Kinetics study of pyridine biodegradation by a novel bacterial strain,Rhizobium sp. NJUST18

Biodegradation of pyridine by a novel bacterial strain, Rhizobium sp. NJUST18, was studied in batch experiments over a wide concentration range (from 100 to 1,000 mg l^?1). Pyridine inhibited both growth of Rhizobium sp. NJUST18 and biodegradation of pyridine. The Haldane model could be fitted to the growth kinetics data well with the kinetic constants μ* = 0.1473 h^?1, K _s = 793.97 mg l^?1, K _i = 268.60 mg l^?1 and S _m = 461.80 mg l^?1. The true μ _max, calculated from μ*, was found to be 0.0332 h^?1. Yield coefficient Y _X/S depended on S _i and reached a maximum of 0.51 g g^?1 at S _i of 600 mg l^?1. V _max was calculated by fitting the pyridine consumption data with the Gompertz model. V _max increased with initial pyridine concentration up to 14.809 mg l^?1 h^?1. The q _S values, calculated from $V_{ \hbox{max} }$ , were fitted with the Haldane equation, yielding q _Smax = 0.1212 g g^?1 h^?1 and q* = 0.3874 g g^?1 h^?1 at S _m′ = 507.83 mg l^?1, K _s′ = 558.03 mg l^?1, and K _i′ = 462.15 mg l^?1. Inhibition constants for growth and degradation rate value were in the same range. Compared with other pyridine degraders, μ _max and S _m obtained for Rhizobium sp. NJUST18 were relatively high. High K _i and K _i′ values and extremely high K _s and K _s′ values indicated that NJUST18 was able to grow on pyridine within a wide concentration range, especially at relatively high concentrations.     

Yield and kinetic constants estimation in the production of hydroxy fatty acids from oleic acid in a bioreactor by Pseudomonas aeruginosa 42A2

We modelled the production of hydroxy fatty acids from oleic acid by Pseudomonas aeruginosa 42A2 in a bioreactor with a non-dispersive aeration system. First, we designed an adapted wetted-wall gas-absorption column, offering a k _La value of 39.9 h^?1, to enhance oxygen absorption in the culture media and prevent foam formation. Then, we analysed different kinetic models to simulate the yield coefficients and the kinetic constants in this bacterial transformation. Monod model fitting (μ _max1?=?0.51 h^?1, K _S1?=?1.60 C-mol l^?1, μ _max2?=?0.12 h^?1, K _S2?=?0.035 C-mol l^?1, and k ₂?=?0.033 h^?1) showed a good accuracy with the experimental data sets and was chosen for its simplicity. Lastly, mass balances were carried out to establish the stoichiometry of this biotransformation with the following yield coefficients, Υ _X/OA, Υ _{X/(10S)-HPOME} and Υ _{(10S)-HPOME/(7S10S)-HPOME} of 0.172, 0.347 and 2.388 C-mol C-mol^?1, respectively.     

Production and optimization of poly-γ-glutamic acid by Bacillus subtilis BL53 isolated from the Amazonian environment

The aims of this research were to screen and characterize a new microbial source of γ-PGA, to optimize aspects of culture conditions and medium composition using central composite design and response surface methodologies. The influence of bioreactor stirring rates on the production of γ-PGA was also investigated and the oxygen volumetric mass transfer coefficients (k _La) were established. The most productive strain was identified by 16S rDNA analysis as Bacillus subtilis, and its γ-PGA production in rotatory shaker was threefold increased under optimized conditions (37 °C, pH 6.9, and 1.22 mM Zn²⁺), compared to conventional medium. In bioreactor, the γ-PGA production was further increased, reaching 17 g l^?1, 70 % higher than shaker cultures. γ-PGA production showed high dependency on oxygen transfer. At k _La of 210 h^?1, the cultivation time could be reduced to 48 h, about 50 % of the time required for operations at k _La 55 h^?1.     

