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Applied Microbiology and Biotechnology (v.51, #6)

Artificial redox coenzymes: biomimetic analogues of NAD⁺ by R. J. Ansell; C. R. Lowe (pp. 703-710).

A range of biomimetic analogues of the nicotinamide nucleotide coenzymes NAD(P)(H) have been developed based on the structure of a triazine dye template. These biomimetic redox coenzymes are relatively straightforward and inexpensive to synthesise and display NAD⁺-like activity with different dehydrogenases, despite their apparently minimal structural similarity to the native coenzyme NAD⁺. Horse liver alcohol dehydrogenase oxidises butan-1-ol, using the most active biomimetic coenzyme (Nap 1), with a k _cat value an order of magnitude lower and a K _m for the coenzyme two orders of magnitude higher than those using native NAD⁺. The enzymatically reduced biomimetic coenzymes may be reoxidised by phenazine methosulfate. We believe that these coenzymes may find applications in biotransformations and biosensors, and in the development of biomimetic catalysts where the redox enzyme itself is replaced by a synthetic binding site.

Extremophiles as a source of novel enzymes for industrial application by F. Niehaus; C. Bertoldo; M. Kähler; G. Antranikian (pp. 711-729).

Extremophilic microorganisms are adapted to survive in ecological niches such as at high temperatures, extremes of pH, high salt concentrations and high pressure. These microorganisms produce unique biocatalysts that function under extreme conditions comparable to those prevailing in various industrial processes. Some of the enzymes from extremophiles have already been purified and their genes successfully cloned in mesophilic hosts. In this review we will briefly discuss the biotechnological significance of extreme thermophilic (optimal growth 70–80 °C) and hyperthermophilic (optimal growth 85–100 °C) archaea and bacteria. In particular, we will focus on selected extracellular-polymer-degrading enzymes, such as amylases, pullulanases, cyclodextrin glycosyltransferases, cellulases, xylanases, chitinases, proteinases and other enzymes such as esterases, glucose isomerases, alcohol dehydrogenases and DNA-modifying enzymes with potential use in food, chemical and pharmaceutical industries and in environmental biotechnology.

Microbial heavy-metal resistance by D. H. Nies (pp. 730-750).

We are just beginning to understand the metabolism of heavy metals and to use their metabolic functions in biotechnology, although heavy metals comprise the major part of the elements in the periodic table. Because they can form complex compounds, some heavy metal ions are essential trace elements, but, essential or not, most heavy metals are toxic at higher concentrations. This review describes the workings of known metal-resistance systems in microorganisms. After an account of the basic principles of homoeostasis for all heavy-metal ions, the transport of the 17 most important (heavy metal) elements is compared.

Biodegradation of EDTA by B. Nörtemann (pp. 751-759).

The chelating agent ethylenediaminetetraacetate (EDTA) is not degraded by conventional biological and physicochemical methods for the treatment of wastewater and the purification of drinking water. Of the measurable organic compounds it is the one present at the highest concentration in many surface and drinking waters. In recent years, however, studies have demonstrated that EDTA can be degraded by specially enriched bacterial cultures and in wastewater treatment plants receiving EDTA-containing effluents. The amounts of EDTA released into the aquatic environment could thus be reduced by establishing appropriate biological wastewater treatment plants. This article describes the degradation of EDTA and its metal chelates by different bacterial cultures, catabolic steps in EDTA degradation, and biological methods for the removal of this chelating agent from wastewaters.

High-density Escherichia coli cultures for continuous l(−)-carnitine production by J. M. Obón; J. R. Maiquez; M. Cánovas; H.-P. Kleber; J. L. Iborra (pp. 760-764).

The use of a biological procedure for l-carnitine production as an alternative to chemical methods must be accompanied by an efficient and highly productive reaction system. Continuous l-carnitine production from crotonobetaine was studied in a cell-recycle reactor with Escherichia coli O44 K74 as biocatalyst. This bioreactor, running under the optimum medium composition (25 mM fumarate, 5 g/l peptone), was able to reach a high cell density (26 g dry weight/l) and therefore to obtain high productivity values (6.2 g l-carnitine l⁻¹ h⁻¹). This process showed its feasibility for industrial l-carnitine production. In addition, resting cells maintained in continuous operation, with crotonobetaine as the only medium component, kept their biocatalytic capacity for 4 days, but the biotransformation capacity decreased progressively when this particular method of cultivation was used.

