Inhibition kinetics of phenol degradation from unstable steady-state data

Multiplicity of steady states of a continuous culture with an inhibitory substrate was used to estimate kinetic parameters under steady-state conditions. A continuous culture of Pseudomonas cepacia G4, using phenol as the sole source of carbon and energy, was overloaded by increasing the dilution rate above the critical dilution rate. The culture was then stabilized in the inhibitory branch by a proportional controller using the carbon dioxide concentration in the reactor exhaust gas as the controlled variable and the dilution rate as the manipulated variable. By variation of the set point, several unstable steady states in the inhibitory branch were investigated and the specific phenol conversion rates calculated. In addition, phenol degradation was investigated under substrate limitation (chemostat operation).The results show that the phenol degradation by P. cepacia can be described by the same set of inhibition parameters under substrate limitation and under high substrate concentrations in the inhibitory branch. Biomass yield and maintenance coefficients were identical. Fitting of the data to various inhibition models resulted in the best fit for the Yano and Koga equation. The well-known Haldane model, which is most often used to describe substrate inhibition by phenol, gave the poorest fit. The described method allows a precise data estimation under steady-state conditions from the maximum of the biological reaction rate up to high substrate concentrations in the inhibitory branch. Inhibition parameter estimation by controlling unstable steady states may thus be useful in avoiding discrepancies between data generated by batch runs and their application to continuous cultures which have been often described in the literature. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54: 567-576, 1997.     

Biodegradation of Phenol by Actinobacillus Sp.: Mathematical Interpretation and Effect of Some Growth Conditions

Models of the cultivation process of Actinobacillus sp. cells in two media, rich (NB) and minimal (M9) that includes phenol as a sole carbon source, have not been described in the available literature. For these reasons, several single-substrate inhibition models (Monod, Andrew, and Tesseir) were investigated in order to determine the mathematical expression of Actinobacillus sp. growth rate. The experimental data for both nutrient broth and M9 media were fitted to the above models mentioning that Andrews' model best fits these data adequately for both media with regression coefficient of 0.973 and 0.962, respectively. The maximum predicted growth rate by this model is 0.37 h^{- 1} for both media obtained when the initial concentration of phenol is 100 mg/L. The half-saturation concentration constant, K_P, is 1.00 mg/L, which represents the phenol concentration when μ is equal to half μ_max. On the other hand, the inhibition constant, K_p is 13,000.00 mg/L for broth medium and 12,000 mg/L for M9 medium, which is a measure of sensitivity to inhibition by inhibitory substances. When cells are grown in nutrient broth and minimal media, the rate of cell production with time can be expressed by the Reccati and Voltera models. Voltera model better fits in the case of M9 minimal medium plus phenol as sole carbon source. The pH of 7, the incubation temperature of 35°C to 37°C, and the agitation rate of 150 rpm are the optimal conditions for achieving the higher percentage of phenol degradation by Actinobacillus sp. Succinic acid and glycine as carbon and nitrogen source, respectively, were the most efficient of the cosubstrates (out of 10 substrates tested) for removal of phenol on an mg/L basis.     

Biodegradation of phenol and chlorophenols with defined mixed culture in shake-flasks and a packed bed reactor

Pseudomonas testosteroni CPW301 degraded phenol and 4-chlorophenol simultaneously, but degradation rates of these compounds were affected by 4-chlorophenol. Phenol increased the cell concentration and therefore the degradation efficiency of 4-chlorophenol was improved. Pseudomonas solanacearum TCP114 could degrade only 2,4,6-trichlorophenol. A defined mixed culture of P. testosteroni CPW301 and P. solanacearum TCP114 could treat phenol, 4-chlorophenol, and 2,4,6-trichlorophenol completely and overcome the inhibition of substrates to other microorganisms. The degradation capacity of the packed bed reactor (PBR) was higher than that of the continuous stirred tank reactor, but the PBR was unsuitable for oxygen-sensitive microorganisms.     

