Biodegradation of phenol and cresol isomer mixtures by Arthrobacter

The Arthrobacter species can degrade phenol, o-cresol and p-cresol much faster (as reflected in high specific growth rates) than other microbes which are reported to degrade toxic compounds. In mixtures, phenol and p-cresol mutually inhibited each other; the inhibition constants show that phenol degradation is strongly inhibited in the presence of p-cresol rather than reverse. o-Cresol enhanced phenol degradation marginally but o-cresol degradation was not affected by the presence of phenol.     

The adsorption of Fusarium flocciferum spores on celite particles and their use in the degradation of phenol

Summary Spores of Fusarium flocciferum were inserted in porous celite beads. The effects of bead size, adsorption time course, washing cycle and spore concentration on spore loading were investigated. Cell loadings up to 50% (dry weight/beads) were obtained. The degradation of phenol using adsorbed cells was studied in batch experiments. The immobilized cell system was shown to efficiently degrade high concentrations of the substrate (up to 2.0 g/l) and to remain active for more than 2 motths. The oxygen uptake rate of free and immobilized cells was determined at various concentrations of phenol. The kinetic constants K _s=85 mg/l, K _i=345 mg/l and SMI=170 mg/l were estimated from the experimental data by linearization of the Haldane function for the free cells. The uptake rates exhibited by the confined cells were lower (30%) than those obtained for free cells and no significant differences were found for phenol concentrations between 150 and 1200 mg/l.     

Degradation of phenol and phenolic compounds by a defined denitrifying bacterial culture

Phenol, a major pollutant in several industrial waste waters is often used as a model compound for studies on biodegradation. This study investigated the anoxic degradation of phenol and other phenolic compounds by a defined mixed culture of Alcaligenes faecalis and Enterobacter species. The culture was capable of degrading high concentrations of phenol (up to 600 mg/l) under anoxic conditions in a simple minimal mineral medium at an initial cell mass of 8 mg/l. However, the lag phase in growth and phenol removal increased with increase in phenol concentration. Dissolved CO₂ was an absolute requirement for phenol degradation. In addition to nitrate, nitrite and oxygen could be used as electron acceptors. The kinetic constants, maximum specific growth rate _max; inhibition constant, K _i and saturation constant, K _s were determined to be 0.206 h^–1, 113 and 15 mg phenol/l respectively. p-Hydroxybenzoic acid was identified as an intermediate during phenol degradation. Apart from phenol, the culture utilized few other monocyclic aromatic compounds as growth substrates. The defined culture has remained stable with consistent phenol-degrading ability for more than 3 years and thus shows promise for its application in anoxic treatment of industrial waste waters containing phenolic compounds.     

Feasibility study of exponential feeding strategy in fed-batch cultures for phenol degradation using Cupriavidus taiwanensis

An indigenous phenol-degrading bacterial isolate Cupriavidus taiwanensis R186 was used to degrade phenol from an aqueous solution under fed-batch operation. An exponential feeding strategy combined with dissolved oxygen control was applied based on kinetic characteristics of cell growth and phenol degradation to meet sufficient metabolic needs for cellular growth and achieve the best phenol removal efficiency. Without the stress of phenol inhibition, the optimal set point of specific growth rate of exponential feeding for fed-batch phenol degradation was found to be 0.50–0.55μ_max (μ_max denotes the maximum specific growth rate from Monod model). Meanwhile, the sufficient set point of dissolved oxygen for maximal phenol degradation efficiency was approximately at 10–55% air saturation. With the optimal operation conditions, the best phenol degradation rate was 0.213 g phenol h⁻¹, while a shortest treatment time of 15 h was achieved for complete degradation of 11.35 mM (ca. 3.20 g) of phenol.     

Degradation kinetics of phenol by immobilized cells of Candida tropicalis in a fluidized bed reactor

Degradation kinetics of phenol by free and agar-entrapped cells of Candida tropicalis was studied in batch cultures. The initial phenol degradation rate achieved with free cells was higher than that obtained with immobilized cells, when phenol concentrations up to 1000 mg l^–1 were used. However, at higher phenol concentrations, the behaviour was quite different. The initial degradation rate of the immobilized yeast cells was about 10 times higher than that of the free cells, at a phenol concentration of 3500 mg l^–1. The semicontinuous and continuous degradation of phenol by immobilized yeast cells was also investigated in a multi-stage fluidized bed reactor. The highest phenol removal efficiencies and degradation rates as well as the lowest values of residual phenol and chemical oxygen demand were obtained in the semicontinuous culture when phenol concentrations up to 1560 mg l^–1 were used.     