Quantification of bacterial polyhydroxyalkanoic acids by Nile red staining by V. Gorenflo; A. Steinbüchel; S. Marose; M. Rieseberg; T. Scheper (pp. 765-772).

The fluorescence properties of one chemically and seven biologically produced polyhydroxyalkanoic acids were investigated as film castings and in living cells respectively after staining with Nile red. All these polyesters show a similar fluorescence behaviour, revealing a clear fluorescence maximum at an excitation wavelength between 540 nm and 560 nm and an emission wavelength between 570 nm and 605 nm. This could be shown by the use of two-dimensional fluorescence spectroscopy and flow cytometry. The examination of native poly(3-hydroxybutyric acid), poly(3HB), granules isolated from cells of Ralstonia eutropha H16 showed that the addition of 6.0 μg Nile red is necessary for total staining of 1.0 mg granules. The fluorescence intensity at an excitation wavelength of 550 nm and an emission wavelength of 600 nm showed high correlation to the poly(3HB) concentration of grana suspensions at different grana concentrations. These results and the staining of cell suspensions during cultivation experiments revealed that Nile red has a high potential for the quantitative determination of hydrophobic bacterial polyhydroxyalkanoic acids.

Improvement of mechanical and biological properties of freeze-dried denitrifying alginate beads by using starch as a filler and carbon source by Y. Tal; J. van Rijn; A. Nussinovitch (pp. 773-779).

Freeze-dried, alginate-based beads, used for the immobilization of a denitrifying bacterium (Pseudomonas sp.), were filled with different concentrations (10%, 20%, 30% and 40%, w/w) of granular starch. The beads were incubated under denitrifying conditions in laboratory-scale, flow-through columns and monitored for changes in their physical and denitrifying properties. Freeze-dried beads containing high concentrations of starch were found to have better mechanical and denitrifying properties than beads containing low concentrations of this filler. Nitrate removal by the beads was found to be correlated with their starch content. Nitrite accumulation, as a result of incomplete denitrification, increased with the decrease in starch content of the beads. Nitrite in the outlet of the columns was measured in all types of beads during the initial phase of incubation but was undetectable, with the exception of beads with the lowest starch content, at later stages of incubation.

Oxygen starvation induces cell death in Candida shehatae fermentations of d-xylose, but not d-glucose by J. R. Kastner; W. J. Jones; R. S. Roberts (pp. 780-785).

Candida shehatae cells, cultivated on d-glucose and d-xylose, were subjected to a shift from fully aerobic to anaerobic fermentative conditions. After anaerobic conditions were imposed, growth was limited to approximately one doubling or less as C. shehatae rapidly entered a stationary phase of growth. Following the shift to anoxia, cell viability rapidly declined and the total cell volume declined in the d-xylose fermentations. Moreover, the cell volume distribution shifted to smaller volumes. Cell viability, measured by plate counts, declined nine times faster for d-xylose fermentations than for d-glucose fermentations. Anaerobic growth did not occur on either d-glucose or d-xylose. Selected vitamins and amino acids did not stimulate anaerobic growth in C. shehatae, but did enhance anaerobic growth on d-glucose in S. cerevisiae. The decline in cell viability and lack of anaerobic growth by C. shehatae were attributed to oxygen deficiency and not to ethanol inhibition. The results shed light on why C. shehatae anaerobic fermentations are not currently practical and suggest that research directed towards a biochemical understanding of why C. shehatae can not grow anaerobically will yield significant improvements in ethanol fermentations from d-xylose.

Isolation and characterization of indene bioconversion genes from Rhodococcus strain I24 by S. L. Treadway; K. S. Yanagimachi; E. Lankenau; P. A. Lessard; G. Stephanopoulos; A. J. Sinskey (pp. 786-793).

Rhodococcus strain I24 is able to convert indene into indandiol via the actions of at least two dioxygenase systems and a putative monooxygenase system. We have identified a cosmid clone from I24 genomic DNA that is able to confer the ability to convert indene to indandiol upon Rhodococcus erythropolis SQ1, a strain that normally can not convert or metabolize indene. HPLC analysis reveals that the transformed SQ1 strain produces cis-(1R,2S)-indandiol, suggesting that the cosmid clone encodes a naphthalene-type dioxygenase. DNA sequence analysis of a portion of this clone confirmed the presence of genes for the dioxygenase as well as genes encoding a dehydrogenase and putative aldolase. These genes will be useful for manipulating indene bioconversion in Rhodococcus strain I24.

