50 min). During the react phase, the reactor was intermittently aerated with an air supply of 0.8L/min four times at 50-min intervals, 50 min each time. At an influent organic loading rate of 1.2g COD/(Ld), average effluent concentrations of COD, TN and TP were 150 mg/L, 15 mg/L and 0.8 mg/L, respectively. This represented COD, TN and TP removals of 96%, 96% and 99%, respectively. Phase studies show that biological phosphorus uptake occurred in the first aeration period and nitrogen removal took place in the following reaction time by means of partial nitrification and denitrification. The nitrogen balance analysis indicates that denitrification and biomass synthesis contributed to 66% and 34% of TN removed, respectively.     

Formation of aerobic granules and their PHB production at various substrate and ammonium concentrations

Aerobic granular sludge rich in polyhydroxybutyrate (PHB) was cultivated in a sequencing batch reactor (SBR) by seeding anaerobic granular sludge. The PHB content in aerobic granules was investigated and the experimental results reveal that both influent chemical oxygen demand (COD) and ammonium concentrations had a significant effect on the morphological characteristics and the PHB production of the aerobic granular sludge. At a COD and ammonium concentration of 750 mg/L and 8.5mg/L, respectively, the PHB content of the granules reached 44%, but their poor settling ability, as evidenced by a high sludge volume index, was observed. This was attributed to the outgrowth of filamentous bacteria on the granule surface. However, an increase in the ammonium concentration resulted in an elevated sludge concentration and a decrease in the PHB content in the granules. In this case, the aerobic granular sludge with a regular and compact structure was formed. The results suggest that, through controlling the COD and ammonium concentrations in the influent, the PHB-rich aerobic granular sludge with good settling ability could be cultivated.     

Poly(3-Hydroxybutyrate) Production with High Productivity and High Polymer Content by a Fed-Batch Culture of Alcaligenes latus under Nitrogen Limitation

Alcaligenes latus has been known to produce poly(3-hydroxybutyrate) (PHB) in a growth-associated manner even under nutrient-sufficient conditions. However, the PHB content obtained by fed-batch culture was always low, at ca. 50%, which makes the recovery process inefficient. In this study, the effect of applying nitrogen limitation on the production of PHB by A. latus was examined. In flask and batch cultures, the PHB synthesis rate could be increased considerably by applying nitrogen limitation. The PHB content could be increased to 87% by applying nitrogen limitation in batch culture, which was considerably higher than that typically obtainable (50%) under nitrogen-sufficient conditions. In fed-batch culture, cells were first cultured by the DO-stat feeding strategy without applying nitrogen limitation. Nitrogen limitation was applied at a cell concentration of 76 g (dry cell weight)/liter, and the sucrose concentration was maintained within 5 to 20 g/liter. After 8 h of nitrogen limitation, the cell concentration, PHB concentration, and PHB content reached 111.7 g (dry cell weight)/liter, 98.7 g/liter, and 88%, respectively, resulting in a productivity of 4.94 g of PHB/liter/h. The highest PHB productivity, 5.13 g/liter/h, was obtained after 16 h.     

Chemostat selection of a bacterial community able to degrade s-triazinic compounds: continuous simazine biodegradation in a multi-stage packed bed biofilm reactor

Using a successive transfer method on mineral salt medium containing simazine, a microbial community enriched with microorganisms able to grow on simazine was obtained. Afterwards, using a continuous enrichment culture procedure, a bacterial community able to degrade simazine from an herbicide formulation was isolated from a chemostat. The continuous selector, fed with a mineral salt medium containing simazine and adjuvants present in the commercial herbicide formulation, was maintained in operation for 42 days. Following the lapse of this time, the cell count increased from 5 x 10(5) to 3 x 10(8) CFU mL(-1), and the simazine removal efficiency reached 96%. The chemostat's bacterial diversity was periodically evaluated by extracting the culture's bacterial DNA, amplifying their 16S rDNA fragments and analyzing them by thermal gradient gel electrophoresis. Finally, a stable bacterial consortium able to degrade simazine was selected. By PCR amplification, sequencing of bacterial 16S rDNA amplicons, and comparison with known sequences of 16S rDNA from the NCBI GenBank, eight bacterial strains were identified. The genera, Ochrobactrum, Mycobacterium, Cellulomonas, Arthrobacter, Microbacterium, Rhizobium and Pseudomonas have been reported as common degraders of triazinic herbicides. On the contrary, we were unable to find reports about the ability of the genus Pseudonocardia to degrade triazinic compounds. The selected bacterial community was attached to a porous support in a concurrently aerated four-stage packed-bed reactor fed with the herbicide. Highest overall simazine removal efficiencies eta (SZ) were obtained at overall dilution rates D below 0.284 h(-1). However, the multistage packed bed reactor could be operated at dilution rates as high as D = 3.58 h(-1) with overall simazine removal volumetric rates R (v,SZ) = 19.6 mg L(-1) h(-1), and overall simazine removal specific rates R (X,SZ) = 13.48 mg (mg cell protein)(-1) h(-1). Finally, the consortium's ability to degrade 2-chloro-4,6-diamino-1,3,5-triazine (CAAT), cyanuric acid and the herbicide atrazine, pure or mixed with simazine, was evaluated in fed batch processes.     

Poly(β-hydroxybutyric acid) thermoplastic production by Alcaligenes latus: Behavior of fed-batch cultures

Fed-batch culture of Alcaligenes latus, ATCC 29713, was investigated for producing the intracellular bioplastic poly(β–hydroxybutyric acid), PHB. Constant rate feeding, exponentially increasing feeding rate, and pH-stat fed batch methods were evaluated. pH-stat fed batch culture reduced or delayed accumulation of the substrate in the broth and led to significantly enhanced PHB productivity relative to the other modes of feeding. Presence of excessive substrate appeared to inhibit PHB synthesis, but not the production of cells. In fed-batch culture, the maximum specific growth rate (0.265?h^?1) greatly exceeded the value (0.075?h^?1) previously observed in batch culture of the same strain. Similarly, the maximum PHB production rate (up to 1.15?g?·?l^?1?·?h^?1) was nearly 8-fold greater than values observed in batch operations. Fed-batch operation was clearly superior to batch fermentation for producing PHB. A low growth rate was not a prerequisite for PHB accumulation, but a reduced or delayed accumulation of substrate appeared to enhance PHB accumulation. Under the best conditions, PHB constituted up to 63% of dry cell mass after 12?h of culture. The average biomass yield coefficient on sucrose was about 0.35, or a little less than in batch fermentations. The highest PHB concentrations attained were about 18?g?·?l^?1.