Purified Penicillin Binding Proteins 1Bs from Escherichia coli Membrane Showing Activities of Both Peptidoglycan Polymerase and Peptidoglycan Crosslinking Enzyme

Our biotransformation using Escherichia coli expressing a cytochrome P450 (CYP) belonging to the CYP153A family from Acinetobacter sp. OC4 produced a great amount of 1-octanol (2,250 mg per liter) from n-octane after 24 h of incubation. This level of production is equivalent to the maximum level previously achieved in biotransformation experiments of alkanes. In addition, the initial production rate of 1-octanol was maintained throughout the entire incubation period. These results indicate that we have achieved the functional and stable expression of a CYP in E. coli for the first time. Further, our biotransformation system showed α,ω-diterminal oxidation activity of n-alkanes, and a large amount of 1,8-octanediol (722 mg per liter) was produced from 1-octanol after 24 h of incubation. This is the first report on the bioproduction of α,ω-alkanediols from n-alkanes or 1-alkanols.     

Highly efficient biotransformation of eugenol to ferulic acid and further conversion to vanillin in recombinant strains of Escherichia coli

The vaoA gene from Penicillium simplicissimum CBS 170.90, encoding vanillyl alcohol oxidase, which also catalyzes the conversion of eugenol to coniferyl alcohol, was expressed in Escherichia coli XL1-Blue under the control of the lac promoter, together with the genes calA and calB, encoding coniferyl alcohol dehydrogenase and coniferyl aldehyde dehydrogenase of Pseudomonas sp. strain HR199, respectively. Resting cells of the corresponding recombinant strain E. coli XL1-Blue(pSKvaomPcalAmcalB) converted eugenol to ferulic acid with a molar yield of 91% within 15 h on a 50-ml scale, reaching a ferulic acid concentration of 8.6 g liter(-1). This biotransformation was scaled up to a 30-liter fermentation volume. The maximum production rate for ferulic acid at that scale was 14.4 mmol per h per liter of culture. The maximum concentration of ferulic acid obtained was 14.7 g liter(-1) after a total fermentation time of 30 h, which corresponded to a molar yield of 93.3% with respect to the added amount of eugenol. In a two-step biotransformation, E. coli XL1-Blue(pSKvaomPcalAmcalB) was used to produce ferulic acid from eugenol and, subsequently, E. coli(pSKechE/Hfcs) was used to convert ferulic acid to vanillin (J. Overhage, H. Priefert, and A. Steinbüchel, Appl. Environ. Microbiol. 65:4837-4847, 1999). This process led to 0.3 g of vanillin liter(-1), besides 0.1 g of vanillyl alcohol and 4.6 g of ferulic acid liter(-1). The genes ehyAB, encoding eugenol hydroxylase of Pseudomonas sp. strain HR199, and azu, encoding the potential physiological electron acceptor of this enzyme, were shown to be unsuitable for establishing eugenol bioconversion in E. coli XL1-Blue.     

Involvement of acyl coenzyme A oxidase isozymes in biotransformation of methyl ricinoleate into gamma-decalactone by Yarrowia lipolytica

We reported previously on the function of acyl coenzyme A (acyl-CoA) oxidase isozymes in the yeast Yarrowia lipolytica by investigating strains disrupted in one or several acyl-CoA oxidase-encoding genes (POX1 through POX5) (H. Wang et al., J. Bacteriol. 181:5140-5148, 1999). Here, these mutants were studied for lactone production. Monodisrupted strains produced similar levels of lactone as the wild-type strain (50 mg/liter) except for Deltapox3, which produced 220 mg of gamma-decalactone per liter after 24 h. The Deltapox2 Deltapox3 double-disrupted strain, although slightly affected in growth, produced about 150 mg of lactone per liter, indicating that Aox2p was not essential for the biotransformation. The Deltapox2 Deltapox3 Deltapox5 triple-disrupted strain produced and consumed lactone very slowly. On the contrary, the Deltapox2 Deltapox3 Deltapox4 Deltapox5 multidisrupted strain did not grow or biotransform methyl ricinoleate into gamma-decalactone, demonstrating that Aox4p is essential for the biotransformation.     