Genetically engineered Rhodobacter sphaeroides for the overproduction of δ-aminolevulinic acid by A. Suwanto (pp. 794-799).

Genes for β and α polypeptides of the light-harvesting II complexes in Rhodobacter sphaeroides 2.4.1 are encoded by the pucBA operon, and their expression is highly regulated by oxygen level and light intensity. δ-Aminolevulinic acid (ALA) in this bacterium is synthesized by ALA synthase isozymes encoded by hemA and hemT. Recombinant plasmids carrying either a pucB′-hemA transcriptional fusion (pAS608A) or a pucB′-hemT translational fusion (pAS607A) have been constructed. Derivatives of Escherichia coli SASP19 (hemA ⁻ mutant), harboring either pAS608A or pAS607A, still required exogenous ALA supplementation. However, each of these functions could be expressed in R. sphaeroides AT1 (hemA − and hemT − mutant of R. sphaeroides 2.4.1) such that AT1 could grow in the medium without exogenous ALA supplementation. Introduction of pAS608A into R. sphaeroides 2.4.1 resulted in the increase of ALA synthase activity under both aerobic and photosynthetic growth conditions, while the introduction of pAS607A resulted in the increase of ALA synthase only under aerobic conditions. The production of extracellular and intracellular ALA in R. sphaeroides 2.4.1 (pAS608A) or R. sphaeroides 2.4.1 (pAS607A) was not significantly different from that of the wild-type strain in either aerobic or photosynthetic growth conditions.

A dominant selection system designed for copy-number-controlled gene integration in Hansenula polymorpha DL-1 by J.-H. Sohn; E.-S. Choi; H. A. Kang; J.-S. Rhee; M. O. Agaphonov; M. D. Ter-Avanesyan; S.-K. Rhee (pp. 800-807).

To facilitate the selection of multiple gene integrants in Hansenula polymorpha, a rapid and copy-number-controlled selection system was developed using a vector containing a telomeric autonomous replication sequence and the bacterial aminoglycoside 3-phosphotransferase (APH) gene. Direct use of the unmodified APH gene as a dominant selectable marker resulted in the extremely slow growth of transformants and the frequent selection of spontaneous resistance. For the proper performance of the APHgene, a set of deleted glyceraldehyde-3-phosphate dehydrogenase (GAPDH) promoters of H. polymorpha were fused to the APH gene. The fusion construct with the 578-bp GAPDH promoter conferred G418 resistance sufficient to allow rapid growth of transformants, and thus facilitated the selection of transformants with up to 15 tandem copies of the vector. To increase further the integration copy number within the gene-dose-dependent range, the GAPDHpromoter was serially deleted down to the −61 nucleotide. With this weak expression cassette, the integration copy number could easily be controlled between 1 and 50. Tandemly integrated copies of plasmids near the end of the chromosome were mitotically stable over l50 generations. The dosage-dependent selection system of this study would provide a powerful tool for the development of H. polymorpha as an industrial strain to produce recombinant proteins.

Isolation and characterization of experimentally induced, aflatoxin biosynthetic pathway deletion mutants of Aspergillus parasiticus by J. W. Cary; N. Barnaby; K. C. Ehrlich; D. Bhatnagar (pp. 808-812).

A plasmid vector (pDEL2) was engineered for the purpose of introducing a deletion within the aflatoxin (AF) biosynthetic gene cluster of Aspergillus parasiticus. The vector was constructed by PCR amplification of a region of the AF gene cluster from an A. parasiticus isolate that had undergone an aberrant recombinational event during transformation with a norA-niaD gene disruption vector. This recombinational event resulted in the deletion of an approximately 6-kb region of the AF gene cluster and accumulation of the AF precursor averantin (AVN). Northern hybridization analysis confirmed that the deletion event resulted in no detectable transcription of the norA gene or the AF biosynthetic genes, avnA, verA, and ver-1. Transformation of A. parasiticus RHN1 with pDEL2 resulted in 16% of the transformants accumulating AVN. Southern hybridization analysis of randomly selected AVN-accumulating transformants indicated that all had undergone a double-crossover homologous, recombinational event resulting in the 6-kb norA to avnA deletion within the AF gene cluster. Aflatoxin precursor feeding studies performed on one of the AVN-accumulating, RHN1(pDEL2) transformants confirmed that the enzyme activities associated with the deleted genes were no longer present.

