Ginsenoside Rd production from the major ginsenoside Rb<Subscript>1</Subscript> by <Emphasis Type="Italic">β</Emphasis>-glucosidase from <Emphasis Type="Italic">Thermus caldophilus</Emphasis>

Under optimum conditions (pH 5, 75°C, and 0.2 U purified enzyme ml⁻¹), 4 mg ginsenoside Rd was produced from 5 mg reagent-grade ginsenoside Rb₁ in 5 ml after 30 min by β-glucosidase from Thermus caldophilus GK24. Using a ginseng root extract containing 1 mg ginsenoside Rb₁ ml⁻¹ and 3.2 mg additional ginsenosides ml⁻¹, 1.23 mg ginsenoside Rd ml⁻¹ was produced after 18 h; the concentrations of ginsenosides Rb₁, Rb₂, and Rc used for ginsenoside Rd production were 0.77, 0.17, and 0.19 mg ml⁻¹, respectively.     

Ginsenoside F1 production from ginsenoside Rg1 by a purified β-glucosidase from Fusarium moniliforme var. subglutinans

Fusarium moniliforme var. subglutinans was selected from among 100 strains of fungi for producing ginsenoside F₁ from ginsenoside Rg₁. The enzyme responsible was purified as a single 85 kDa band with a specific activity of 136 U mg⁻¹. It hydrolysed glucose-linked ginsenosides Rb₁, Rd and Rg₁ but not for other monosaccharide-linked ginsenosides, Rb₂, Rc, R₁, and Re. Under the optimum conditions of pH 6.0, 50°C, 30 U l⁻¹ of enzyme, and 5 mg Rg₁ ml⁻¹, 4 mg F₁ ml⁻¹ was produced after 4 h, with a molar yield of 100% and a productivity of 1 g l⁻¹ h⁻¹. This represents the highest productivity and conversion yield of F₁ yet reported.     

β-Glucosidase from Penicillium aculeatum hydrolyzes exo-, 3-O-, and 6-O-β-glucosides but not 20-O-β-glucoside and other glycosides of ginsenosides

A novel β-glucosidase from Penicillium aculeatum was purified as a single 110.5-kDa band on SDS–PAGE with a specific activity of 75.4 U?mg^?1 by salt precipitation and Hi-Trap Q HP and Resource Q ion exchange chromatographies. The purified enzyme was identified as a member of the glycoside hydrolase 3 family based on its amino acid sequence. The hydrolysis activity for p-nitrophenyl-β-d-glucopyranoside was optimal at pH 4.5 and 70 °C with a half-life of 55 h. The enzyme hydrolyzed exo-, 3-O-, and 6-O-β-glucosides but not 20-O-β-glucoside and other glycosides of ginsenosides. Because of the novel specificity, this enzyme had the transformation pathways for ginsenosides: Rb₁?→?Rd?→?F₂?→?compound K, Rb₂?→?compound O?→?compound Y, Rc?→?compound Mc₁?→?compound Mc, Rg₃?→?Rh₂?→?aglycone protopanaxadiol (APPD), Rg₁?→?F₁, and Rf?→?Rh₁?→?aglycone protopanaxatriol (APPT). Under the optimum conditions, the enzyme converted 0.5 mM Rb_2, Rc, Rd, Rg₃, Rg₁, and Rf to 0.49 mM compound Y, 0.49 mM compound Mc, 0.47 mM compound K, 0.23 mM APPD, 0.49 mM?F₁, and 0.44 mM APPT after 6 h, respectively.     

Production of rare ginsenosides (compound Mc, compound Y and aglycon protopanaxadiol) by β-glucosidase from Dictyoglomus turgidum that hydrolyzes β-linked, but not α-linked, sugars in ginsenosides

Optimal hydrolytic activity of β-glucosidase from Dictyoglomus turgidum for the ginsenoside Rd was at pH 5.5 and 80?°C, with a half-life of ~11?h. The enzyme hydrolysed β-linked, but not α-linked, sugar moieties of ginsenosides. It produced the rare ginsenosides, aglycon protopanaxadiol (APPD), compounds Y, and Mc, via three unique transformation pathways: Rb(1)?→?Rd?→?F(2)?→?compound K?→?APPD, Rb(2)?→?compound Y, and Rc?→?compound Mc. The enzyme converted 0.5?mM Rb(2) and 0.5?mM Rc to 0.5?mM compound Y and 0.5?mM compound Mc after 3?h, respectively, with molar conversion yields of 100?%.     