Continuous aerobic phenol degradation by defined mixed immobilized culture in packed bed reactors

A defined mixed culture of Pseudomonas putida, Commamonas testosteroni and Candida tropicalis was immobilized by adsorption on polyurethane foam, cocoa-fibers, expanded slate and sintered glass. Packed bed reactors were used for long-term continuous phenol biodegradations. Loading experiments were done to study the impact of the following parameters: (1) hydraulic retention time, (2) dissolved oxygen concentration, and (3) elimination of the oxygen limitation. After the acclimation period (approximately 10 d), the loading test with the individual packings showed the following maximum degradation rates: sintered glass 34, polyurethane foam 12, expanded slate 11.5, and cocoa-fibers 7.7 kg m(-3) d(-1). All these values were reached at a removal efficiency >99 % and with oxygen in excess. Under these conditions, the pH of the diluted unbuffered medium in the reactor effluent was 3.2-4.0 and no incompletely oxidized metabolic intermediates were found. The free cell concentration in the effluent increased after the phenol overloading time period.     

KINETICS OF NUTRIENT UPTAKE AND GROWTH IN PHYTOPLANKTON1

Microscopic algae can grow rapidly in natural waters that are extremely low in essential macro and micro nutrients. Yet, their nutrient uptake systems exhibit only mediocre nutrient affinities, the saturation constants being often 10–1000 times the (estimated) ambient concentrations. The large difference which exists between the saturation constants for growth (K_u) and short term uptake (K_p) are due to the acclimation capabilities of the organisms. Over the acclimation range, K_u, to K_p the algae can maintain maximum growth rate by modulating both their internal nutrient quotas (Q) and their maximum short term nutrient uptake rates (P_max) in response to variations in external nutrient concentrations. The commonly assumed hyperbolic relationships for steady growth and uptake (viz “chemostat theory”) are coherent with a hyperbolic expression for short term uptake including a variable maximum (P_max). The ratio of the saturation constants for growth and uptake is then directly related to the extreme in quotas and maximum uptake rates: K^μ/K^ρ= Q^min/Q^maxρ^max/ρQ^max. This result is applicable even when the exact hyperbolic laws are not. Published data on Fe, Mn, P and N limitation in algae are generally in accord with the theory and demonstrate a wider acclimation range for trace than for major nutrients.     

Influence of phenol on biodegradation of p-nitrophenol by freely suspended and immobilized Nocardioides sp. NSP41

The effect of the presence of an alternate toxiccompound (phenol) on the p-nitrophenol(PNP)-degrading activity of freely suspended andcalcium alginate immobilized Nocardioides sp.NSP41 was investigated. In the single substrateexperiments, when the concentration of phenol and PNPwas increased to 1400 mg l^-1 and 400 mg l^-1,respectively, the initial cell concentrations in thefreely suspended cell culture should be higher than1.5 g dry cell weight l^-1 for completedegradation. In the simultaneous degradationexperiment, when the initial concentration of phenolwas increased from 100 to 400 mg l^-1, thespecific PNP degradation rate at the concentration of200 mg l^-1 was decreased from 0.028 to 0.021h^-1. A freely suspended cell culture with a highinitial cell concentration resulted in a highvolumetric degradation rate, suggesting the potentialuse of immobilized cells for simultaneous degradation.In the immobilized cell cultures, althoughsimultaneous degradation of PNP and phenol wasmaintained, the specific PNP and phenol degradationrate decreased. However, a high volumetric PNP andphenol degradation rate could be achieved byimmobilization because of the high cell concentration.Furthermore, when the immobilized cells were reused inthe simultaneous degradation of PNP and phenol, theydid not lose their PNP- and phenol-degrading activityfor 12 times in semi-continuous cultures. Takentogether, the use of immobilized Nocardioidessp. NSP41 for the simultaneous degradation of PNP andphenol at high concentrations is quite feasiblebecause of the high volumetric PNP and phenoldegradation rate and the reusability of immobilizedcells.     