Characterization of alcohol dehydrogenase from <Emphasis Type="Italic">Kangiella koreensis</Emphasis> and its application to production of all-<Emphasis Type="Italic">trans</Emphasis>-retinol

A recombinant alcohol dehydrogenase (ADH) from Kangiella koreensis was purified as a 40 kDa dimer with a specific activity of 21.3 nmol min^?1 mg^?1, a K _m of 1.8 μM, and a k _cat of 1.7 min^?1 for all-trans-retinal using NADH as cofactor. The enzyme showed activity for all-trans-retinol using NAD ⁺ as a cofactor. The reaction conditions for all-trans-retinol production were optimal at pH 6.5 and 60 °C, 2 g enzyme l^?1, and 2,200 mg all-trans-retinal l^?1 in the presence of 5 % (v/v) methanol, 1 % (w/v) hydroquinone, and 10 mM NADH. Under optimized conditions, the ADH produced 600 mg all-trans-retinol l^?1 after 3 h, with a conversion yield of 27.3 % (w/w) and a productivity of 200 mg l^?1 h^?1. This is the first report of the characterization of a bacterial ADH for all-trans-retinal and the biotechnological production of all-trans-retinol using ADH.     

Production of aglycone protopanaxatriol from ginseng root extract using Dictyoglomus turgidum β-glycosidase that specifically hydrolyzes the xylose at the C-6 position and the glucose in protopanaxatriol-type ginsenosides

The hydrolytic activity of a recombinant β-glycosidase from Dictyoglomus turgidum that specifically hydrolyzed the xylose at the C-6 position and the glucose in protopanaxatriol (PPT)-type ginsenosides followed the order Rf > Rg₁ > Re > R₁ > Rh₁ > R₂. The production of aglycone protopanaxatriol (APPT) from ginsenoside Rf was optimal at pH 6.0, 80 °C, 1 mg ml^?1 Rf, and 10.6 U ml^?1 enzyme. Under these conditions, D. turgidum β-glycosidase converted ginsenoside R₁ to APPT with a molar conversion yield of 75.6 % and a productivity of 15 mg l^?1 h^?1 after 24 h by the transformation pathway of R₁ → R₂ → Rh₁ → APPT, whereas the complete conversion of ginsenosides Rf and Rg₁ to APPT was achieved with a productivity of 1,515 mg l^?1 h^?1 after 6.6 h by the pathways of Rf → Rh₁ → APPT and Rg₁ → Rh₁ → APPT, respectively. In addition, D. turgidum β-glycosidase produced 0.54 mg ml^?1 APPT from 2.29 mg ml^?1 PPT-type ginsenosides of Panax ginseng root extract after 24 h, with a molar conversion yield of 43.2 % and a productivity of 23 mg l^?1 h^?1, and 0.62 mg ml^?1 APPT from 1.35 mg ml^?1 PPT-type ginsenosides of Panax notoginseng root extract after 20 h, with a molar conversion yield of 81.2 % and a productivity of 31 mg l^?1 h^?1. This is the first report on the APPT production from ginseng root extract. Moreover, the concentrations, yields, and productivities of APPT achieved in the present study are the highest reported to date.     

Metabolism of Atrazine in Liquid Cultures and Soil Microcosms by Nocardioides Strains Isolated from a Contaminated Nigerian Agricultural Soil