Conversion of Major Ginsenoside Rb1 to Ginsenoside F2 by Caulobacter leidyia

Ginsenoside Rb₁ is the most predominant ginsenoside in Panax species (ginseng) and the hydrolysis of this ginsenoside produces pharmaceutically active compounds. Caulobacter leidyia GP45, one of the isolates having strong β-glucosidase-producing activity, converted ginsenoside Rb₁ to the active metabolites by 91%. The structures of the resultant metabolites were identified by NMR. Ginsenoside Rb₁ had been consecutively converted to ginsenoside Rd (1), F₂ (2) and compound K (3) via the hydrolyses of 20-C β-(1→6)-glucoside, 3-C β-(1→2)-glucoside, and 3-C β-glucose of ginsenoside Rb₁.     

Biodegradation kinetics of 1,4-benzoquinone in batch and continuous systems

Combining chemical and biological treatments is a potentially economic approach to remove high concentration of recalcitrant compounds from wastewaters. In the present study, the biodegradation of 1,4-benzoquinone, an intermediate compound formed during phenol oxidation by chlorine dioxide, was investigated using Pseudomonas putida (ATCC 17484) in batch and continuous bioreactors. Batch experiments were conducted to determine the effects of 1,4-benzoquinone concentration and temperature on the microbial activity and biodegradation kinetics. Using the generated data, the maximum specific growth rate and biodegradation rate were determined as 0.94 h⁻¹ and 6.71 mg of 1,4-benzoquinone l⁻¹ h⁻¹. Biodegradation in a continuous bioreactor indicated a linear relationship between substrate loading and biodegradation rates prior to wash out of the cells, with a maximum biodegradation rate of 246 mg l⁻¹ h⁻¹ observed at a loading rate of 275 mg l⁻¹ h⁻¹ (residence time: 1.82 h). Biokinetic parameters were also determined using the steady state substrate and biomass concentrations at various dilution rates and compared to those obtained in batch cultures.     

Ethrel treatment enhanced isoflavonoids accumulation in cell suspension cultures of Pueraria tuberosa, a woody legume

The cell cultures of Pueraria tuberosa, a perennial leguminous lianas, were maintained in modified MS medium (KNO₃ 475 mg l⁻¹, thiamine 1 mg l⁻¹, biotin 1 mg l⁻¹, calcium pantothenate 1 mg l⁻¹) containing 0.1 mg l⁻¹ 2,4,5-trichloroacetic acid and 0.1 mg l⁻¹ kinetin. Isoflavonoids (puerarin, genistin, daidzein, genistein) accumulation in cell suspension cultures was increased by 14-fold to ~12 mg l⁻¹ after 48 h of adding 100 μM ethrel. Ethrel inhibitors (silver nitrate and silver thiosulfate) completely inhibited this effect in the presence of ethrel and isoflavonoids were not detected in the spent medium. The increase was dose dependent and can be explored to trigger high yield of isoflavonoids production.     

Highly selective biotransformation of ginsenoside Rb<Subscript>1</Subscript> to Rd by the phytopathogenic fungus<Emphasis Type="Italic"> Cladosporium fulvum</Emphasis> (<Emphasis Type="Italic">syn</Emphasis>.<Emphasis Type="Italic"> Fulvia fulva</Emphasis>)

Fourteen phytopathogenic fungi were tested for their ability to transform the major ginsenosides to the active minor ginsenoside Rd. The transformation products were identified by TLC and HPLC, and their structures were assigned by NMR analysis. Cladosporium fulvum, a tomato pathogen, was found to transform major ginsenoside Rb₁ to Rd as the sole product. The following optimum conditions for transforming Rd by C. fulvum were determined: the time of substrate addition, 24 h; substrate concentration, 0.25 mg ml⁻¹; temperature, 37°C; pH 5.0; and biotransformation period, 8 days. At these optimum conditions, the maximum yield was 86% (molar ratio). Further, a preparative scale transformation with C. fulvum was performed at a dose of 100 mg of Rb₁ by a yield of 80%. This fungus has potential to be applied on the preparation for Rd in pharmaceutical industry.     