The coupling between catabolism and anabolism of Methanobacterium thermoautotrophicum in H2- and iron-limited continuous cultures

The aim of the present work was to investigate whether uncoupling of catabolism from anabolism, which was often observed in heterotrophic microorganisms under energy-sufficient growth conditions, also occurs in the autotrophic bacterium Methanobacterium thermoautotrophicum. For this purpose, M. thermoautotrophicum was cultivated in continuous cultures that were limited by the trace element iron. The influences of both dilution rate and iron supply rate on the coupling between anabolism and catabolism were investigated. As compared to continuous cultures of M. thermoautotrophicum limited by the energy substrate H₂, a 5-fold decrease in the biomass concentration and a 3-fold decrease in H₂, CO₂, and CH₄ conversion rates were observed in iron-limited cultures. However, the specific substrate and product conversion rates increased as compared to the values determined in energy-limited cultures. Thus, iron limitation provoked an uncoupling of catabolism from anabolism. At a dilution rate of 0.096 h⁻¹ and at an iron concentration of 17 μM in the feed, the specific H₂ consumption rate was 100% higher than the rate determined under H₂-limiting conditions, whereas at a dilution rate of 0.168 h⁻¹, the values differed only by 5%. Uncoupling of catabolism from anabolism also increased dramatically when the iron supply rate was lowered but the dilution rate was kept constant. Thus, the extent of uncoupling is a function of both the dilution rate and the iron supply rate. It was found that the specific consumption rate of H₂ increased in parallel with the partial pressure of H₂ in the culture medium. This suggested that the catabolic activity of M. thermoautotrophicum was not stringently controlled at the enzymatic level and can be considerably stimulated by the excess of H₂ in the medium. Hypotheses as to the fate of the excess energy derived from uncoupled catabolism are discussed, but the physiological reason for the partial uncoupling between catabolism and anabolism remains yet to be clarified.     

Phenolics and antimicrobial activity of traditional stoned table olives 'alcaparra'

In the present work, we report the determination of phenolic compounds in ‘alcaparra’ table olives by reversed-phase HPLC/DAD, and the evaluation of their extract in vitro activity against several microorganisms that may be causal agents of human intestinal and respiratory tract infections, namely Gram positive (Bacillus cereus, Bacillus subtilis, and Staphylococcus aureus), Gram negative bacteria (Pseudomonas aeruginosa, Escherichia coli, and Klebsiella pneumoniae) and fungi (Candida albicans and Cryptococcus neoformans). Three flavonoidic compounds were identified and quantified: luteolin 7-O-glucoside, apigenin 7-O-glucoside, and luteolin. At low concentrations (0.05 mg/mL) ‘alcaparra’ extract revealed significant inhibition of both Gram positive and Gram negative bacteria growth, with exception of P. aeruginosa. Nevertheless, no antifungal activity was observed at the tested concentrations.     

Assessment of the antibacterial activity of selected flavonoids and consideration of discrepancies between previous reports

Activity of the flavonoids apigenin, baicalin and galangin against sensitive and antibiotic resistant strains of Staphylococcus aureus, Enterococcus faecalis, E. faecium, Escherichia coli and Pseudomonas aeruginosa was investigated. Using an agar dilution assay, galangin was shown to have a minimum inhibitory concentration (MIC) of 25 to 50 μg/mL against all six strains of S. aureus but negligible activity against the other species. Apigenin displayed only marginal activity against S. aureus and no activity was detected from baicalin. In inhibition curve studies, galangin caused a 100,000-fold decrease in the viability of a growing population of S. aureus NCTC 6571 within the first two hours of treatment. Decreases in viability of S. aureus NCTC 11561 and NCIMB 9968 populations were also observed.     

Some effects of growth conditions on steady state and heat shock induced htpG gene expression in continuous cultures of Escherichia coli

Most of the data concerning heat shock gene expression reported in the literature are derived from batch culture experiments under substrate and nutrient sufficient conditions. Here, the effects of dilution rate and medium composition on the steady state and heat shock induced htpG gene expression have been investigated in continuous cultures of Escherichia coli, using a chromosomal htpG-lacZ gene fusion. During steady state growth temperature dependent patterns of the relative htpG expression were found to be largely similar, irrespective of the growth condition. However, nitrogen-limited growth resulted in a markedly reduced specific steady state htpG expression as compared to growth under carbon limitation or in complex medium, correlating qualitatively with the total cellular protein content. During heat shock, tight temperature controlled expression was evident. While the relative heat shock induced expression was largely identical at various dilution rates in a given growth medium, significantly different response patterns were observed in the three growth media at any give dilution rate. From these results a clearly temperature regulated htpG expression during both, steady and transient state growth in continuous culture is evident, which is further significantly affected by the growth condition used.     