Biotransformation kinetics of Pseudomonas putida for cometabolism of phenol and 4-chlorophenol in the presence of sodium glutamate

A kinetic model to describe the degradation of phenol and cometabolictransformation of 4-chlorophenol (4-cp) in the presence of sodium glutamate(SG) has been developed and validated experimentally. The integrated modelaccounts for cell growth, toxicity of 4-cp, cross-inhibitions among the threesubstrates, and the different roles of the specific growth substrate (phenol)and the conventional carbon source (SG) in the cometabolism of 4-cp. In thisternary substrate system, the overall phenol degradation and 4-cp transformation rates are greatly enhanced by the addition of SG since SG is able to attenuate the toxicity of 4-cp and therefore increase the cell growth rate. Model analysis indicates that the maximum specific degradation rate of phenol (0.819 mg (mg.h)^-1) is lowered by SG by up to 46% whereas the specific transformation rate of 4-cp is notdirectly affected by the presence of SG. The competitive inhibition coefficient of 4-cp to phenol degradation (K_i,cp) and that of phenol to 4-cp transformation (K_i,ph) were determined to be 6.49 mg l^-1 and 0.193 mg l^-1, respectively, indicatingthat phenol imposes much larger competitive inhibition to 4-cp transformation than the converse. The model developed can simultaneously predict phenol degradation and 4-cp transformation, and is useful for dealing with cometabolism involving multiple substrates.     

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.     

Role of oxygen in the utilization of phenol by Pseudomonas CF600 in continuous culture

The dissolved oxygen (DO) level is the key factor which decides the rate of degradation of the organic load in aerobic growth conditions. In this study the role of DO levels on the utilization of phenols has been reported using the continuous culture system. A phenol-utilizing strain, Pseudomonas CF600 has been used as a model. Its phenol-degrading capacity was studied using continuous cultivation for a period of 60 days. The bioreactor was kept at a dilution rate of 0.006 h^–1 with DO levels maintained at 2, 3, and 4 ppm keeping all the other cultivation conditions constant. Physiological variations under the cultivation conditions were studied by monitoring off-line phenol utilization and respirometric analysis of harvested culture against different substrates. It was observed that the accumulation of 2-hydroxymuconate semialdehyde (HMS), an intermediate in the phenol degradation pathway, depends on the DO level. The maximum level of HMS in the medium observed was 3.92 M when DO was maintained at 2 ppm whereas with 3 ppm of DO, HMS level was below 0.4 M. Oxygen uptake data of the cells harvested from cultures grown at different DO levels showed that the uptake was highest at 3 ppm DO for all the substrates tried. When phenol was used as substrate, the oxygen uptake rate was 42.66, 66.36 and 35.55 nM/min/mg dry weight of cells at 4, 3 and 2 ppm DO respectively. Results show that DO levels influence the rate of phenol utilization in Pseudomonas CF600.     

Kinetics of methanogenic degradation of phenol by activated-carbon-supported and granular biomass

A continuous-feed recycle bioreactor was used to study the kinetics of methanogenic degradation of phenol at 35 degrees C by bacteria supported on a bed of granular activated carbon (GAC). At dilution rates well above the growth rate of the culture, the cells not only populated the GAC, but also formed a layer of granular biomass. This layer was stabilized by the presence of the GAC, and accounted for over half of the phenol-degrading activity in the bioreactor. The specific phenol degradation rates for GAC-attached biomass, suspended biomass, and granular biomass were all in the range 0.15 to 0.22 mg phenol/mg volatile solids per day as measured under pseudo-steady-state conditions. (c) 1992 John Wiley & Sons, Inc.     