Characterization of a novel ginsenoside-hydrolyzing α-l-arabinofuranosidase, AbfA, from Rhodanobacter ginsenosidimutans Gsoil 3054T

The gene encoding an α-l-arabinofuranosidase that could biotransform ginsenoside Rc {3-O-[β-d-glucopyranosyl-(1–2)-β-d-glucopyranosyl]-20-O-[α-l-arabinofuranosyl-(1–6)-β-d-glucopyranosyl]-20(S)-protopanaxadiol} to ginsenoside Rd {3-O-[β-d-glucopyranosyl-(1–2)-β-d-glucopyranosyl]-20-O-β-d-glucopyranosyl-20(S)-protopanaxadiol} was cloned from a soil bacterium, Rhodanobacter ginsenosidimutans strain Gsoil 3054^T, and the recombinant enzyme was characterized. The enzyme (AbfA) hydrolyzed the arabinofuranosyl moiety from ginsenoside Rc and was classified as a family 51 glycoside hydrolase based on amino acid sequence analysis. Recombinant AbfA expressed in Escherichia coli hydrolyzed non-reducing arabinofuranoside moieties with apparent K _m values of 0.53 ± 0.07 and 0.30 ± 0.07 mM and V _max values of 27.1 ± 1.7 and 49.6 ± 4.1 μmol min⁻¹ mg⁻¹ of protein for p-nitrophenyl-α-l-arabinofuranoside and ginsenoside Rc, respectively. The enzyme exhibited preferential substrate specificity of the exo-type mode of action towards polyarabinosides or oligoarabinosides. AbfA demonstrated substrate-specific activity for the bioconversion of ginsenosides, as it hydrolyzed only arabinofuranoside moieties from ginsenoside Rc and its derivatives, and not other sugar groups. These results are the first report of a glycoside hydrolase family 51 α-l-arabinofuranosidase that can transform ginsenoside Rc to Rd.     

Enhanced regeneration of haploid plantlets from microspores of <Emphasis Type="Italic">Brassica napus</Emphasis> L. using bleomycin,PCIB, and phytohormones

The effects of three periods of incubation (10, 20 and 30 min) at different levels of bleomycin (0, 0.1, 0.2, 0.3, 0.4 and 0.5 μg ml⁻¹), as well as three periods of exposure (12, 24 and 48 h) to different levels of the anti-auxin p-chlorophenoxyisobutyric acid (PCIB), including 1, 2, 3, 4 and 5 mg l⁻¹, on microspore embryogenesis of rapeseed cv. ‘Amica’ were investigated. Microspore embryogenesis was significantly enhanced following 20 min treatment with 0.2 μg ml⁻¹ bleomycin compared with untreated cultures. Highest embryo yield (163 embryos Petri dish⁻¹) was observed with 24 h treatment of 4 mg l⁻¹ PCIB. The highest percentage of secondary embryogenesis was observed on B₅ medium containing 0.15 mg l⁻¹ of gibberellic acid (GA₃) and 0.2 mg l⁻¹ 6-benzyladenine (BA) in 4–6 mm microspore-derived embryos (MDEs). Most callus formed on B₅ medium containing 0.15 mg l⁻¹ GA₃, 0.1 mg l⁻¹ BA and 0.1 mg l⁻¹ indole-3-acetic acid (IAA) when 4–6 mm embryos were used. Regeneration was highest on B₅ medium containing 0.05 mg l⁻¹ GA₃ or 0.1 mg l⁻¹ BA and 0.2 mg l⁻¹ IAA with 2–4 mm embryos. Microspore embryogenesis and plant regeneration could be improved by both bleomycin and PCIB when the appropriate MDE length and phytohormone level were selected.     

Microbial transformation of ginsenosides Rb1, Rb3 and Rc by Fusarium sacchari

Aims: This study examined the transformation pathways of ginsenosides G‐Rb₁, G‐Rb₃, and G‐Rc by the fungus Fusarium sacchari. Methods and Results: Ginsenosides G‐Rb₁, G‐Rb₃ and G‐Rc were isolated from leaves of Radix notoginseng, and their structural identification was confirmed using NMR. Transformation of G‐Rb₁, G‐Rb₃ and G‐Rc by Fusarium sacchari was respectively experimented. Kinetic evolutions of G‐Rb₁, G‐Rb₃ and G‐Rc and their metabolites during the cell incubation were monitored by HPLC analysis. High‐performance liquid chromatography (HPLC) was used for monitoring the transformation kinetics of bioactive compounds during F. sacchari metabolism. Conclusions: Ginsenoside C‐K was transformed by F. sacchari from G‐Rb₁ via G‐Rd or via G‐F₂, or from G‐Rb₁ via firstly Rd and then G‐F₂, and C‐Mx was transformed by F. sacchari or directly from Rb₃, or from Rb₃ via Gy‐IX, while G‐Mc was transformed by F. sacchari directly from G‐Rc. Furthermore, C‐K could be also formed from G‐Rc via notoginsenoside Fe (N‐Fe). Significance and Impact of the Study: The results showed an important practical application in the preparation of ginsenoside C‐K. As our precious research indicated C‐K possessed much more antitumor activities than C‐Mx and G‐Mc, so according to the transformation pathways proposed by this work, the production of antitumor compound C‐K may be performed by biotransformation of G‐Rb₁ previously isolated from PNLS.     