Atrazine-degrading microorganisms designated EAA-3 and EAA-4, belonging to the genus Nocardioides, were obtained from an agricultural soil in Nigeria. The degradation kinetics of the two strains revealed total disappearance of 25 mg l^?1 of atrazine in less than 72 h of incubation at the rate of 0.42 mg l^?1 h^?1 and 0.35 mg l^?1 h^?1, respectively. Screening for atrazine catabolic genes in these organisms revealed the presence of trzN, atzB, and atzC. Other genes, specifically atzA, atzD, and trzD, were not detected. Potential intermediates of atrazine catabolic route such as hydroxyatrazine, desethylatrazine, and desisopropylatrazine were utilized as sources of carbon and energy, while desisopropyl desethyl-2-hydroxyatrazine and desisopropyl-2-hydroxyatrazine were attacked but in the presence of glucose. A soil microcosm study showed that degradation was faster in microcosms contaminated with 13 mg of atrazine per g^?1 of soil compared with 480 mg g^?1 of soil. In the former, degradation was 10% higher in the inoculated soil than the non-inoculated control (natural attenuation) over the 28-day study period. Corresponding value obtained for the latter was nearly 70% higher. This study has demonstrated that the bacterial strains isolated enhanced atrazine degradation and the catabolic activities of these strains were not affected with increasing soil atrazine concentration.     

Substrate concentration dependence of voltage and power production characteristics in two-chambered mediator-less microbial fuel cells with acetate and peptone substrates

Objectives

Power production characteristics and substrate concentration dependence of voltage have been investigated together with the determination of kinetic constants in two-chambered mediator-less microbial fuel cells (MFC) for acetate and peptone substrates.

Results

At 500 mg DOC l^?1 (dissolved organic carbon), power densities normalized to the anode surface of 112 mW m^?2 with acetate and 114 mW m^?2 with peptone as electron donor were attained by applying cathodes with a Pt catalyst layer. Related anode surface specific substrate removal rate was 44 g DOC m^?2 h^?1 for acetate and 52 g DOC m^?2 h^?1 for peptone. Substrate concentration dependency of the voltage suggests Monod-like kinetics with extremely low, <1 mg DOC l^?1, half saturation constants and with final DOC concentrations of 6–10 mg l^?1.

Conclusions

Acetate and peptone are equivalent substrates for the exoelectrogenic bacteria both from the point of view of biodegradation kinetics and power production characteristics.

     

Co-Metabolic Biodegradation of DBP by Paenibacillus sp. S-3 and H-2

Two di-n-butyl phthalate (DBP)-degrading strains, designated as S-3 and H-2, were isolated from DBP-polluted soil and both identified as Paenibacillus sp. When DBP was provided as the sole carbon source, about 45.5 and 71.7 % of DBP (100 mg/L) were degraded by strain S-3 and H-2, respectively, after incubation for 48 h. However, DBP (100 mg/L) was degraded completely by co-culture of strain S-3 and H-2 after incubation for 60 h. Four phthalic acid (PA) esters could be utilized by co-metabolism in the study and the degradation rates followed the order of dimethyl phthalate > diethyl phthalate > DBP > dioctyl phthalate. The metabolic pathway of DBP was elucidated based on the results of metabolites identification and enzyme assays. For strain S-3, DBP was degraded into butyl hydrogen phthalate which was degraded to PA by carboxyesterase further. But PA could be not hydrolyzed further because strain S-3 lacked 3,4-phthalate dioxygenase. Different with S-3, strain H-2 could hydrolyze PA into 3,4-dihydroxy-PA by 3,4-phthalate dioxygenase. Then 3,4-dihydroxy-PA was converted to protocatechuate and benzoic acid. Finally, the aromatic ring was cleavage and mineralized to CO₂ and H₂O. Above all, co-metabolism could increase the activity of 3,4-phthalate dioxygenase and accelerated the degradation of DBP. This study highlights an important potential use of co-metabolic biodegradation for the in situ bioremediation of DBP and its metabolites-contaminated environment.     

Characterization of a d-psicose-producing enzyme, d-psicose 3-epimerase, from Clostridium sp.

The gene coding for d-psicose 3-epimerase (DPEase) from Clostridium sp. BNL1100 was cloned and expressed in Escherichia coli. The recombinant enzyme was purified by Ni-affinity chromatography. It was a metal-dependent enzyme and required Co²⁺ as optimum cofactor. It displayed catalytic activity maximally at pH 8.0 and 65 °C (as measured over 5 min). The optimum substrate was d-psicose, and the K _m, turnover number (k _cat), and catalytic efficiency (k _cat/K _m) for d-psicose were 227 mM, 32,185 min^?1, and 141 min^?1 mM^?1, respectively. At pH 8.0 and 55 °C, 120 g d-psicose l^?1 was produced from 500 g d-fructose l^?1 after 5 h.     