KINETICS OF NUTRIENT UPTAKE AND GROWTH IN PHYTOPLANKTON1

Microscopic algae ran grow rapidly in natural waters that are extremely low in essential macro and micro nutrients. Yet, their nutrient uptake systems exhibit only mediocre nutrient affinities, the saturation constants being often 10–1000 times the (estimated) ambient concentrations. The large difference which exists between the saturation constants for growth (K_μ) and short term uptake (K_ρ) are due to the acclimation capabilities of the organisms. Over the acclimation range, K_μ to K_ρ, the algae can maintain maximum growth rate by modulating both their internal nutrient quotas (Q) and their maximum short term nutrient uptake rates (ρ_max) in response to variations in external nutrient concentrations. The commonly assumed hyperbolic relationships for steady growth and uptake (viz “chemostat theory”) are coherent with a hyperbolic expression for short term uptake including a variable maximum (ρ_max). The ratio of the saturation constants for growth and uptake is then directly related to the extreme in quotas and maximum uptake rates: K_μ/K_ρ= Q_min/Q_max·ρ^lo_max/ρ^hi_max. This result is applicable even when the exact hyperbolic laws are not. Published data on Fe, Mn, P and N limitation in algae are generally in accord with the theory and demonstrate a wider acclimation range for trace than for major nutrients.     

STEADY-STATE LUXURY CONSUMPTION AND THE CONCEPT OF OPTIMUM NUTRIENT RATIOS: A STUDY WITH PHOSPHATE AND NITRATE LIMITED SELENASTRUM MINUTUM (CHLOROPHYTA)1

Selenastrum minutum (Naeg.) Collins was grown over a wide range of growth rates under phosphate or nitrate limitation with non-limiting nutrients added to great excess. This resulted in saturated luxury consumption. The relationships between growth rate and cell quota for the limiting nutrients were well described by the Droop relationship. The observed variability in N cell quota under N limitation as reflected in k_Q·Q_max^?1*, was similar in magnitude to previously reported values but k_Q·Q_max^?1* for P under P limitation was greater than previously reported for other species. These results were evaluated in light of the optimum ratio hypothesis. Our findings support previous work suggesting that the use of a single optimum ratio (k_Qi·K_Qj^?1) is inappropriate for dealing with a species growing under steady-state nutrient limitation. Under these conditions the optimum ratio should be viewed as a growth rate dependent variable. Two approaches for testing the growth rate dependency of optimum ratios are proposed. The capacity for luxury consumption differed between nutrients and was growth rate dependent. At low growth rates, the coefficient of luxury consumption (R_sat) for P was ca. four times that for N. The set of all possible relationships between N and P cell quota under these conditions was reported and these values were then used to establish the cellular N:P niche boundaries for S. minutum. Cell quotas of non-limiting nutrients were not described by the Droop equation. Analysis showed that as the cellular N:P ratio deviates from the optimum ratio, the ability of the Droop equation to describe the relationship between growth rate and non-limiting cell quotas decreases. When non-limiting nutrient cell quotas are saturated, the Droop equation appears to be invalid. Previously reported patterns of non-limiting nutrient utilization are summarized in support of this conclusion. The physiological and ecological consequences of luxury consumption and growth rate dependent optimum ratios are considered.     

Effects of substrate limitation on product distribution and H2/CO2 ratio inKlebsiella pneumoniae during anaerobic fermentation of glycerol

Product formation during anaerobic degradation of glycerol byKlebsiella pneumoniae DSM 2026, under glycerol limitation and glycerol excess in continugius cultures, has been investigated. Major and minor products and by-products as well as gaseous products were measured. The results indicated a positive correlation between specific glycerol uptake and most product formation rates under glycerol limitation. The production of 1,3-propanediol, lactate, formate, acetate, succinate and the by-products of anaerobic glycerol degradation byK. pneumoniae, acetoin and 2,3-butanediol, was favoured by glycerol excess, while hydrogen generation and ethanol formation were best under glycerol limitation. It was also found that under glycerol limitation the rate of hydrogen evolution was generally higher than the CO₂ production rate while under excess glycerol the reverse was true. Hence, on the basis of the ratio of the specific rates of evolution of H₂ and CO₂ (q _{H 2}/q _{CO 2}), it is possible to infer the existence of glycerol limitation. On the basis of the carbon and available electron balances, which are independent of metabolic pathways, the data are consistent. The NADH₂ balance, which took into consideration the pathways of product formation, was also tested to check the validity of the assumed pathways and to check critically the consistency of the data. Good balances were also obtained.[     

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.     

Performance characterization of a model bioreactor for the biodegradation of trichloroethylene by Pseudomonas cepacia G4.