Involvement of Acyl Coenzyme A Oxidase Isozymes in Biotransformation of Methyl Ricinoleate into γ-Decalactone by Yarrowia lipolytica

We reported previously on the function of acyl coenzyme A (acyl-CoA) oxidase isozymes in the yeast Yarrowia lipolytica by investigating strains disrupted in one or several acyl-CoA oxidase-encoding genes (POX1 through POX5) (H. Wang et al., J. Bacteriol. 181:5140–5148, 1999). Here, these mutants were studied for lactone production. Monodisrupted strains produced similar levels of lactone as the wild-type strain (50 mg/liter) except for Δpox3, which produced 220 mg of γ-decalactone per liter after 24 h. The Δpox2 Δpox3 double-disrupted strain, although slightly affected in growth, produced about 150 mg of lactone per liter, indicating that Aox2p was not essential for the biotransformation. The Δpox2 Δpox3 Δpox5 triple-disrupted strain produced and consumed lactone very slowly. On the contrary, the Δpox2 Δpox3 Δpox4 Δpox5 multidisrupted strain did not grow or biotransform methyl ricinoleate into γ-decalactone, demonstrating that Aox4p is essential for the biotransformation.     

Homofermentative production of D- or L-lactate in metabolically engineered Escherichia coli RR1

We investigated metabolic engineering of fermentation pathways in Escherichia coli for production of optically pure D- or L-lactate. Several pta mutant strains were examined, and a pta mutant of E. coli RR1 which was deficient in the phosphotransacetylase of the Pta-AckA pathway was found to metabolize glucose to D-lactate and to produce a small amount of succinate by-product under anaerobic conditions. An additional mutation in ppc made the mutant produce D-lactate like a homofermentative lactic acid bacterium. When the pta ppc double mutant was grown to higher biomass concentrations under aerobic conditions before it shifted to the anaerobic phase of D-lactate production, more than 62.2 g of D-lactate per liter was produced in 60 h, and the volumetric productivity was 1.04 g/liter/h. To examine whether the blocked acetate flux could be reoriented to a nonindigenous L-lactate pathway, an L-lactate dehydrogenase gene from Lactobacillus casei was introduced into a pta ldhA strain which lacked phosphotransacetylase and D-lactate dehydrogenase. This recombinant strain was able to metabolize glucose to L-lactate as the major fermentation product, and up to 45 g of L-lactate per liter was produced in 67 h. These results demonstrate that the central fermentation metabolism of E. coli can be reoriented to the production of D-lactate, an indigenous fermentation product, or to the production of L-lactate, a nonindigenous fermentation product.     

Process and metabolic strategies for improved production of Escherichia coli-derived 6-deoxyerythronolide B

Recently, the feasibility of using Escherichia coli for the heterologous biosynthesis of complex polyketides has been demonstrated. In this report, the development of a robust high-cell-density fed-batch procedure for the efficient production of complex polyketides is described. The effects of various physiological conditions on the productivity and titers of 6-deoxyerythronolide B (6dEB; the macrocyclic core of the antibiotic erythromycin) in recombinant cultures of E. coli were studied in shake flask cultures. The resulting data were used as a foundation to develop a high-cell-density fermentation procedure by building upon procedures reported earlier for recombinant protein production in E. coli. The fermentation strategy employed consistently produced approximately 100 mg of 6dEB per liter, whereas shake flask conditions generated between 1 and 10 mg per liter. The utility of an accessory thioesterase (TEII from Saccharopolyspora erythraea) for enhancing the productivity of 6dEB in E. coli was also demonstrated (increasing the final titer of 6dEB to 180 mg per liter). In addition to reinforcing the potential for using E. coli as a heterologous host for wild-type- and engineered-polyketide biosynthesis, the procedures described in this study may be useful for the production of secondary metabolites that are difficult to access by other routes.     

重组大肠杆菌全细胞催化合成莱鲍迪苷D

莱鲍迪苷D(Rebaudioside D,RD)是一种稀有具有高甜度的甜菊糖苷类化合物。本文实现了重组大肠杆菌全细胞催化莱鲍迪苷A(Rebaudioside A,RA)合成RD。以水稻c DNA为模板,扩增得到葡萄糖基转移酶基因eugt11,构建了重组菌株E.coli BL21(p ETDuet-eugt11),并成功表达了重组蛋白6His-EUGT11。通过Ni柱亲和层析纯化并在体外酶催化反应表征了其催化活性。将重组菌BL21(p ETDuet-eugt11)应用于催化合成RD研究。探讨了反应体系pH、温度、柠檬酸钠浓度、菌体密度、二价金属离子、二甲苯体积分数、UDPG添加浓度对反应效率的影响。单因素考察结果显示,在菌体密度0.16 g湿细胞/m L反应液,底物RA浓度为1.0 mmol/L,pH 8.0,60 mmol/L柠檬酸钠,1%二甲苯,0.1 mmol/L Zn Cl2,12.0 mmol/L UDPG,反应温度42℃,反应时间24 h的条件下,RD产量为123.6 mg/L(约0.1 mmol/L)。     

