Production of Rhamnolipid Biosurfactant by Fed-batch Culture of Pseudomonas aeruginosa Using Glucose as a Sole Carbon Source

The pH-stat fed-batch culture of Pseudomonas aeruginosa YPJ-80 was done to produce a rhamnolipid biosurfactant. With glucose as the sole carbon source, the final concentrations of cells and rhamnolipid biosurfactant obtained in 25 h were 25 g cell dry weight/l and 4.4 g/l, respectively.     

Production and characterisation of a biosurfactant isolated from Pseudomonas aeruginosa UW-1

Pseudomonas aeruginosa UW-1 produced 17–24 g L⁻¹ rhamnolipid in vegetable oil-containing media in shake flask cultures in 13 days. In time course studies of growth and rhamnolipid production in a salts medium containing 6% canola oil, total bacterial count reached 2.6 × 10¹⁰ CFU ml⁻¹ after 48 h and a maximum rhamnolipid yield of 24.3 g L⁻¹ was obtained after 9 days. Rhamnolipid components were purified and separated by chloroform-methanol extraction and TLC chromatography. The major rhamnolipid components were characterised as L-rhamnosyl-β-hydroxydecanoyl-β-hydroxydecanoate and L-rhamnosyl-L-rhamnosyl-β-hydroxydecanoyl-β-hydroxydecanoate by nuclear magnetic resonance and mass spectrometry. The components were separated preparatively by silica gel column chromatography. The recovered monorhamnosyl fraction contained no dirhamnosyl moiety while the recovered dirhamnosyl fraction contained 5% of the monorhamnosyl moiety when analyzed by HPLC. The ratio of mono- to dirhamnosyl components produced by P. aeruginosa UW-1 was determined by HPLC to be 4 : 1 by weight. Purified mono- and dirhamnosyl components had the same CMC value of 40 μg ml⁻¹ and decreased the surface tension of water to 27.7 and 30.4 dynes cm⁻¹, respectively. Received 04 April 1997/ Accepted in revised form 15 July 1997     

Stimulating in-soil rhamnolipid production in a bioslurry reactor by limiting nitrogen

A soil with aged contamination from lubricating oil (LO) and polychlorinated biphenyls (PCBs) was treated in a bioslurry reactor to investigate in-soil biosurfactant production by Pseudomonas aeruginosa, the most abundant indigenous, culturable, hydrocarbon-degrading microorganism. After 2 days of growth on LO, a depletion of nitrogen stimulated the production and accumulation of rhamnolipids to levels roughly 20 times the critical micelle concentration. Surface tensions and concentrations of monorhamnolipid and dirhamnolipid, PCBs, and total petroleum hydrocarbons (TPH) were measured in a slurry filtrate. Soil-bound PCBs and TPH were also quantified. Rhamnolipid production was observed within 1 to 2 days after nitrogen depletion in each of the 10 batches tested. By day 6, total rhamnolipid concentrations increased from below detection to average values over 1,000 mg/L, which caused over 98% of soil-bound PCBs and over 99% of TPH to be emulsified and recovered in the filtrate. After 70 days, rhamnolipid concentrations were only reduced by 15%, because of nitrogen-limited rates of rhamnolipid biodegradation. The results show that in-soil biosurfactant production can be stimulated in a controlled way with nutrient limitation and can be used to achieve soil washing.     

Demonstration of efficient trichloroethylene biodegradation in a hollow‐fiber membrane bioreactor

Rapid cometabolism of trichloroethylene (TCE) by pure cultures of Methylosinus trichosporium OB3b PP358 was demonstrated in a two‐stage hollow‐fiber membrane bioreactor over the course of 3 weeks. PP358 was grown in a continuous‐flow chemostat and circulated through the shell of a hollow‐fiber membrane module (HFMM), while TCE contaminated water (160 to 1450 μg/L) was pumped through the fiber lumen (fiber interior). In parallel‐flow HFMM biological experiments, 82% to 89% of the influent TCE was removed from the lumen (5.1‐min residence time) with 99% of the transferred TCE undergoing biodegradation. Biological experiments in a larger capacity baffled radial‐flow HFMM resulted in 66% to 99% TCE transferred and 93% to 96% TCE biodegradation at lumen residence times of between 1.5 and 3.7 min. Biodegradation was maintained throughout the experiments at pseudo‐first‐order biodegradation rate constants of 0.41 to 2.8 L/mg TSS/day. Best‐fit computer modeling of the baffled radial‐flow biological process estimated mass transfer coefficients as large as 2.7 × 10⁻² cm/min. The computer model was also shown to simulate the experimental results quite well. © 1999 John Wiley & Sons, Inc. Biotechnol Bioeng 62: 681–692, 1999.     