The ferrous iron oxidation kinetics of Thiobacillus ferrooxidans in batch cultures by M. Boon; C. Ras; J. J. Heijnen (pp. 813-819).

The ferrous iron oxidation kinetics of Thiobacillus ferrooxidans in batch cultures was examined, using on-line off-gas analyses to measure the oxygen and carbon dioxide consumption rates continuously. A cell suspension from continuous cultures at steady state was used as the inoculum. It was observed that a dynamic phase occurred in the initial phase of the experiment. In this phase the bacterial ferrous iron oxidation and growth were uncoupled. After about 16 h the bacteria were adapted and achieved a pseudo-steady state, in which the specific growth rate and oxygen consumption rate were coupled and their relationship was described by the Pirt equation. In pseudo-steady state, the growth and oxidation kinetics were accurately described by the rate equation for competitive product inhibition. Bacterial substrate consumption is regarded as the primary process, which is described by the equation for competitive product inhibition. Subsequently the kinetic equation for the specific growth rate, μ, is derived by applying the Pirt equation for bacterial substrate consumption and growth. The maximum specific growth rate, μ _max, measured in the batch culture agrees with the dilution rate at which washout occurs in continuous cultures. The maximum oxygen consumption rate, q _O2,max, of the cell suspension in the batch culture was determined by respiration measurements in a biological oxygen monitor at excess ferrous iron, and showed changes of up to 20% during the course of the experiment. The kinetic constants determined in the batch culture slightly differ from those in continuous cultures, such that, at equal ferric to ferrous iron concentration ratios, biomass-specific rates are up to 1.3 times higher in continuous cultures.

The ferrous iron oxidation kinetics of Thiobacillus ferrooxidans in continuous cultures by M. Boon; T. A. Meeder; C. Thöne; C. Ras; J. J. Heijnen (pp. 820-826).

The oxidation and growth kinetics of ferrous iron with Thiobacillus ferrooxidans in continuous cultures was examined at several total iron concentrations. On-line off-gas analyses of O₂ and CO₂ were used to measure the oxygen and carbon dioxide consumption rates in the culture. Off-line respiration measurements in a biological oxygen monitor (BOM) were used to measure directly the maximum specific oxygen consumption rate, qO₂,max, of cells grown in continuous culture. It was shown that these reproducibly measured values of qO₂,max vary with the dilution rate. The biomass-specific oxygen consumption rate, qO₂, is dependent on the ratio of the ferric and ferrous iron concentrations in the culture. The oxidation kinetics was accurately described with a rate equation for competitive ferric iron inhibition, using the value of qO₂,max measured in the BOM. Accordingly, only the kinetic constant Ks/K _i needed to be fitted from the measurements. A new method was introduced to determine the steady-state kinetics of a cell suspension in a batch culture that only takes a few hours. The batch culture was set up by terminating the feeding of a continuous culture at its steady state. The kinetic constant K _s/K _i determined in this batch culture agreed with the value determined in continuous cultures at various steady states.

Biochemical basis for carbon monoxide tolerance and butanol production by Butyribacterium methylotrophicum by G.-J. Shen; J.-S. Shieh; A. J. Grethlein; M. K. Jain; J. G. Zeikus (pp. 827-832).

The biochemical mechanisms for growth tolerance to a 100% CO headspace in cultures, and butanol plus ethanol production from CO by Butyribacterium methylotrophicum were assessed in the wild-type and CO-adapted strains. The CO-adapted strain grew on glucose or CO under a 100% CO headspace, whereas, the growth of the wild-type strain was severely inhibited by 100% CO. The CO-adapted strain, unlike the wild-type, also produced butyrate, from either pyruvate or CO. The CO-adapted strain was a metabolic mutant having higher levels of ferredoxin–NAD oxidoreductase activity, which was not inhibited by NADH. Consequently, only the CO-adapted strain can grow on CO because CO oxidation generates reduced ferredoxin which, via the mutated ferredoxin–NAD reductase activity, forms reduced NADH required for catabolism. When the CO-adapted strain was grown at pH 6.0 it produced butanol (0.33 g/l) and ethanol (0.5 g/l) from CO and the cells contained the following NAD-linked enzyme activities (μmol min⁻¹ mg protein⁻¹): butyraldehyde dehydrogenase (227), butanol dehydrogenase (686), acetaldehyde dehydrogenase (82) and ethanol dehydrogenase (129).