Candida galli Strain PGO6: A Novel Isolated Yeast Strain Capable of Transformation of Isoeugenol into Vanillin and Vanillic Acid

Candida galli strain PGO6 isolated from oil-contaminated water is the first isolated yeast strain which is capable to form vanillin and vanillic acid during isoeugenol biotransformation. The products were confirmed by thin-layer chromatography (TLC), changes in the UV absorption pattern and high-performance liquid chromatography (HPLC). The phenotypic and physiochemical characteristics as well as molecular phylogenetic analysis based on amplification the ITS1-5.8S-ITS2 rDNA regions indicated the isolated strain PGO6 was identified as C. galli (GenBank accession number HM641231). Resting cells of C. galli PGO6 from the late-exponential of growth phase were used as biocatalysts for the biotransformation of isoeugenol. The optimal molar conversion of vanillin (48%) and vanillic acid (19%) was obtained after a 30 h incubation using 0.1% (v/v) of isoeugenol and 6 mg of dry weight of cells per ml without further optimization. Under these conditions, the total amount of vanillin and vanillic acid was 583 mg l(-1). Further biotransformation was carried out using 0.5% (v/v) of isoeugenol under the resting cells conditions, yielding a vanillin concentration of 1.12 g l(-1) (molar yield 25.7%) after 60 h incubation. This study brings the first evidence for biotransformation of isoeugenol to vanillin and vanillic acid by a yeast strain.     

Efficiency of bacterial protein synthesis during anaerobic degradation of cattle waste.

The rate of [15N]ammonia (15NH3) uptake or incorporation into bacterial cells was studied, using stirred, 3-liter benchtop digestors fed on a semicontinuous basis with cattle waste. The fermentations were carried out at 40 and 60 degrees C and at four different loading rates (3, 6, 9, and 12 g of volatile solids per liter of reactor volume per day). The rate of NH3-N incorporation for the period 1 to 5 h after feeding at the four different loading rates was 0.49, 0.83, 1.05, and 1.08 mg/liter per h in the mesophilic digestor and 0.68, 1.07, 1.17, and 1.21 mg/liter per h in the thermophilic digestor. Values were lower 7 to 21 h after feeding in both digestors and were related to the rate of fermentation or CH4 production. In the mesophilic digestors, the rate of bacterial cell production ranged from 3.97 to 8.72 mg of dry cells per liter per h, 1 to 5 h after feeding at the different loading rates. Corresponding values for the thermophilic digestors ranged from 5.46 to 9.77 mg of dry cells per liter per h. Cell yield values ranged from 2.3 to 3.1 mg of dry cells per mol of CH4 produced in the mesophilic and thermophilic digestors at the two lower loading rates. The values were higher (2.8 to 3.4) in the mesophilic digestors at the two higher loading rates because of the accumulation of propionate and a consequent reduction in CH4 production. Low cell yields such as those measured in this study are characteristic of low-specific-growth rates under energy-limited conditions.     

Efficiency of bacterial protein synthesis during anaerobic degradation of cattle waste

The rate of [15N]ammonia (15NH3) uptake or incorporation into bacterial cells was studied, using stirred, 3-liter benchtop digestors fed on a semicontinuous basis with cattle waste. The fermentations were carried out at 40 and 60 degrees C and at four different loading rates (3, 6, 9, and 12 g of volatile solids per liter of reactor volume per day). The rate of NH3-N incorporation for the period 1 to 5 h after feeding at the four different loading rates was 0.49, 0.83, 1.05, and 1.08 mg/liter per h in the mesophilic digestor and 0.68, 1.07, 1.17, and 1.21 mg/liter per h in the thermophilic digestor. Values were lower 7 to 21 h after feeding in both digestors and were related to the rate of fermentation or CH4 production. In the mesophilic digestors, the rate of bacterial cell production ranged from 3.97 to 8.72 mg of dry cells per liter per h, 1 to 5 h after feeding at the different loading rates. Corresponding values for the thermophilic digestors ranged from 5.46 to 9.77 mg of dry cells per liter per h. Cell yield values ranged from 2.3 to 3.1 mg of dry cells per mol of CH4 produced in the mesophilic and thermophilic digestors at the two lower loading rates. The values were higher (2.8 to 3.4) in the mesophilic digestors at the two higher loading rates because of the accumulation of propionate and a consequent reduction in CH4 production. Low cell yields such as those measured in this study are characteristic of low-specific-growth rates under energy-limited conditions.     