发酵碳源对铜绿假单胞菌NY3所产鼠李糖脂结构及性能的影响

为研究发酵碳源对铜绿假单胞菌NY3所产鼠李糖脂结构及性能的影响,从鼠李糖脂的结构组分、性能和应用效果等方面展开研究。薄层实验证明两种鼠李糖脂均含有单糖脂和双糖脂。液质分析发现以橄榄油作碳源时,鼠李糖脂中双糖脂(Rha-Rha-C5-C6:1和Rha-Rha-C8-C8:2)比例更大,约为73.09%。而地沟油作碳源时,单糖脂(Rha-C10-C10和Rha-C16-C16:2)的比例更高,约为76.91%。橄榄油和地沟油为碳源的鼠李糖脂的临界胶束浓度(CMC)分别为55 mg/L和80mg/L。相同投加量时,前者乳化性和乳化稳定性均优于后者。NY3菌降解含油污泥时,投加双糖脂含量高的鼠李糖脂会使C16-C30直链烷烃的去除率更高。     

Continuous rhamnolipid production with integrated product removal by foam fractionation and magnetic separation of immobilized Pseudomonas aeruginosa

Increasing interest in biological surfactants has led to intensified research directed at more cost-efficient production of biosurfactants, relative to traditional surface-active components based on petrochemical feedstocks. This publication will focus on a new integrated process for continuous rhamnolipid (RL) production. RL was synthesized by Pseudomonas aeruginosa DSM 2874 and was continuously removed in situ by foam fractionation. To prevent loss of the biocatalyst through foaming, bacteria were entrapped in magnetic alginate beads. Immobilizates were retained from the foam by high-gradient magnetic separation and back-flushed in the bioreactor at constant intervals. It was demonstrated that continuous RL production in a 10-L bioreactor over several cycles with intermediate growth periods is feasible. Complete separation of RLs from the production medium with an average enrichment ratio of 15 in the collapsed foam was demonstrated, yielding a final RL amount of 70 g after four production cycles.     

Evaluation of critical nutritional parameters and their significance in the production of rhamnolipid biosurfactants from Pseudomonas aeruginosa BS‐161R

Eleven biosurfactant producing bacteria were isolated from different petroleum‐contaminated soil and sludge samples. Among these 11 isolates, two were identified as promising, as they reduced the surface tension of culture medium to values below 27 mN m^?1. Besides biosurfactant production property, they exhibited good flocculating activity. Microbacterium sp. was identified as a new addition to the list of biosurfactant and bioflocculant‐producers. Optimization of various conditions for rhamnolipid production was carried out for one of the promising isolate, Pseudomonas aeruginosa BS‐161R. Bioglycerol (2.5%), as a cheap renewable carbon source, attained better rhamnolipid yield, while sodium nitrate appeared to be the preferable nitrogen source. The optimum carbon to nitrogen (C/N) and carbon to iron (C/Fe) ratios achieved were 15 and 28,350, respectively, which favored rhamnolipid production. Physical parameters like pH, temperature, and agitation speed also affected the production of rhamnolipids. Results from shake flask optimization indicated that the concentration of bioglycerol, sodium nitrate, and iron were the most significant factors affecting rhamnolipid production, which was supported by the results of central composite rotatable design. After optimization of the culture conditions, the production of rhamnolipids increased by ninefold from 0.369 to 3.312 g L^?1. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 2012     

Optimization and characterization of rhamnolipid production by Pseudomonas aeruginosa NY3 using waste frying oil as the sole carbon

