| Check out our New Publishers' Select for Free Articles |
Applied Microbiology and Biotechnology (v.54, #3)
Yeast secretory expression of insulin precursors by T. Kjeldsen (pp. 277-286).
Since the 1980s, recombinant human insulin for the treatment of diabetes mellitus has been produced using either the yeast Saccharomyces cerevisiae or the prokaryote Escherichia coli. Here, development of the insulin secretory expression system in S. cerevisiae and its subsequent optimisation is described. Expression of proinsulin in S. cerevisiae does not result in efficient secretion of proinsulin or insulin. However, expression of a cDNA encoding a proinsulin-like molecule with deletion of threonineB30 as a fusion protein with the S. cerevisiaeα-factor prepro-peptide (leader), followed either by replacement of the human proinsulin C-peptide with a small C-peptide (e.g. AAK), or by direct fusion of lysineB29 to glycineA1, results in the efficient secretion of folded single-chain proinsulin-like molecules to the culture supernatant. The secreted single-chain insulin precursor can then be purified and subsequently converted to human insulin by tryptic transpeptidation in organic–aqueous medium in the presence of a threonine ester. The leader confers secretory competence to the insulin precursor, and constructed (synthetic) leaders have been developed for efficient secretory expression of the insulin precursor in the yeasts S. cerevisiae and Pichia pastories. The Kex2 endoprotease, specific for dibasic sites, cleaves the leader-insulin precursor fusion protein in the late secretory pathway and the folded insulin precursor is secreted to the culture supernatant. However, the Kex2 endoprotease processing of the pro-peptide-insulin precursor fusion protein is incomplete and a significant part of the pro-peptide-insulin precursor fusion protein is secreted to the culture supernatant in a hyperglycosylated form. A spacer peptide localised between the leader and the insulin precursor has been developed to optimise Kex2 endoprotease processing and insulin precursor fermentation yield.
Improvement of microbial strains and fermentation processes by S. Parekh; V. A. Vinci; R. J. Strobel (pp. 287-301).
Improvement of microbial strains for the over-production of industrial products has been the hallmark of all commercial fermentation processes. Conventionally, strain improvement has been achieved through mutation, selection, or genetic recombination. Over-production of primary or secondary metabolites is a complex process, and successful development of improved strains requires a knowledge of physiology, pathway regulation and control, and the design of creative screening procedures. In addition, it requires mastery of the fermentation process for each new strain, as well as sound engineering know-how for media-optimization and the fine-tuning of process conditions. This review focuses on the various options that may be employed to improve microbial strains and addresses the complex problems of screening, the tools and technology behind the selection of targeted organisms, and the importance of process optimization. Furthermore, this review discusses new and emerging technologies and designing optimized media for tracking mutants with enhanced productivity or other desired attributes.
Enslaved bacteria as new hope for plant biotechnologists by M. Hager; R. Bock (pp. 302-310).
The most distinguishing feature of the plant cell is a DNA-containing organelle that sets plants apart from all other organisms: the chloroplast. Compelling evidence supports an endosymbiotic origin for chloroplasts. According to this theory, chloroplasts are descendants of formerly free-living cyanobacterial ancestors which entered an endosymbiotic relationship with a pre-eukaryotic cell and were ultimately integrated into the metabolism of the host cell. Chloroplasts retain many prokaryotic features and their gene expression system still closely resembles that of their eubacterial ancestors. During the past decade, our knowledge about chloroplast biology has benefited immensely from a most remarkable methodological breakthrough: the development of transformation technologies for chloroplast genomes. Moreover, recent advances in the manipulation of higher plant chloroplast genomes have created unprecedented opportunities for the genetic engineering of plants and promise to overcome many of the problems associated with conventional transgenic technologies. This review describes the state of the art in genetic engineering of higher plant chloroplast genomes and highlights the tremendous potential of these technologies for the biotechnology of the future.
Intestinal receptors for adhesive fimbriae of enterotoxigenic Escherichia coli (ETEC) K88 in swine – a review by L. Z. Jin; X. Zhao (pp. 311-318).