Highly selective hydrolysis for the outer glucose at the C-20 position in ginsenosides by β-glucosidase from Thermus thermophilus and its application to the production of ginsenoside F2 from gypenoside XVII

β-Glucosidase from Thermus thermophilus has specific hydrolytic activity for the outer glucose at the C-20 position in protopanaxadiol-type ginsenosides without hydrolysis of the inner glucose. The hydrolytic activity of the enzyme for gypenoside XVII was optimal at pH 6.5 and 90 °C, with a half-life of 1 h with 3 g enzyme l^?1 and 4 g gypenoside XVII l^?1. Under the optimized conditions, the enzyme converted the substrate gypenoside XVII to ginsenoside F₂ with a molar yield of 100 % and a productivity of 4 g l^?1 h^?1. The conversion yield and productivity of ginsenoside F₂ are the highest reported thus far among enzymatic transformations.     

Phenol Biodegradation and Metal Removal by a Mixed Bacterial Consortium

This paper reports the tolerance and biodegradation of phenol by a heavy metal–adapted environmental bacterial consortium, known as consortium culture (CC). At the highest tolerable phenol concentration of 1200 mg/L, CC displayed specific growth rate of 0.04 h^?1, phenol degradation rate of 6.11 mg L^?1 h^?1 and biomass of 8.45 ± 0.35 (log₁₀ colony-forming units [CFU]/ml) at the end of incubation. Phenol was degraded via the ortho-cleavage pathway catalyzed by cathechol-1,2-dioxygenase with specific activity of 0.083 (µmol min^?1 mg^?1 protein). The different constituent bacterial isolates of CC preferentially grow on benzene, toluene, xylene, ethylbenzene, cresol, and catechol, suggesting a synergistic mechanism involved in the degradation process. Microtox assay showed that phenol degradation was achieved without producing toxic dead-end metabolites. Moreover, lead (Pb) and cadmium (Cd) at the highest tested concentration of 1.0 and 0.1 mg/L, respectively, did not inhibit phenol degradation by CC. Simultaneous metal removal during phenol degradation was achieved using CC. These findings confirmed the dual function of CC to degrade phenol and to remove heavy metals from a mixed-pollutant medium.     

Production of ginsenosides Rg1 and Rh1 by hydrolyzing the outer glycoside at the C-6 position in protopanaxatriol-type ginsenosides using β-glucosidase from Pyrococcus furiosus

The specific activity of a recombinant β-glucosidase from Pyrococcus furiosus for protopanaxatriol (PPT)-type ginsenosides followed the order Rf > R₁ > Re > R₂ > Rg₂, which were converted to Rh₁, Rg₁, Rg₁, Rh₁, and Rh₁, respectively. No activity was observed with Rg₁ and Rh₁. Thus, P. furiosus β-glucosidase hydrolyzed the outer glycoside at the C-6 position in PPT-type ginsenosides whereas the enzyme did not hydrolyze the inner glucoside at the C-6 position and the glucoside at the C-20 position. The activity for Rf was optimal at 95 °C, pH 5.5, 5 mM ginsenoside, and 32 U enzyme l^?1. Under these conditions, P. furiosus β-glucosidase completely converted from R₁ to Rg₁ after 10 h, with a productivity of 0.4 g l^?1 h^?1 and completely converted Rf to Rh₁ after 1.2 h, with a productivity of 2.74 g l^?1 h^?1.     