Biotreatment of phenol-contaminated wastewater in a spiral packed-bed bioreactor

A spiral packed-bed bioreactor inoculated with microorganisms obtained from activated sludge was used to conduct a feasibility study for phenol removal. The reactor was operated continuously at various phenol loadings ranging from 53 to 201.4 g m⁻³ h⁻¹, and at different hydraulic retention times (HRT) in the range of 20–180 min to estimate the performance of the device. The results indicated that phenol removal efficiency ranging from 82.9 to 100% can be reached when the reactor is operated at an HRT of 1 h and a phenol loading of less than 111.9 g m⁻³ h⁻¹. At an influent phenol concentration of 201.4 g m⁻³, the removal efficiency increased from 18.6 to 76.9% with an increase in the HRT (20–120 min). For treatment of phenol in the reactor, the maximum biodegradation rate (V _m) was 1.82 mg l⁻¹ min⁻¹; the half-saturation constant (K _s), 34.95 mg l⁻¹.     

Low salt medium for lactate and ethanol production by recombinant Escherichia coli B

Individual nutrient salts were experimentally varied to determine the minimum requirements for efficient l(+)-lactate production by recombinant strains of Escherichia coli B. Based on these results, AM1 medium was formulated with low levels of alkali metals (4.5 mM and total salts (4.2 g l⁻¹). This medium was equally effective for ethanol production from xylose and lactate production from glucose with average productivities of 18–19 mmol l⁻¹ h⁻¹ for both (initial 48 h of fermentation).     

Cytokinin-induced organogenesis in Lessertia (Sutherlandia) frutescens L. using hypocotyl and cotyledon explants affects yields of l-canavanine in shoots

A simple protocol for direct shoot organogenesis and plant regeneration in Lessertia frutescens using hypocotyl and cotyledon segments is reported. l-canavanine content in the derived shoots is also quantified. Media containing different concentrations and combinations of the cytokinins kinetin (K) and benzyladenine (BA) were tested for shoot induction potential. The best shoot regeneration rate (83%) was obtained from hypocotyl segments cultured in Murashige and Skoog (MS) medium supplemented with 1 mg l⁻¹ K; these hypocotyls also produced the largest number of shoots per explant (3.5) and the longest shoots per explant (13.3 mm). The best shoot regeneration rate (46%) using cotyledons as explant material was obtained in MS medium supplemented with 1 mg l⁻¹ K and 1 mg l⁻¹ BA or with 5 mg l⁻¹ K and 0.5 mg l⁻¹ BA. The highest number of cotyledon-derived shoots (1.5) was obtained in MS medium containing 2 mg l⁻¹ K and 0.5 mg l⁻¹ BA, and the longest cotyledon-derived shoots (6.1 mm) were obtained in MS medium containing 1 mg l⁻¹ K and 0.5 mg l⁻¹ BA. Shoots derived from hypocotyls cultured on media containing 1 mg l⁻¹ K contained the highest quantity of l-canavanine (1.42 mg g⁻¹) relative to the control (0.52 mg g⁻¹). Shoots derived from cotyledons cultured on media containing 2 mg l⁻¹ K contained the highest quantity of l-canavanine (2.07 mg g⁻¹) compared to the control. Scanning electron microscopy revealed that shoots regenerated directly from the wounded epidermal tissue, although callus formation was observed in most cultures. Young shoot clusters proliferated into healthy adventitious shoots that were subsequently transferred directly onto rooting medium (MS medium containing 4 mg l⁻¹ indole-3-butyric acid), eliminating the need for an additional multiplication or elongation phase. The in vitro plants were successfully acclimatized in a growth chamber, achieving an 85% survival rate.     