High-level expression of human cytochrome P450 1A2 by co-expression with human molecular chaperone HDJ-1(Hsp40)

Human cytochrome P450 (CYP) 1A2 is of great interest because of its important roles in the oxidation of numerous drugs and carcinogens. HDJ-1, a molecular chaperone in human, is known to assist the correct folding of unfolded proteins. To achieve high yield of recombinant human CYP1A2 in Escherichia coli, the CYP1A2 encoding gene was co-expressed with the chaperone HDJ-1 under the control of an inducible tac promoter in bicistronic format. Expression level of CYP1A2 in the bicistronic construct reached up to 520 nmol/liter culture within 16 h at 37 degrees C, which is 3.4-fold increase compared to the expression yield of CYP1A2 alone without HDJ-1. By co-expression with HDJ-1, the catalytic activity of CYP1A2 was also increased 5.5-fold. The activity increase seems to be associated with the increase of CYP production at whole cell level. The present over-expression system may be useful for rapid production of large amounts of active human CYP1A2 in E. coli.     

代谢工程方法改造大肠杆菌生产胸苷

胸苷是抗艾滋病药物司他夫定(3′-脱氧-2′,3′-双脱氢胸苷)和叠氮胸苷的重要前体物质。应用代谢工程方法对大肠杆菌Escherichia coli BL21(DE3)生物合成胸苷进行了研究。通过敲除E.coli BL21嘧啶回补途径的deo A、tdk和udp三个基因,BS03工程菌株能够积累21.6 mg/L胸苷。为了增加合成胸苷前体物核糖-5-磷酸和NADPH的供给,进一步敲除pgi和pyr L使工程菌BS05胸苷的产量提高到90.5 mg/L。而通过过表达胸苷合成途径的ush A、thy A、dut、ndk、nrd A和nrd B六个基因,菌株BS08胸苷的产量能达到272 mg/L。通过分批补料发酵,BS08最终可以积累1 248.8 mg/L的胸苷。本研究结果表明经过代谢工程改造的E.coli BL21具有良好的胸苷合成能力和应用潜力。     

Prostaglandin production by corpora lutea of rhesus monkeys: characterization of incubation conditions and examination of putative regulators

Prostaglandins (PGs) are produced by the corpus luteum (CL) of many domestic and laboratory species and may play a role in CL regulation. The production of PGs by luteal tissue of the rhesus monkey has yet to be clearly elucidated. The production of PGE2, PGF2 alpha, and 6-keto-PGF1 alpha by CL from rhesus monkeys and the incubation conditions (time and cell number) that permit assessment of their synthesis were examined. CL (n = 3 per characterization) were surgically removed from nonpregnant monkeys during the mid-luteal phase of the menstrual cycle (approximately 8-10 days after ovulation). Luteal tissue was dissociated and the cells were incubated at varying concentrations for increasing periods of time at 37 degrees C. Subsequent to defining incubation conditions, various exogenous factors were examined for their potential to modify PG production. Indomethacin, calcium ionophore, human chorionic gonadotropin (hCG), estradiol-17 beta (E2), progesterone (P), testosterone (T), dihydrotestosterone (DHT), and 1-4-6 androstatriene-3, 17-dione (ATD) were incubated with luteal cells in increasing doses. PG and P concentrations in the medium were determined by radioimmunoassay. PGs in the medium after 6 h incubation were detectable at all cell concentrations tested (50,000, 100,000, 200,000 cells/tube). Concentrations of PGs and P increased with cell number (p less than 0.05). Luteal cells (50,000 cells/tube) were incubated for times of 0-24 h. Concentrations of P, PGE2, and PGF2 alpha in the medium were relatively low prior to incubation (0 h), increased (p less than 0.05) linearly within the first 6-12 h, and plateaued through the remaining 24 h.(ABSTRACT TRUNCATED AT 250 WORDS)     