Microbial lipid production: screening with yeasts grown on Brazilian molasses

Rhodotorula glutinis CCT 2182, Rhodosporidium toruloides CCT 0783, Rhodotorula minuta CCT 1751 and Lipomyces starkeyi DSM 70296 were evaluated for the conversion of sugars from Brazilian molasses into single-cell oil (SCO) feedstock for biodiesel. Pulsed fed-batch fermentations were performed in 1.65 l working volume bioreactors. The maximum specific growth rate (µ_max), lipid productivity (Pr) and cellular lipid content were, respectively, 0.23 h^?1, 0.41 g l^?1 h^?1, and 41 % for Rsp. toruloides; 0.20 h^?1, 0.27 g l^?1 h^?1, and 36 % for Rta. glutinis; 0.115 h^?1, 0.135 g l^?1 h^?1, and 27 % for Rta. minuta; and 0.11 h^?1, 0.13 g l^?1 h^?1, and 32 % for L. starkeyi. Based on their microbial lipid productivity, content, and profile, Rsp. toruloides and Rta. glutinis are promising candidates for biodiesel production from Brazilian molasses. All the oils from the yeasts were similar to the composition of plant oils (rapeseed and soybean) and could be used as raw material for biofuels, as well as in food and nutraceutical products.     

Increased production of γ-lactones from hydroxy fatty acids by whole Waltomyces lipofer cells induced with oleic acid

Among several fatty acids tested, oleic acid was selected as the most efficient inducer for the production of 4-hydroxydodecanoic acid, a metabolite of β-oxidation, by Waltomyces lipofer. Cells were induced by incubation for 12 h in a medium containing 10 g l^?1 yeast extract, 10 g l^?1 peptone, 5 g l^?1 oleic acid, 1 g l^?1 glucose, and 0.05 % (w/v) Tween 80. The optimal reaction conditions for the production of γ-lactones by induced cells were pH 6.5, 35 °C, 200 rpm, 0.71 M Tris, 60 g l^?1 hydroxy fatty acid, and 20 g l^?1 cells. Non-induced cells produced 38 g l^?1 γ-dodecalactone from 60 g l^?1 10-hydroxystearic acid after 30 h, with a conversion yield of 63 % (w/w) and a productivity of 1.3 g l^?1 h^?1 under the optimized conditions, whereas induced cells produced 51 g l^?1 γ-dodecalactone from 60 g l^?1 10-hydroxystearic acid after 30 h, with a conversion yield of 85 % (w/w) and a productivity of 1.7 g l^?1 h^?1. The conversion yield and productivity of induced cells were 22 % and 1.3-fold higher, respectively, than those of non-induced cells. Induced cells also produced 28 g l^?1 γ-decalactone and 12 g l^?1 γ-butyrolactone from 60 g l^?1 12-hydroxystearic acid and 60 g l^?1 10-hydroxydecanoic acid, respectively, after 30 h. The concentration, conversion yield, and productivity of γ-dodecalactone and γ-decalactone are the highest reported thus far. This is the first study on the biotechnological production of γ-butyrolactone.     

Biodecolorization of textile azo dyes by isolated yeast from activated sludge: Issatchenkia orientalis JKS6

An ascomycetous yeast strain isolated from activated sludge could decolorize Reactive Black 5 azo dye at 200 mg l^?1 up to 90 % within 12–18 h under agitated condition. Yeast decolorization ability was investigated at different RB5 concentrations and, at higher dye concentration, 500 mg l^?1, the decolorization was found to be 98 % after 36 h incubation time. Extensive decolorization (95–99 %) was obtained in presence of five other azo dyes, Reactive Orange 16, Reactive Red 198, Direct Blue 71, Direct Yellow 12, and Direct Black 22, by isolated yeast. HPLC analysis, UV–vis spectra and colorless biomass obtained after complete decolorization showed that the decolorization occured through a biodegradation mechanism. Decolorization was occurred during the exponential growth phase which is associated to primary metabolism. Laccase production by the yeast cells was not detected. The isolated yeast was characterized according to phenotypical and molecular procedures and was closely related (99 % identity) to Issatchenkia orientalis.     