Mechanism for phenol tolerance in phenol-degrading Comamonas testosteroni strain by L. F. Yap; Y. K. Lee; C. L. Poh (pp. 833-840).

Comamonas testosteroni P15 and its mutant strain E23 can tolerate and utilize phenol as the sole source of carbon and energy at up to 15 mM and 20 mM, respectively. Compared to the wild type P15, mutant E23 showed higher values of K _s and K _i but a lower μ_max value, and had lower phenol hydroxylase and catechol 2,3-dioxygenase activities. Without phenol exposure, mutant E23 demonstrated a two-fold greater amount of cardiolipin than the wild type P15. Upon exposure to phenol, an increase in cardiolipin at the expense of phosphatidylethanolamine was observed in the wild type P15. However, there was no significant difference in major phospholipid contents between mutant E23 cells grown in the presence or absence of phenol. It was noted that the ratio of trans/cis fatty acids of phosphatidylethanolamine and cardiolipin in mutant E23 was 65–70% higher than that in the wild type P15. In the absence of phenol, the degree of saturation of cardiolipin in mutant E23 was 33% higher than that in wild type P15. In contrast to earlier findings, an increase in C16:1 9trans with a simultaneous decrease in C18:1 11cis instead of C16:1 9cis was observed in specific classes of phospholipids.

Phenol inhibition kinetics for growth of Acetobacter aceti on ethanol by G. A. Hill; A. J. Daugulis (pp. 841-846).

Acetobacter aceti have been grown on ethanol under inhibitory conditions created by high concentrations of phenol. A defined medium with no vitamin or amino acid supplements has been used such that ethanol was the sole carbon substrate. The culture temperature was maintained at 30 °C while the pH was manually controlled to fall within the range 4.5–6.0 during ethanol consumption. Growth on ethanol at a few thousand milligrams per litre (below the known inhibitory level) resulted in a maximum specific growth rate of 0.16 h⁻¹ with a 95% yield of acetic acid, followed immediately by acetic acid consumption at a growth rate of 0.037 h⁻¹. Phenol was found to inhibit growth by decreasing both the specific growth rate and the biomass yield during ethanol consumption. On the other hand, the yield of acetic acid during ethanol consumption and the yield of biomass during acetic acid consumption remained constant, independent of phenol inhibition. A model is presented and is shown to represent the phenol-inhibited growth behaviour of A. aceti during both ethanol and acetic acid consumption.

Synthesis of optically active ethyl 4-chloro-3-hydroxybutanoate by microbial reduction by Y. Yasohara; N. Kizaki; J. Hasegawa; S. Takahashi; M. Wada; M. Kataoka; S. Shimizu (pp. 847-851).

A total of 400 yeast strains were examined for the ability to reduce ethyl 4-chloroacetoacetate (COBE) to ethyl 4-chloro-3-hydroxybutyrate (CHBE) by using acetone-dried cells in the presence of a coenzyme-recycling system in water/n-butyl acetate. We discovered some yeast strains that reduced COBE to (S)-CHBE. Heating of acetone-dried cells of the selected yeast strains increased the optical purity of the product. There may be several enzymes that can reduce COBE stereoselectively in the same yeast cells. The cultured broth of Candida magnoliae accumulated 90 g/l (S)-CHBE (96.6% enantiomeric excess, e.e.) in the presence of glucose, NADP and glucose dehydrogenase in n-butyl acetate. When these cells were heated, the stereoselectivity of the reduction increased to 99% e.e. (S)-CHBE is one of the useful chiral building blocks applicable to the synthesis of some pharmaceuticals. We expect that the cheap and industrial production of this important chiral compound will follow the discovery of this yeast strain.

Duplicated Clostridium thermocellum cellobiohydrolase gene encoding cellulosomal subunits S3 and S5 by V. V. Zverlov; G. A. Velikodvorskaya; W. H. Schwarz; J. Kellermann; W. L. Staudenbauer (pp. 852-859).