Yield and cost are two major factors limiting the widespread use of rhamnolipids (RLs). In the present study, waste frying oil (WFO) was used as the sole carbon source to produce environmentally friendly RLs by Pseudomonas aeruginosa NY3. The Plackett–Burman design (PBD) and Box–Behnken design (BBD) methods were used to maximize the production yield of RL. The PBD results showed that the concentrations of NaNO₃, Na₂HPO₄, and trace elements were the key factors affecting the yield of RL. Furthermore, the BBD results showed that at NaNO₃, Na₂HPO₄, and trace elements concentrations were 4.95, 0.66, and 0.64 mL/L, respectively, the average RL yield reached 9.15 ± 0.52 g/L, 1.58-fold higher than that observed before optimization. Fourier transform infrared spectroscopy (FTIR) and liquid chromatography-ion trap-time of flight mass spectrometry (LCMS-IT-TOF) were used to elucidate the diversity of RL congeners. The results showed that, after optimization, the RL congener diversity increased, and the major RL constituent was converted from di-RLs (64.04%) to mono-RLs (60.44%). These results suggested that the concentrations of the components contained in the culture medium of P. aeruginosa NY3 influenced not only the yield of RL, but also its congener distribution.     

Continuous production of isovaleraldehyde through extractive bioconversion in a hollow-fiber membrane bioreactor

A membrane bioreactor was developed to perform an extractive bioconversion aimed at the production of isovaleraldehyde by isoamyl alcohol oxidation with whole cells of Gluconobacter oxydans. A liquid/liquid extractive system using isooctane as extractant and assisted by a hollow-fiber hydrophobic membrane was chosen to recover the product. The aqueous bioconversion phase and the organic phase were maintained apart with the aid of the membrane. The extraction of alcohol and aldehyde was evaluated by performing equilibrium and mass transfer kinetic studies. The bioprocess was then performed in a continuous mode with addition of the substrate to the aqueous phase. Fresh solvent was added to the organic phase and exhausted solvent was removed at the same flow rate. The extractive system enabled a fast and selective in situ removal of the aldehyde from the water to the organic phase. High conversions (72–90%) and overall productivity (2.0–3.0 g l⁻¹ h⁻¹) were obtained in continuous experiments performed with different rates of alcohol addition (1.5–3.5 g l⁻¹ h⁻¹). Cell deactivation was observed after 10–12 h of operation.     

铜绿假单胞菌产蛋白酶的发酵条件优化

【目的】鉴定一株来源于酱油曲能够分泌蛋白酶的铜绿假单胞菌CAU342A,优化其产蛋白酶的发酵条件。【方法】采用形态学观察、16S r RNA基因序列比对和生理生化方法鉴定菌株CAU342A;通过碳源、氮源、初始pH、温度、表面活性剂及发酵时间的单因素优化和正交试验获得最适发酵条件。【结果】菌株CAU342A被鉴定为铜绿假单胞菌(Pseudomonas aeruginosa),其最适发酵产酶条件为(质量体积比):3%酒糟,1.5%酵母浸提物,0.05%吐温-80,0.5%NaCl,0.7%K_2HPO_4,0.3%KH_2PO_4,0.04%MnSO_4,培养基初始pH 7.5,30°C培养72 h。在最适发酵条件下,该菌株最大产酶水平达到2 653.5 U/m L。蛋白酶酶谱分析表明该菌株能够产生至少4种具有蛋白酶活性的同工酶,其中两个主要酶谱带对应分子量分别为32 k D和50 k D。【结论】铜绿假单胞菌CAU342A高产蛋白酶,具有很大的工业应用潜力。     

Biosurfactant synthesis by Pseudomonas aeruginosa LBI isolated from a hydrocarbon-contaminated site