Assessing biodegradation of furfuryl alcohol using <Emphasis Type="Italic">Pseudomonas putida</Emphasis> MTCC 1194 and <Emphasis Type="Italic">Pseudomonas aeruginosa</Emphasis> MTCC 1034 and its kinetics

The biodegradation of furfuryl alcohol (FA) in shake flask experiments using a pure culture of Pseudomonas putida (MTCC 1194) and Pseudomonas aeruginosa (MTCC 1034) was studied at 30 °C and pH 7.0. Experiments were performed at different FA concentrations ranging from 50 to 500 mg/l. Before carrying out the biodegradation studies, the bacterial strains were acclimatized to the concentration of 500 mg/l of FA by gradually raising 100 mg/l of FA in each step. The well acclimatized culture of P. putida and P. aeruginosa degraded about 80 and 66% of 50 mg/l FA, respectively. At higher concentration of FA, the percentage of FA degradation decreased. The purpose of this study was to determine the kinetics of biodegradation of FA by measuring biomass growth rates and concentration of FA as a function of time. Substrate inhibition was calculated from experimental growth parameters using the Haldane equation. Data for P. putida were determined as µ _max ?=?0.23 h^?1, K _s ?=?23.93 mg/l and K _i ?=?217.1 mg/l and for P. aeruginosa were determined as µ _max ?=?0.13 h^?1, K _s ?=?21.3 mg/l and K _i ?=?284.9 mg/l. The experimental data were fitted in Haldane, Aiba and Edwards inhibition models.     

Effect of controlled oxygen limitation on Candida shehatae physiology for ethanol production from xylose and glucose

Carbon distribution and kinetics of Candida shehatae were studied in fed-batch fermentation with xylose or glucose (separately) as the carbon source in mineral medium. The fermentations were carried out in two phases, an aerobic phase dedicated to growth followed by an oxygen limitation phase dedicated to ethanol production. Oxygen limitation was quantified with an average specific oxygen uptake rate (OUR) varying between 0.30 and 2.48 mmolO₂ g dry cell weight (DCW)^?1 h^?1, the maximum value before the aerobic shift. The relations among respiration, growth, ethanol production and polyol production were investigated. It appeared that ethanol was produced to provide energy, and polyols (arabitol, ribitol, glycerol and xylitol) were produced to reoxidize NADH from assimilatory reactions and from the co-factor imbalance of the two-first enzymatic steps of xylose uptake. Hence, to manage carbon flux to ethanol production, oxygen limitation was a major controlled parameter; an oxygen limitation corresponding to an average specific OUR of 1.19 mmolO₂ g DCW^?1 h^?1 allowed maximization of the ethanol yield over xylose (0.327 g g^?1), the average productivity (2.2 g l^?1 h^?1) and the ethanol final titer (48.81 g l^?1). For glucose fermentation, the ethanol yield over glucose was the highest (0.411 g g^?1) when the specific OUR was low, corresponding to an average specific OUR of 0.30 mmolO₂ g DCW^?1 h^?1, whereas the average ethanol productivity and ethanol final titer reached the maximum values of 1.81 g l^?1 h^?1 and 54.19 g l^?1 when the specific OUR was the highest.     

Enhanced production of hairy root metabolites using microbubble generator

Previously, increased partitioning of the natural product nicotine from tobacco hairy roots into the culture media was achieved by altering the expression of the nicotine uptake permease gene. The present study demonstrated that further increases in nicotine yield in the media were attained by using surfactant-stabilized microbubbles. Compared to other non-ionic surfactants (Tween 20 and Tween 80) and the ionic surfactant SDS, Triton X-100 (TX100) both increased total nicotine production and exudation into the hairy root culture media. In comparison to surfactant-free medium, TX100 at 10, 25, and 50 mg l^?1 did not show strong inhibition of hairy root growth. At 4,000 rpm shear speed, microbubbles stabilized by 10, 25, and 50 mg l^?1 TX100 had k _L a of 22.3, 36.2, and 44.1 h^?1 in Gamborg’s B5 medium, respectively, in comparison to 16.4 h^?1 with conventional air sparging. In a 1-l bioreactor, microbubbles stabilized by TX100 were applied to hairy roots after the inoculated root tips were self-immobilized by branching. With microbubble dispersion, dissolved oxygen rapidly increased from 60 to 85 %, and hairy root growth rate increased. Nicotine accumulation in culture medium with microbubbles reached 146 mg l^?1 after 30 days cultivation. These results show that combining genetic modification with surfactant-stabilized microbubble dispersion can substantially increase levels of nicotine in the media of hairy root cultures.     