The upstream region of the cellobiohydrolase gene cbhA of Clostridium thermocellum F7 was sequenced. It was found that this region contains the previously sequenced gene celK encoding an enzyme closely related to CbhA (cellulosomal subunit S3). The presence of a putative transcription terminator in the 524-bp intergenic region indicates that celK and cbhA are not cotranscribed as an operon. Sequence comparison between the two cellobiohydrolases revealed high sequence conservation in the catalytic domain and in the N-terminal cellulose-binding domain (CBD) homologous to CBD family IV, which binds specifically to amorphous cellulose and soluble cellooligosaccharides. In contrast to CbhA, CelK lacks a family III CBD capable of binding to crystalline cellulose. By partial amino acid sequence determination CelK was shown to be identical to cellulosomal subunit S5. CelK and CbhA were found to be members of subfamily E1 of cellulase family E (glycosylhydrolase family 9). Sequence comparison of catalytic domains of family E1 cellulases with C. thermocellum CelD, a family E1 endoglucanase of known three-dimensional structure, revealed a significant variation in the lengths of substrate-binding loops connecting the helices of the (α/α)₆ barrel fold. The extended loops of CelK and CbhA might form an active-site tunnel, as found in the catalytic domains of fungal cellobiohydrolases.

Subcellular location of enzymes involved in oxidation of n-alkane by Cladosporium resinae by P. Goswami; J. J. Cooney (pp. 860-864).

More than 70% of n-hexadecane-grown cells of Cladosporium resinae ATCC 22711 were converted to spheroplasts when they were treated with chitinase and lytic enzyme from Trichoderma harziamum. The light mitochondrial fraction, containing microbodies, mitochondria and vacuoles, was isolated from spheroplasts. Vacuoles in cells were demonstrated by the inability of acridine orange to stain organelles previously treated with 2.5 μM Bafilomycin A₁, a vacuolar ATPase inhibitor. Microbodies, mitochondria and vacuoles were separated from the light mitochondrial fraction by self-generated density-gradient ultracentrifugation using iodixanol as gradient medium. NADH-dependent n-alkane monooxygenase activity and fatty alcohol oxidase activity were located in the cytoplasm and mitochondrial fractions respectively.

Biodegradation of azo dyes in cocultures of anaerobic granular sludge with aerobic aromatic amine degrading enrichment cultures by N. C. G. Tan; F. X. Prenafeta-Boldú; J. L. Opsteeg; G. Lettinga; J. A. Field (pp. 865-871).

A prerequisite for the mineralization (complete biodegradation) of many azo dyes is a combination of reductive and oxidative steps. In this study, the biodegradation of two azo dyes, 4-phenylazophenol (4-PAP) and Mordant Yellow 10 (4-sulfophenylazo-salicylic acid; MY10), was evaluated in batch experiments where anaerobic and aerobic conditions were integrated by exposing anaerobic granular sludge to oxygen. Under these conditions, the azo dyes were reduced, resulting in a temporal accumulation of aromatic amines. 4-Aminophenol (4-AP) and aniline were detected from the reduction of 4-PAP. 5-Aminosalicylic acid (5-ASA) and sulfanilic acid (SA) were detected from the reduction of MY10. Subsequently, aniline was degraded further in the presence of oxygen by the facultative aerobic bacteria present in the anaerobic granular sludge. 5-ASA and SA were also degraded, if inocula from aerobic enrichment cultures were added to the batch experiments. Due to rapid autoxidation of 4-AP, no enrichment culture could be established for this compound. The results of this study indicate that aerobic enrichment cultures developed on aromatic amines combined with oxygen-tolerant anaerobic granular sludge can potentially be used to completely biodegrade azo dyes under integrated anaerobic/aerobic conditions.

Degradation of phosphonates by streptomycete isolates by A. Obojska; B. Lejczak; M. Kubrak (pp. 872-876).

Wild-type Streptomyces sp. strains, able to utilise both naturally occurring and synthetic organophosphonates, were isolated. High levels of inorganic phosphate were necessary for their growth in complete medium as well as in medium, supplemented with phosphonates as the sole carbon or nitrogen source. Isolate StA expressed detectable enzymatic activity against 2-aminoethylphosphonate in vivo. Streptomycete StC had a surprising ability to degrade N-phosphonomethylglycine (glyphosate) in a phosphate-independent manner via C–P bond cleavage accompanied by sarcosine formation.