Fluoranthene influences endogenous abscisic acid level and primary photosynthetic processes in pea (<Emphasis Type="Italic">Pisum sativum</Emphasis> L.) plants in vitro

The influence of increasing concentrations (0.1, 1.0 and 5.0 mg l⁻¹) of fluoranthene (FLT) on growth, endogenous abscisic acid (ABA) level and primary photosynthetic processes in 21-day-old pea plants (Pisum sativum L.) in vitro was investigated. Murashige and Skoog’s (MS) medium, with or without FLT, was enriched with indole-3-acetic acid (IAA; 0.1 mg l⁻¹) or a combination of IAA (0.1 mg l⁻¹) plus N⁶-benzyladenine (BA; 0.1 mg l⁻¹). The level of endogenous ABA significantly increased with increasing FLT concentrations in the presence of both IAA and IAA plus BA. An increased level of endogenous ABA was observed in plants treated with IAA alone. The growth of shoot, callus and the content of photosynthetic pigments (chlorophyll a and b, carotenoids), in both IAA- and IAA plus BA-treated plants, were significantly stimulated by FLT at its lowest concentration (0.1 mg l⁻¹) assayed in this study. However, FLT at higher concentrations (1.0 and 5.0 mg l⁻¹) significantly inhibited all these parameters. Chlorophyll fluorescence imaging showed that FLT only at the highest concentration (5.0 mg l⁻¹) in the presence of IAA (0.1 mg l⁻¹) significantly increased F₀, but decreased F_V/F_M and Φ_II.     

Increase of lycopene production by supplementing auxiliary carbon sources in metabolically engineered <Emphasis Type="Italic">Escherichia coli</Emphasis>

In the fed-batch culture of glycerol using a metabolically engineered strain of Escherichia coli, supplementation with glucose as an auxiliary carbon source increased lycopene production due to a significant increase in cell mass, despite a reduction in specific lycopene content. l-Arabinose supplementation increased lycopene production due to increases in cell mass and specific lycopene content. Supplementation with both glucose and l-arabinose increased lycopene production significantly due to the synergistic effect of the two sugars. Cell growth by the consumption of carbon sources was related to endogenous metabolism in the host E. coli. Supplementation with l-arabinose stimulated only the mevalonate pathway for lycopene biosynthesis and supplementation with both glucose and l-arabinose stimulated synergistically only the mevalonate pathway. In the fed-batch culture of glycerol with 10 g l⁻¹ glucose and 7.5 g l⁻¹ l-arabinose, the cell mass, lycopene concentration, specific lycopene content, and lycopene productivity after 34 h were 42 g l⁻¹, 1,350 mg l⁻¹, 32 mg g cells⁻¹, and 40 mg l⁻¹ h⁻¹, respectively. These values were 3.9-, 7.1-, 1.9-, and 11.7-fold higher than those without the auxiliary carbon sources, respectively. This is the highest reported concentration and productivity of lycopene.     

In vitro root culture of <Emphasis Type="Italic">Ocimum sanctum</Emphasis> L. and evaluation of its free radical scavenging activity

Young leaf explants of Ocimum sanctum L. incubated on solidified Murashige and Skoog (MS) medium supplemented with 2 mg l⁻¹ 1-naphthaleneacetic acid (NAA) and 0.2 mg l⁻¹ kinetin (Kn) developed rhizogenic callus. When these were subcultured onto MS medium supplemented with 1.5 mg l⁻¹ 2, 4-dichlorophenoxyacetic acid (2, 4-D) and 0.5 mg l⁻¹ NAA, friable rhizogenic callus was observed. Upon transfer of this friable callus onto liquid MS medium containing 4 mg l⁻¹ NAA and 1.3 mg l⁻¹ 6-benzyladnine (BA) under continuous agitation at 90 rpm and 16 h photoperiod, roots with an optimum dry weight of 1,460 mg l⁻¹ were obtained. An ethyl acetate extract of these roots exhibited 1, 1–diphenyl-2-picrylhydrazyl (DPPH) radical scavenging activity.     

Microbial community of acetate utilizing denitrifiers in aerobic granules

Nitrite accumulates during biological denitrification processes when carbon sources are insufficient. Acetate, methanol, and ethanol were investigated as supplementary carbon sources in the nitrite denitrification process using biogranules. Without supplementary external electron donors (control), the biogranules degraded 200 mg l⁻¹ nitrite at a rate of 0.27 mg NO₂–N g⁻¹ VSS h⁻¹. Notably, 1,500 mg l⁻¹ acetate and 700 mg l⁻¹ methanol or ethanol enhanced denitrification rates for 200 mg l⁻¹ nitrite at 2.07, 1.20, and 1.60 mg NO₂–N g⁻¹ VSS h⁻¹, respectively; these rates were significantly higher than that of the control. The sodium dodecyl sulfate polyacrylamide gel electrophoresis of the nitrite reductase (NiR) enzyme identified three prominent bands with molecular weights of 37–41 kDa. A linear correlation existed between incremental denitrification rates and incremental activity of the NiR enzyme. The NiR enzyme activity was enhanced by the supplementary carbon sources, thereby increasing the nitrite denitrification rate. The capacity of supplementary carbon source on enhancing NiR enzyme activity follows: methanol > acetate > ethanol on molar basis or acetate > ethanol > methanol on an added weight basis.     