Aerobic decolorization of Acid Brilliant Scarlet GR by microbial community and the community dynamics during sequencing batch processes

In this research, aerobic decolorization of Acid Brilliant Scarlet GR by microbial community was studied. Effects of conditions and dye concentraion on decolorization processes were investigated. Additionally, continuous decolorization was evaluated through sequencing batch tests and the microbial dynamics during this process was analyzed by polymerase chain reaction-denaturing gradient gel electrophoresis. The results showed that 100 mg l^?1 of the dye was completely decolorized within 12 h, which was mainly caused by biodegradation. The optimal decolorization conditions were as follows: inoculation size 2.07 g l^?1 (wet cell pellet), rotation speed 150 r min^?1, pH 5.0–7.0 and 30 °C. The processes were well described by zero-order kinetics, and more than 700 mg l^?1 of the dye would inhibit the activity of the consortium. Furthermore, the microbial community exhibited high efficiency in sequencing batch processes for continuous decolorization. Microbial community structure shifted obviously when exposed to higher concentration of the dye (500 mg l^?1), and all the dominant microorganisms were affiliated with four different phyla of Actinobacteria, Bacteroidetes, Proteobacteria and Firmicutes.     

Recovery of avocado (<Emphasis Type="Italic">Persea americana</Emphasis> Mill.) plants transformed with the antifungal plant defensin gene PDF1.2

Embryogenic avocado cultures derived from ‘Hass’ protoplasts were genetically transformed with the plant defensin gene (pdf1.2) driven by the CaMV 35S promoter in pGPTV with uidA as a reporter gene and bar, the gene for resistance to phosphinothricin, the active ingredient of the herbicide Finale® (Basta) (Bayer Environmental Science, Research Triangle Park, Durham, NC ). Transformation was mediated by Agrobacterium tumefaciens strain EHA105. Transformed cultures were selected in the presence of 3.0 mg l^?1 phosphinothricin in liquid maintenance medium for 3–4 mo. Liquid maintenance medium consisted of modified MS medium containing (per liter) 12 mg NH₄NO₃ and 30.3 mg KNO₃ and supplemented with 0.1 mg l^?1 thiamine HCl, 100 mg l^?1 myo-inositol, 30 g l^?1 sucrose, 3.0 mg l^?1 phosphinothricin, and 0.41 μM picloram. Somatic embryo development from transformed cultures was initiated on MS medium supplemented with 45 g l^?1 sucrose, 4 mg l^?1 thiamine HCl, 100 mg l^?1 myo-inositol, 10% (v/v) filter-sterilized coconut water, 3.0 mg l^?1 phosphinothricin, and 6.0 g l^?1 gellan gum. Limited plant recovery occurred from somatic embryos on semi-solid MS medium supplemented with 3.0 mg l^?1 phosphinothricin, 4.44 μM 6-benzylaminopurine (BA), and 2.89 μM GA₃; transformed shoots were micrografted on in vitro-grown seedling rootstocks. Approximately 1 yr after acclimatization in the greenhouse, transformed shoots were air-layered to recover transformed roots. Genetic transformation of embryogenic cultures, somatic embryos, and regenerated plants was confirmed by polymerase chain reaction (PCR), Southern blot hybridization, the XGLUC reaction for uidA, and application of the herbicide Finale® to regenerated plants.