Kinetic studies of constitutive human granulocyte-macrophage colony stimulating factor (hGM-CSF) expression in continuous culture of <Emphasis Type="Italic">Pichia pastoris</Emphasis>

Extracellular human granulocyte-macrophage colony stimulating factor (hGM-CSF) expression was studied under the control of the GAP promoter in recombinant Pichia pastoris in a series of continuous culture runs (dilution rates from 0.025 to 0.2 h⁻¹). The inlet feed concentration was also varied and the steady state biomass concentration increased proportionally demonstrating efficient substrate utilization and constancy of the biomass yield coefficient (Y_x/s) for a given dilution rate. The specific product formation rate (q_P) showed a strong correlation with dilution rates demonstrating growth associated product formation of hGM-CSF. The volumetric product concentration achieved at the highest feed concentration (4×) and a dilution rate of 0.2 h⁻¹ was 82 mg l⁻¹ which was 5-fold higher compared to the continuous culture run with 1× feed concentration at the lowest dilution rate thus translating to a 40 fold increase in the volumetric productivity. The specific product yield (Y_P/X) increased slightly from 2 to 2.5 mg g⁻¹, with increasing dilution rates, while it remained fairly invariant, for all feed concentrations demonstrating negligible product degradation or feed back inhibition. The robust nature of this expression system would make it easily amenable to scale up for industrial production.     

Anaerobic degradation of phenol in batch and continuous cultures by a denitrifying bacterial consortium

Summary The anaerobic degradation of phenol under denitrifying conditions by a bacterial consortium was studied both in batch and continuous cultures. Anaerobic degradation was dependent on NO_f3 ^p– and concentrations up to 4 mm phenol were degraded within 2–5 days. During continuous growth in a fermenter, steady states could be maintained at eight dilution rates (D) corresponding to residence times between 12.5 and 50 h. Culture wash-out occurred at D=0.084 h^–1. The kinetic parameters obtained for anaerobic degradation of phenol under denitrifying conditions by the consortium were: maximam specific growth rate = 0.091 h^–1; saturation constant = 4.91 mg phenol/l; true growth yield = 0.57 mg dry wt/mg phenol; maintenance coefficient = 0.013 mg phenol/mg dry wt per hour. The Haldane model inhibition constant was estimated from batch culture data giving a value of 101 mg/l. The requirement of CO₂ for the anaerobic degradation of phenol with NO_f3 ^p– indicates that phenol carboxylation to 4-hydroxybenzoate was the first step of phenol degradation by this culture. 4-Hydroxybenzoate, proposed as an intermediate of phenol carboxylation under these conditions, was detected only in continuous cultures at very low growth rates (D=0.02 h^–1), but was never detected as a free intermediary metabolite either in batch or in continuous cultures. Correspondence to: N. Khoury     

Actual and potential rates of substrate oxidation and product formation in continuous cultures ofChromatium vinosum

Kinetics of electron-donor oxidation, storage-polymer formation and growth were studied in continuous cultures ofChromatium under conditions of balanced growth as well as during transient states.Under steady-state conditions, glycogen was accumulated at all dilution rates. This observation is consistent with previously postulated ideas about an ineffective glycogen-synthesis regulation.Upon perturbing the steady states, brought about by injection of extra sulfide into steady-state cultures, the following phenomena were observed immediately, irrespective of the dilution rate: the specific rate of sulfide oxidation increased to the value found in batch cultures, the sulfur-oxidation rate was decreased, the specific glycogen-synthesis rate increased, the increment being higher the lower the dilution rate, but an increase in the specific growth rate, if any, was below the limit of detection. The inverse relationship between the specific rates of glycogen synthesis and growth after removing the substrate limitation is to be explained by a shortage of intermediates, rather than by a growth-rate dependent intrinsic glycogen-synthesis limitation, because upon complete inhibition of growth a further increase in the rate of glycogen synthesis was observed. Essayed in this way, identical glycogen-synthesis rates were found at all dilution rates.Competitive advantages of such an apparently not adapted metabolism in environments with diurnal fluctuations in substrate concentrations are discussed.Non-Standard Abbreviations N_c cell nitrogen - TS total sugar - PHB poly--hydroxybutyrate - D dilution rate - S_R reservoir concentration of the growth-limiting substrate - CAP chloramphenicol     

Dynamics and stability analysis of the growth and astaxanthin production system of Haematococcus pluvialis