Pseudomonas cepacia G4 grown in chemostats with phenol demonstrated constant specific degradation rates for both phenol and trichloroethylene (TCE) over a range of dilution rates. Washout of cells from chemostats was evident at a dilution rate of 0.2 h-1 at 28 degrees C. Increased phenol concentrations in the nutrient feed led to increased biomass production with constant specific degradation rates for both phenol and TCE. The addition of lactate to the phenol feed led to increased biomass production but lowered specific phenol and TCE degradation rates. The maximum potential for TCE degradation was about 1.1 g per day per g of cell protein. Cell growth and degradation kinetic parameters were used in the design of a recirculating bioreactor for TCE degradation. In this reactor, the total amount of TCE degraded increased as either reaction time or biomass was increased. TCE degradation was observed up to 300 microM TCE with no significant decreases in rates. On the average, this reactor was able to degrade 0.7 g of TCE per day per g of cell protein. These results demonstrate the feasibility of TCE bioremediation through the use of bioreactors.     

Performance characterization of a model bioreactor for the biodegradation of trichloroethylene by Pseudomonas cepacia G4

Pseudomonas cepacia G4 grown in chemostats with phenol demonstrated constant specific degradation rates for both phenol and trichloroethylene (TCE) over a range of dilution rates. Washout of cells from chemostats was evident at a dilution rate of 0.2 h-1 at 28 degrees C. Increased phenol concentrations in the nutrient feed led to increased biomass production with constant specific degradation rates for both phenol and TCE. The addition of lactate to the phenol feed led to increased biomass production but lowered specific phenol and TCE degradation rates. The maximum potential for TCE degradation was about 1.1 g per day per g of cell protein. Cell growth and degradation kinetic parameters were used in the design of a recirculating bioreactor for TCE degradation. In this reactor, the total amount of TCE degraded increased as either reaction time or biomass was increased. TCE degradation was observed up to 300 microM TCE with no significant decreases in rates. On the average, this reactor was able to degrade 0.7 g of TCE per day per g of cell protein. These results demonstrate the feasibility of TCE bioremediation through the use of bioreactors.     

Uptake of phenol by the phenol-metabolizing bacteria of a stable,strictly anaerobic consortium

Phenol was absorbed unspecifically by active and by inactivated cells of a strictly anaerobic, phenol-degrading consortium to reach about twice the concentration of the medium. The absorption was temperature-dependent. A Q₁₀ of 1.7 was determined, indicating that accumulation was due to diffusion or facilitated diffusion and not to an active transport process. At increasing phenol concentration in the medium, concentrated cell suspensions adsorpted phenol proportionally until saturation was reached at about 25 nmol phenol/mg cell dry weight. At a phenol concentration in the medium of 2 mm, the washed cell pellet contained 3.5 mm phenol. Under conditions that allowed phenol metabolism (presence of CO₂), [¹⁴C]4-hydroxybenzoyl-coenzyme A and [¹⁴C]4-hydroxybenzoate were found as early intermediates of [U-¹⁴C]phenol degradation for the first time. [¹⁴C]Benzoate was excreted stoichiometrically if phenol degradation to acetate was prevented by H₂. Absolutely no ¹⁴C-label was found in the phenylphosphate peak after HPLC separation, which excluded phosphorylation of phenol during uptake or during degradation in the cells. Correspondence to: J. Winter     

Monochlorophenols as enzyme substrates for the preparatory metabolism of phenol in Candida tropicalis yeasts

The object of this work was to find out whether Candida tropicalis can be used for monochlorophenol degradation. Phenol monooxygenase and pyrocatechase, enzymes involved in preparatory phenol metabolism were shown to catalyse transformation of 3- and 4-chlorophenols. Phenol monooxygenase catalyses hydroxylation of 3- and 4-chlorophenols to 4-chloropyrocatechol which yields beta-chloromuconic acid under the action of pyrocatechase. Synthesis of phenol monooxygenase is induced by 3- and 4-chlorophenols. beta-Chloromuconic acid is a terminal product of 3- and 4-chlorophenol transformation under neutral conditions. In a weakly acid medium (the Rieder medium, phosphate buffer, pH 5.5), transformation of these chlorophenols terminates with spontaneous lactonization of beta-chloromuconic acid and its dehalogenation. C. tropicalis hardly transforms 2-chlorophenol although certain oxygen uptake occurs in its presence. 3- and 4-chlorophenols are not nutrient sources for C. tropicalis. The yeast has not been adapted to 3- and 4-chlorophenols as sole nutrient sources.