Bioremediation of atrazine-contaminated soil by repeated applications of atrazine-degrading bacteria by D. A. Newcombe; D. E. Crowley (pp. 877-882).

Bioaugmentation has previously been unreliable for the in situ clean-up of contaminated soils because of problems with poor survival and the rapid decline in activity of the bacterial inoculum. In an attempt to solve these problems, a 500-l batch fermenter was investigated for its ability to deliver inoculum repeatedly to contaminated soils via irrigation lines. In a field experiment, mesocosms were filled with 350 kg soil containing 100 mg kg⁻¹ atrazine, and inoculated one, four or eight times with an atrazine-degrading bacterial consortium that was produced in the fermenter. After 12 weeks, no significant degradation of atrazine had occurred in soil that was inoculated only once; whereas, mesocosms inoculated four and eight times mineralized 38% and 72% of the atrazine respectively. Similar results were obtained in a laboratory experiment using soil contaminated with 100 mg kg⁻¹ [¹⁴C]atrazine. After 35 days, soil that was inoculated once with 10⁸ cfu ml⁻¹ of the consortium or with the atrazine-degrading bacterium, Pseudomonas sp. strain ADP, mineralized 17% and 35% of the atrazine respectively. In comparison, microcosms inoculated every 3 days with the consortium or with Pseudomonas sp. (ADP) mineralized 64% or 90% of the atrazine over this same period. Results of these experiments suggest that repeated inoculation from an automated fermenter may provide a strategy for bioaugmentation of contaminated soil with xenobiotic-degrading bacteria.

Towards a reduction in excess sludge production in activated sludge processes: biomass physicochemical treatment and biodegradation by M. Rocher; G. Goma; A. Pilas Begue; L. Louvel; J. L. Rols (pp. 883-890).

To decrease activated sludge production, microbial cell lysis can be amplified to enhance cryptic growth (biomass growth on lysates). Cell breakage techniques (thermal, alkaline, acid) were studied to generate Alcaligenes eutrophus and sludge lysates and to evaluate their biodegradability. Gentle treatment conditions produced the best results. Complete cell deactivation was obtained for temperatures higher than 55 °C. The release kinetics were similar for temperatures varying from 60 °C to 100 °C. A 20-min incubation was suitable for reaching 80% of the maximum releasable carbon. In thermal-chemical hydrolysis, NaOH was the most efficient for inducing cell lysis. Carbon release was a two-step process. First an immediate release occurred, which was of the same order of magnitude for A. eutrophus and sludge [100–200 mg dissolved organic C (DOC) g total suspended solids (TSS)⁻¹], followed by a post-treatment release. The second step was virtually equivalent to the first for sludge, and weaker for A. eutrophus (<50 mg DOC g TSS⁻¹). The biodegradability of the soluble fraction, both the immediate and the post-treatment carbon release, was investigated. The optimal degradation yield, obtained with sludge cells, reached 55% after 48 h of incubation and 80% after 350 h. The most consistent lysis and biodegradation results occurred at pH 10 and 60 °C after a 20-min incubation.

Solid matrix characterization of immobilized Pseudomonas putida MTCC 1194 used for phenol degradation by K. Bandhyopadhyay; D. Das; B. R. Maiti (pp. 891-895).

Characterization studies of calcium alginate beads with encapsulated Pseudomonas putida MTCC 1194, used for the biodegradation of phenol, were carried out to investigate the reactivity, reusability and structural strength of the solid matrix. Various techniques were employed to improve the structural stability of the immobilized solid necessary for its use in commercial reactors like packed bed flow reactor, fluidized bed and CSTR systems. Experiments were performed to establish the optimum conditions for durability, strength and steady biochemical reactivity. During a batch run of 40 h a gradual decline in the rate of phenol degradation was observed with the immobilized system. The calcium alginate beads with high structural strength yielded decreased activity. Treatment with a hardening agent like glutaraldehyde for different concentrations and treatment times led to variations in structural stability, reusability and the extent of phenol degradation. Scanning electron microscope studies of the immobilized solid indicated the internal distribution pattern of the cells encapsulated in a calcium alginate bead.

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Applied Microbiology and Biotechnology (v.51, #6)

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Applied Microbiology and Biotechnology (v.51, #6)