This paper investigated high cell density cultivation of Haematococcus pluvialis for astaxanthin production in 3.7-L bioreactors. A biomass concentration of 2.74 g L⁻¹and an astaxanthin yield of 64.4 mg L⁻¹ were obtained. Based on the experimental results, a new and simple dynamic model is proposed, differing from Monod kinetics, to describe cell growth, product formation and substrate consumption. Good agreement was found between the model predictions and experimental data. The model revealed that there was cell growth inhibition on product formation and product feedback compensation for substrate consumption, but no substrate inhibition or product inhibition of cell growth. Stability analysis demonstrated that no multiplicity of steady states was observed; the unique positive steady state was locally asymptotically stable; and the effect of dilution rate on steady states was greater than that of the initial substrate concentration. Received 23 February 1999/ Accepted in revised form 08 June 1999     

Molecular characterization and properties of (R)-specific enoyl-CoA hydratases from Pseudomonas aeruginosa: metabolic tools for synthesis of polyhydroxyalkanoates via fatty acid beta-oxidation

The use of (R)-specific enoyl-coenzyme A (CoA) hydratase (PhaJ) provides a powerful tool for polyhydroxyalkanoate (PHA) synthesis from fatty acids or plant oils in recombinant bacteria. PhaJ provides monomer units for PHA synthesis from the fatty acid ß-oxidation cycle. Previously, two phaJ genes (phaJ1_Pa and phaJ2_Pa) were identified in Pseudomonas aeruginosa. This report identifies two new phaJ genes (phaJ3_Pa and phaJ4_Pa) in P. aeruginosa through a genomic database search. The abilities of the four PhaJ_Pa proteins and the (R)-3-hydroxyacyl-acyl carrier protein [(R)-3HA-ACP] dehydrases, FabA_Pa and FabZ_Pa, to supply monomers from enoyl-CoA substrates for PHA synthesis were determined. The presence of either PhaJ1_Pa or PhaJ4_Pa in recombinant Escherichia coli led to the high levels of PHA accumulation (as high as 36–41 wt.% in dry cells) consisting of mainly short- (C4–C6) and medium-chain-length (C6–C10) 3HA units, respectively. Furthermore, detailed characterizations of PhaJ1_Pa and PhaJ4_Pa were performed using purified samples. Kinetic analysis revealed that only PhaJ4_Pa exhibits almost constant maximum reaction rates (V_max) irrespective of the chain length of the substrates. The assay for stereospecific hydration revealed that, unlike PhaJ1_Pa, PhaJ4_Pa has relatively low (R)-specificity. These hydratases may be very useful as monomer-suppliers for the synthesis of designed PHAs in recombinant bacteria.     

The use of multi-parameter flow cytometry to study the impact of limiting substrate, agitation intensity, and dilution rate on cell aggregation during Bacillus licheniformis CCMI 1034 aerobic continuous culture fermentations

The main objective of this work was to establish those factors either physical (power input) or chemical (limiting substrate or dilution rate) that enhance cell aggregation (biofilm or floc formation) and cell physiological state during aerobic continuous cultures of Bacillus licheniformis. Glucose-limited steady-state continuous cultures growing at a dilution rate between 0.64 and 0.87/h and 1,000 rpm (mean specific energy dissipation rate (epsilonT) = 6.5 W/kg), led to the formation of a thin biofilm on the vessel wall characterized by the presence of a high proportion of healthy cells in the broth (after aggregate disruption by sonication) defined as having intact polarized cytoplasmic membranes. An increased epsilonT (from 6.5 W/kg to 38 W/kg) was found to hinder cell aggregation under carbon limitation. The carbon recovery calculated from glucose indicated that additional extracellular polymer was being produced at dilution rates >0.87/h. B. licheniformis growth under nitrogen limitation led to floc formation which increased in size with dilution rate. Counter-intuitively the flocs became more substantial with an increase in epsilonT from 6.5 W/kg to 38 W/kg under nitrogen limitation. Indeed the best culture conditions for enhanced metabolically active cell aggregate formation was under nitrogen limitation at epsilonT = 6.5 W/kg (leading to floc formation), and under carbon limitation at a dilution rate of between 0.64 and 0.87/h, at epsilonT = 6.5 W/kg (leading to vessel wall biofilm formation). This information could be used to optimize culture conditions for improved cell aggregation and hence biomass separation, during thermophilic aerobic bioremediation processes.     