Production of Thermostable alpha-Amylase, Pullulanase, and alpha-Glucosidase in Continuous Culture by a New Clostridium Isolate

The production of alpha-amylase, pullulanase, and alpha-glucosidase and the formation of fermentation products by the newly isolated thermophilic Clostridium sp. strain EM1 were investigated in continuous culture with a defined medium and an incubation temperature of 60 degrees C. Enzyme production and excretion were greatly influenced by the dilution rate and the pH of the medium. The optimal values for the formation of starch-hydrolyzing enzymes were a pH of 5.9 and a dilution rate of 0.075 to 0.10 per h. Increase of the dilution rate from 0.1 to 0.3 per h caused a drastic drop in enzyme production. The ethanol concentration and optical density of the culture, however, remained almost constant. Growth limitation in the chemostat with 1% (wt/vol) starch was found optimal for enzyme production. Under these conditions 2,800 U of pullulanase per liter and 1,450 U of alpha-amylase per liter were produced; the amounts excreted were 70 and 55%, respectively.     

Production of higher alcohols during indonesian tapé ketan fermentation

A study was made of the higher alcohols (fusel oils) produced during the Indonesian tapé ketan fermentation using Amylomyces rouxii as the principal mold, alone or in combination with yeasts belonging to genera commonly found in the tapé ketan fermentation (Endomycopsis, Candida, and Hansenula). Total fusel oils increased with length of fermentation. Fusel oils detected in the product distillate included isobutanol and isoamyl and active amyl alcohols. No n-propanol was detected. Isobutanol and isoamyl alcohols were formed in the largest amounts. A. rouxii alone produced nearly the same quantity of fusel oils (total production, 275 mg/liter at 192 h) as it did in combination with Endomycopsis burtonii (total production, 292 mg/liter at 192 h).A. rouxii and Endomycopsis fibuliger produced fusel oils totaling 72 mg/liter at 32 h and 558 mg/liter at 192 h. A. rouxii in combination with Candida yeasts produced somewhat more fusel oils, ranging from 590 to 618 mg/liter at 192 h. A. rouxii in combination with Hansenula yeasts produced the least fusel oils, totaling 143 to 248 mg/liter at 192 h. During the first 36 h, production of fusel oils was higher at 30 and 35 degrees C than at 25 degrees C. At 48 h fusel oil production was slightly higher at 30 degrees C than at 35 degrees C. Beyond 48 h, production of fusel oils was higher at 25 degrees C. A. rouxii in combination with Hansenula anomala and Hansenula subpelliculosa produced considerable ethyl acetate, ranging from 145 to 199 mg/liter at 36 h and 354 to 369 mg/liter at 192 h.     

High-level production of hyperthermophilic cellulase in the Bacillus brevis expression and secretion system

A hyperthermophilic cellulase derived from Pyrococcus horikoshii was successfully produced with the Bacillus brevis host-vector system. The production of the recombinant enzyme was increased about 20-fold (to a level of 100 mg per liter) by the insertion of certain amino acid such as alanine and peptides like AEEAADP between the carboxyl end of signal peptide and the N-terminus of the mature cellulase. These recombinant cellulases had the same characteristics as that of the cellulase expressed in Escherichia coli.     

Production of Pseudomonas aeruginosa Rhamnolipid Biosurfactants in Heterologous Hosts

The high-level production of rhamnolipid biosurfactants is a unique feature of Pseudomonas aeruginosa and is strictly regulated in response to environmental conditions. The final step in rhamnolipid biosynthesis is catalyzed by the rhlAB genes encoding a rhamnosyltransferase. The expression of the cloned rhlAB genes was studied in heterologous hosts, either under the control of the rhlR and rhlI rhamnolipid regulatory elements or under the control of the tac promoter. A recombinant P. fluorescens strain harboring multiple plasmid-encoded copies of the rhamnolipid gene cluster produced rhamnolipids (0.25 g liter(sup-1)) when grown under nitrogen-limiting conditions. The highest yields (0.6 g liter(sup-1)) and productivities (24 mg liter(sup-1) h(sup-1)) were obtained in a recombinant Pseudomonas putida strain, KT2442, harboring promoterless rhlAB genes fused to the tac promoter on a plasmid. Active rhamnosyltransferase was synthesized, but no rhamnolipids were produced, by recombinant Escherichia coli upon induction of rhlAB gene expression.     