Enhanced degradation of phenol by <Emphasis Type="Italic">Pseudomonas</Emphasis> sp. CP4 entrapped in agar and calcium alginate beads in batch and continuous processes

Phenol is one of the major toxic pollutants in the wastes generated by a number of industries and needs to be eliminated before their discharge. Although microbial degradation is a preferred method of waste treatment for phenol removal, the general inability of the degrading strains to tolerate higher substrate concentrations has been a bottleneck. Immobilization of the microorganism in suitable matrices has been shown to circumvent this problem to some extent. In this study, cells of Pseudomonas sp. CP4, a laboratory isolate that degrades phenol, cresols, and other aromatics, were immobilized by entrapment in Ca-alginate and agar gel beads, separately and their performance in a fluidized bed bioreactor was compared. In batch runs, with an aeration rate of 1 vol⁻¹ vol⁻¹ min⁻¹, at 30°C and pH 7.0 ± 0.2, agar-encapsulated cells degraded up to 3000 mg l⁻¹ of phenol as compared to 1500 mg l⁻¹ by Ca-alginate-entrapped cells whereas free cells could tolerate only 1000 mg l⁻¹. In a continuous process with Ca-alginate entrapped cells a degradation rate of 200 mg phenol l⁻¹ h⁻¹ was obtained while agar-entrapped cells were far superior and could withstand and degrade up to 4000 mg phenol l⁻¹ in the feed with a maximum degradation rate of 400 mg phenol l⁻¹ h⁻¹. The results indicate a clear possibility of development of an efficient treatment technology for phenol containing waste waters with the agar-entrapped bacterial strain, Pseudomonas sp. CP4.     

Phenol biodegradation by the thermoacidophilic archaeon <Emphasis Type="Italic">Sulfolobus solfataricus</Emphasis> 98/2 in a fed-batch bioreactor

Toxic at low concentrations, phenol is one of the most common organic pollutants in air and water. In this work, phenol biodegradation was studied in extreme conditions (80°C, pH = 3.2) in a 2.7 l bioreactor with the thermoacidophilic archaeon Sulfolobus solfataricus 98/2. The strain was first acclimatized to phenol on a mixture of glucose (2000 mg l⁻¹) and phenol (94 mg l⁻¹) at a constant dissolved oxygen concentration of 1.5 mg l⁻¹. After a short lag-phase, only glucose was consumed. Phenol degradation then began while glucose was still present in the reactor. When glucose was exhausted, phenol was used for respiration and then for biomass build-up. After several batch runs (phenol < 365 mg l⁻¹), specific growth rate (μ_X) was 0.034 ± 0.001 h⁻¹, specific phenol degradation rate (q_P) was 57.5 ± 2 mg g⁻¹ h⁻¹, biomass yield (Y_X/P) was 52.2 ± 1.1 g mol⁻¹, and oxygen yield factor ( \textY_{\textX/\textO 2} ) \left( {{\text{Y}}_{{{\text{X}}/{\text{O}}_{ 2} }} } \right) was 9.2 ± 0.2 g mol⁻¹. A carbon recovery close to 100% suggested that phenol was exclusively transformed into biomass (35%) and CO₂ (65%). Molar phenol oxidation constant ( \textY_{\textO 2 /\textP} ) \left( {{\text{Y}}_{{{\text{O}}_{ 2} /{\text{P}}}} } \right) was calculated from stoichiometry of phenol oxidation and introducing experimental biomass and CO₂ conversion yields on phenol, leading to values varying between 4.78 and 5.22 mol mol⁻¹. Respiratory quotient was about 0.84 mol mol⁻¹, very close to theoretical value (0.87 mol mol⁻¹). Carbon dioxide production, oxygen demand and redox potential, monitored on-line, were good indicators of growth, substrate consumption and exhaustion, and can therefore be usefully employed for industrial phenol bioremediation in extreme environments.