Continuous microalgae cultivation in a photobioreactor

New biomass sources for alternative fuels has become a subject of increasing importance as the nation strives to resolve the economic and strategic impacts of limited fossil fuel resources on our national security, environment, and global climate. Algae are among the most promising non‐food‐crop‐based biomass feedstocks. However, there are currently no commercially viable microalgae‐based production systems for biofuel production that have been developed, as limitations include less‐than optimal oil content, growth rates, and cultivation techniques. While batch studies are critical for determining basic growth phases and characteristics of the algal species, steady‐state studies are necessary to better understand and measure the specific growth parameters. This study evaluated the effects of dilution rate on microalgal biomass productivity, lipid content, and fatty acid profile under steady‐state conditions with continuous illumination and carbon dioxide supplemention for two types of algae. Continuous cultures were conducted for more that 3 months. Our results show that the productivity of Chlorella minutissima varied from 39 to 137 mg/L/day (dry mass) when the dilution rate varied from 0.08 to 0.64 day^?1. The biomass productivity of C. minutissima reached a maximum value (137 mg/L/day) at a dilution rate of 0.33 day^?1, while the productivity of Dunaliella tertiolecta varied from 46 to 91 mg/L/day at a dilution rate of 0.17 to 0.74 day^?1. The biomass productivity of D. tertiolecta reached a maximum value of 91 mg/L/day at a dilution rate of 0.42 day^?1. Moreover, the lipid content had no significant change with various dilution rates. Biotechnol. Bioeng. 2012; 109: 2468–2474. © 2012 Wiley Periodicals, Inc.     

Production of the antitumoral retamycin during continuous fermentations of Streptomyces olindensis

Continuous fermentations were performed in order to correlate the production of retamycin, an anthracycline antibiotic produced by Streptomyces olindensis in submerged cultures, with the dilution rate. Maximum retamycin production was achieved at a dilution rate of 0.05 h⁻¹ (D=μ_x=0.05 h⁻¹), while higher dilution rates caused a decrease in antibiotic production, which ceased completely at a dilution rate of 0.30 h⁻¹. Otherwise, biomass productivity was favoured by high dilution rates, achieving a maximum at D=0.25 h⁻¹, whereas retamycin productivity reached a maximum at D=0.05 h⁻¹. Dilution rate influenced morphology, which was assessed by image analysis. The percentage of clumps decreased with an increase in dilution rate, with a correspondent increase in pellet percentage.     

A biochemically structured model for Saccharomyces cerevisiae.

A biochemically structured model for the aerobic growth of Saccharomyces cerevisiae on glucose and ethanol is presented. The model focuses on the pyruvate and acetaldehyde branch points where overflow metabolism occurs when the growth changes from oxidative to oxido-reductive. The model is designed to describe the onset of aerobic alcoholic fermentation during steady-state as well as under dynamical conditions, by triggering an increase in the glycolytic flux using a key signalling component which is assumed to be closely related to acetaldehyde. An investigation of the modelled process dynamics in a continuous cultivation revealed multiple steady states in a region of dilution rates around the transition between oxidative and oxido-reductive growth. A bifurcation analysis using the two external variables, the dilution rate, D, and the inlet concentration of glucose, S(f), as parameters, showed that a fold bifurcation occurs close to the critical dilution rate resulting in multiple steady-states. The region of dilution rates within which multiple steady states may occur depends strongly on the substrate feed concentration. Consequently a single steady state may prevail at low feed concentrations, whereas multiple steady states may occur over a relatively wide range of dilution rates at higher feed concentrations.     

The effect of iron-hexacyanide binding on the determination of redox potentials of cytochromes and copper proteins

The midpoint redox potentials of Pseudomonas aeruginosa cytochrome c-551 and Rhodopseudomonas viridis cytochrome c₂ were measured as a function of pH in the presence of Euglena cytochrome c-558 and the results compared with those obtained in the presence of ferro-ferricyanide. The pattern of pH dependence observed for the two bacterial cytochromes was the same whether it was measured by equilibrium with another redox protein or with the inorganic redox couple. Thus, the pH dependence of redox potential is not a consequence of pH-dependent ligand binding. The midpoint potential of Ps. aeruginosa azurin was measured as a function of pH using both ferro-ferricyanide mixtures and redox equilibrium with horse cytochrome c or Rhodopseudomonas capsulata cytochrome c₂. In this case also the pattern of pH dependence obtained did not vary with the redox system used and it closely resembled that of Ps. aeruginosa cytochrome c-551. This is consistent with the observation that the equilibrium between cytochrome c-551 and azurin is relatively independent of pH. An equation was derived which described pH-dependent ligand binding and which can produce theoretical curves to fit the experimental pH dependence of redox potential for both cytochrome and azurin. However, the pronounced effect on such curves produced by varying the ligand association constants, and the insensitivity of the experimental data to changes in ionic strength, suggest that ligand binding effects do not account for the pH dependence of redox potential.     