Comparison of the biotransformation of the 14C-labelled insecticide carbaryl by non-transformed and human CYP1A1-, CYP1A2-, and CYP3A4-transgenic cell cultures of Nicotiana tabacum

Transgenic tobacco-cell-suspension cultures expressing separately the human cytochrome P450 monooxygenases CYP1A1, CYP1A2, and CYP3A4 were utilized to study the biotransformation of the 14C-labelled insecticide carbaryl (=naphthalen-1-yl methylcarbamate). The resulting data were compared to similar data from the corresponding non-transformed (NT) tobacco-cell culture and commercially available membrane preparations (Bactosomes) of genetically modified bacteria separately containing the same human P450s. A rapid conversion rate of carbaryl was observed with the CYP1A1 and CYP1A2 cells, where only 49.7 and 0.2% of applied carbaryl (1 mg/l), respectively, remained after 24 h, as compared to 77.7% in the non-transformed culture. Unexpectedly, the corresponding results obtained from the CYP3A4 cultures were not definite. With 25 mg/l of carbaryl and 96 h of incubation, it was proven that the insecticide is also substrate of CYP3A4. This finding was supported by GC/EI-MS analysis of the primary metabolite pattern produced by the isozyme. This consisted of naphthalene-1-ol, N-(hydroxymethyl)carbaryl, 4-hydroxycarbaryl, and 5-hydroxycarbaryl, whereas the main product in non-transformed cells was N-(hydroxymethyl)carbaryl. Data obtained from the CYP1A1, CYP1A2, or CYP3A4 Bactosomes agreed with those of the P450-transgenic tobacco cells. Problems with GC/EI-MS analysis of carbaryl and its metabolites are discussed.     

Enhanced production of D-(-)-3-hydroxybutyric acid by recombinant Escherichia coli

Wild-type bacteria including Escherichia coli normally do not produce extracellular D-(-)-3-hydroxybutyric acid (3HB). To produce extracellular chiral 3HB, a new pathway for synthesis of 3HB was constructed by simultaneous expression of genes of beta-ketothiolase (phbA), acetoacetyl-CoA reductase (phbB), phosphor-transbutyrylase (ptb) and butyrate kinase (buk) in E. coli strain DH5alpha. E. coli DH5alpha containing any one of the four plasmids pBHR69, pUCAB, p68CM or pKKAB that harbor the phbA and phbB genes produced small amounts of 3HB, ranging from 75 to 400 mg l(-1), while E. coli DH5alpha harboring p68CMPTK containing genes of phbA, phbB, ptb and buk increased the 3HB concentration to 1.4 g l(-1) in shake flasks supplemented with LB broth and 20 g l(-1) glucose. 3HB production was further improved to over 2 g l(-1) in shake flasks when E. coli DH5alpha hosted two plasmids simultaneously that separately contained phbA and phbB in one plasmid while ptb and buk in the other. A batch fermentation run in a 5-l fermenter produced approximately 5 g l(-1) 3HB after 24 h. A fed-batch process increased 3HB production to 12 g l(-1) after 48 h of fermentation.     

CYP79B1 from Sinapis alba converts tryptophan to indole-3-acetaldoxime

The cytochrome P450 CYP79B1 from Sinapis alba has been heterologously expressed in Escherichia coli and shown to catalyze the conversion of tryptophan to indole-3-acetaldoxime. Three expression constructs were made, one expressing the native protein and two expressing proteins with different N-terminal modifications. The native construct gave the highest yield as estimated by enzymatic activity per liter of culture. Spheroplasts of E. coli expressing CYP79B1 were reconstituted with the Arabidopsis thaliana NADPH:cytochrome P450 reductase ATR1 heterologously expressed in E. coli to obtain enzymatic activity. This indicates that the E. coli electron-donating system, flavodoxin/flavodoxin reductase, does not support CYP79B1 activity. Recombinant CYP79B1 has a K(m) for tryptophan of 29+/-2 microM and a V(max) of 36.5+/-0.7nmolh(-1)(mlculture)(-1). The identity at the amino acid level of CYP79B1 is, respectively, 93 and 84% to CYP79B2 and CYP79B3 from A. thaliana, and 96% to CYP79B5 (Accession No. AF453287) from Brassica napus. The CYP79B subfamily of cytochromes P450 is likely to constitute a group of orthologous genes in the biosynthesis of indole glucosinolates.