Aims: Pseudomonas aeruginosa LBI (Industrial Biotechnology Laboratory) was isolated from hydrocarbon-contaminated soil as a potential producer of biosurfactant and evaluated for hydrocarbon biodegradation. The emulsifying power and stability of the product was assessed in the laboratory, simulating water contamination with benzene, toluene, kerosene, diesel oil and crude oil at various concentrations. Methods and Results: Bacteria were grown at 30°C and shaken at 200 rpm for 168 h, with three repetitions. Surface tension, pH and biosurfactant stability were observed in the cell-free broth after 168 h of incubation. The strain was able to produce biosurfactant and grow in all the carbon sources under study, except benzene and toluene. When cultivated in 30% (w/v) diesel oil, the strain produced the highest quantities (9·9 g l⁻¹) of biosurfactant. The biosurfactant was capable of emulsifying all the hydrocarbons tested. Conclusion: The results from the present study demonstrate that Ps. aeruginosa LBI can grow in diesel oil, kerosene, crude oil and oil sludge and the biosurfactant produced has potential applications in the bioremediation of hydrocarbon-contaminated sites. Significance and Impact of the Study: Pseudomonas aeruginosa LBI or the biosurfactant it produces can be used in the bioremediation of environmental pollution induced by industrial discharge or accidental hydrocarbon spills.     

Swarming of Pseudomonas aeruginosa PAO1 without differentiation into elongated hyperflagellates on hard agar minimal medium

Polar flagellated Pseudomonas aeruginosa PAO1 demonstrated extensive spreading growth in 2 days on 1.5% agar medium. Such spreading growth of P. aeruginosa PAO1 strains was absent on Luria-Bertani 1.5% agar medium, but remarkable on Davis minimal synthetic agar medium (especially that containing 0.8% sodium citrate and 1.5% Eiken agar) under aerobic 37 degrees C conditions. Analyses using isogenic mutants and complementation transformants showed that bacterial flagella and rhamnolipid contributed to the surface-spreading behavior. On the other hand, a type IV pilus-deficient pilA mutant did not lose the spreading growth activity. Flagella staining of PAO1 T cells from the frontal edge of a spreading colony showed unipolar and normal-sized rods with one or two flagella. Thus, the polar flagellate P. aeruginosa PAO1 T appears to swarm on high-agar medium by producing biosurfactant rhamnolipid and without differentiation into an elongated peritrichous hyperflagellate.     

Pseudomonas aeruginosa PAO1 as a model for rhamnolipid production in bioreactor systems

Rhamnolipids are biosurfactants with interesting physico-chemical properties. However, the main obstacles towards an economic production are low productivity, high raw-material costs, relatively expensive downstream processing, and a lack of understanding the rhamnolipid production regulation in bioreactor systems. This study shows that the sequenced Pseudomonas aeruginosa strain PAO1 is able to produce high quantities of rhamnolipid during 30 L batch bioreactor cultivations with sunflower oil as sole carbon source and nitrogen limiting conditions. Thus PAO1 could be an appropriate model for rhamnolipid production in pilot plant bioreactor systems. In contrast to well-established production strains, PAO1 allows knowledge-based systems biotechnological process development combined with the frequently used heuristic bioengineering approach. The maximum rhamnolipid concentration obtained was 39 g/L after 90 h of cultivation. The volumetric productivity of 0.43 g/Lh was comparable with previous described production strains. The specific rhamnolipid productivity showed a maximum between 40 and 70 h of process time of 0.088 g_RL/g_BDMh. At the same time interval, a shift of the molar di- to mono-rhamnolipid ratio from 1:1 to about 2:1 was observed. PAO1 not only seems to be an appropriate model, but surprisingly has the potential as a strain of choice for actual biotechnological rhamnolipid production.     

Mapping of mutations affecting pyoverdine production in Pseudomonas aeruginosa

Abstract Pyoverdine, the yellow-green fluorescent pigment produced by Pseudomonas aeruginosa , is a highly efficient siderophore. Pyoverdine-deficient ( pvd ) mutants of P. aeruginosa PAO isolated after mutagenesis were non-fluorescent and unable to grow in the presence of 2.8 mM ethylenediamine-di-( o -hydroxyphenylacetate) (EDDHA). Addition of purified pyoverdine to media containing EDDHA restored growth of pvd mutants. 6 pvd mutations were mapped between catA and mtu -9002 (at 65–70 min on the chromosome map) by R68.45-mediated conjugation. 2 slightly leaky pvd mutations were localised between argC and strA (at 35 min) by transduction. Thus, we have identified at least 2 genes or gene clusters required for pyoverdine production in P. aeruginosa .