蛹虫草多糖和D-甘露醇深层发酵的非结构动力学模型

多糖和D-甘露醇是蛹虫草的重要药理活性成分。本文开展了蛹虫草在分批发酵过程中同时生产多糖和D-甘露醇的发酵动力学研究。利用Sigmoid函数构建了蛹虫草菌丝生长、糖基质消耗、多糖和D-甘露醇的非结构动力学模型,并根据Boltzmann方程拟合求解出各模型参数。结果显示,各模型的实测值和预测值拟合度较好。蛹虫草比生长速率在第1.0天达到最大值（μ_max）1.244d^-1;底物葡萄糖的比消耗速率在第0.6天达到最大值（q_{S, max}）2.163d^-1;多糖比合成速率在第2.0天达到最大值（q_{P, max}）51.852mg/(g·d);D-甘露醇比合成速率在第0.99天左右达到最大值（q_{D, max}）37.963mg/(g·d)。蛹虫草多糖的形成与菌丝细胞的生长呈现部分生长关联型,而D-甘露醇的形成与细胞生长呈现生长关联型关系。研究结果为利用分批发酵规模化同时发酵生产蛹虫草多糖和D-甘露醇提供了理论依据。     

超声波对铜绿微囊藻与蛋白核小球藻生理特征及竞争生长的影响

铜绿微囊藻是常见的水华蓝藻,常常在湖泊中与蛋白核小球藻共存或竞争生长。超声波可用于藻华即时治理,能够降低藻类生理活性,影响藻类生长,还可能改变藻类种间竞争关系。为了探究超声胁迫(35 kHz,0.035 W·cm^-3)对铜绿微囊藻与蛋白核小球藻的生理特征及种间竞争的影响,本研究设置纯藻组和1:1混合组(细胞浓度比)进行试验。结果表明: 铜绿微囊藻对超声胁迫更加敏感。超声处理600 s后,铜绿微囊藻的光合活性(F_v/F_m)和酯酶活性存在显著变化,纯藻组和混合组的F_v/F_m分别降低了51.8%和64.7%。而各组中蛋白核小球藻的光合活性变化较小。同时,铜绿微囊藻释放的荧光溶解性有机物(类色氨酸、类酪氨酸、类富里酸物质)含量多于蛋白核小球藻。两种藻的细胞浓度对超声波的响应也不同,蛋白核小球藻变化较小,而铜绿微囊藻的细胞浓度出现不同程度的下降。尤其是600 s超声处理大幅降低了混合组中铜绿微囊藻的细胞浓度(-42.6%),在超声胁迫解除后的8 d内蛋白核小球藻占优势,种间关系由铜绿微囊藻单边抑制蛋白核小球藻转变为两者互相抑制。在超声处理后,铜绿微囊藻的活性能够逐渐恢复,为了提高控藻效果的持久性,建议在一周后再次进行超声处理。     

Specific ratio and survival of Pseudomonas CF600 as co-culture for phenol degradation in continuous cultivation

Studies were carried out to understand parallel survival of two strains when cultivated as co-culture on a single carbon source in continuous cultivation. Strains used were Pseudomonas sp. strain CF600 that is reported for degradation of phenol; and HKR1 a lab strain, which was isolated from a site contaminated with phenol. In continuous cultivation Pseudomonas sp. CF600 showed an accumulation of colored intermediate, 2-hydroxy muconic semialdehyde (HMS), when fed with phenol as a sole source of carbon under dissolved oxygen limiting condition (40% saturation level). Under the same cultivation condition when it was co-cultured with strain HKR1, complete degradation of phenol was observed with no accumulation of intermediate. Different dilution rates (0.03, 0.15, and 0.30) were set in the bioreactor during cultivation. It was also observed that both the strains follow a typical cell density ratio of 1:18 as strain HKR1: Pseudomonas sp. CF600 irrespective of the dilution rates used in the study to favor degradation of phenol. Pseudomonas sp. CF600 is reported to degrade phenol via a plasmid-encoded pathway (pVI150). The enzymes for this meta-cleavage pathway are clustered on 15 genes encoded by a single operon, the dmp operon. PCR using primers from the different catabolic loci of dmp operon, demonstrated that the strain HKR1 follows a different metabolic pathway for intermediate utilization.