Determining the structure of the intestinal receptor for enterotoxigenic Escherichia coli (ETEC) K88 fimbriae will make it possible to develop new strategies to prevent K88+ ETEC-induced disease in pigs. Putative K88 adhesin receptors have been identified in both intestinal brush border and mucus preparations as either glycoproteins or glycolipids. Proteins with sizes of 25, 35, 40–42, 60, and 80 kDa in the intestinal mucus and 16, 23, 35, 40–70, 74, 210, and 240 kDa in brush border membranes were reported to bind specifically to K88ab and K88ac fimbriae. The factors accounting for these variable results may include the variants of K88, ages, breeds, and phenotypes of pigs, and even the sampling sites in the small intestine. Of the reported K88 receptors, only three brush border receptors, i.e., a pair of mucin-type sialoglycoproteins (210 kDa or 240 kDa), an intestinal neutral glycosphingolipid (IGLad), and a 74-kDa transferrin glycoprotein (GP74), have fulfilled the criteria as phenotype-specific K88 fimbrial receptors. Inhibiting the attachment of ETEC to intestine by modifying the receptor attachment sites has been the key for developing novel approaches to preventing ETEC-induced diarrhea in pigs. These include: (1) receptor analogs from a variety of biological sources, (2) an enteric protected protease, (3) chicken egg-yolk containing anti-K88 fimbrial antibodies, and (4) some Lactobacillus isolates producing proteinaceous components or carbohydrates interacting with mucus components. Future studies should be directed to further characterize the carbohydrate and protein moieties of receptors recognized by the K88 adhesin variants and to identify the genes responsible for susceptibility to K88+ infections.
Polymer production by two newly isolated extremely halophilic archaea: application of a novel corrosion-resistant bioreactor by F. F. Hezayen; B. H. A. Rehm; R. Eberhardt; A. Steinbüchel (pp. 319-325).
A novel corrosion-resistant bioreactor composed of polyetherether ketone (PEEK), tech glass and silicium nitrite ceramics was constructed and applied for the cultivation of two newly isolated, extremely halophilic archaea producing poly(γ-glutamic acid) (PGA), or poly(β-hydroxy butyric acid) (PHB), respectively. These bacteria were isolated from hypersaline soil close to Aswan (Egypt). The isolate strain 40, which is related to the genus Natrialba, produced large amounts of PGA when cultivated on solid medium. Culture conditions were optimised applying the corrosion-resistant bioreactor. PGA production was dependent on NaCl concentration and occurred about at 20% (w/v) NaCl in the medium. A maximum cell density of about 1.6 g cell dry matter/l was obtained when the bioreactor was stirred and aerated in a batch fermentation process using proteose-peptone medium. The supernatant was monitored with respect to PGA formation, and after 90 h a maximum of 470 mg/l culture volume was detected by HPLC analysis. Culture conditions were optimized for the isolate 56, which accumulated PHB as intracellular granules. Batch fermentations in the stirred and aerated bioreactor applying acetate and n-butyric acid as carbon sources led to cell density of 2.28 g cell dry matter/l and a maximum PHB accumulation contributing to about 53% of cellular dry weight. About 4.6 g PHB were isolated from 10.6 g dried cells of strain 56, which exhibited a weight average molar mass of 2.3 × 105 g mol−1 and a polydispersity of about 1.4.
Growth of Photorhabdus luminescens in batch and glucose fed-batch culture by T. Jeffke; D. Jende; C. Mätje; R.-U. Ehlers; L. Berthe-Corti (pp. 326-330).
Photorhabdus luminescens, a bacterial symbiont of entomopathogenic biocontrol nematodes, was grown in batch and glucose fed-batch culture. The cell density, bioluminescence, production of antibiotic substances, number of cells with inclusion bodies, glucose concentration and oxygen uptake rate were recorded. The addition of 12.4 g l−1 glucose prolonged the growth, and the yield almost doubled, from 6.85 g l−1 to 12.45 g l−1 dry mass. The production of antibiotic substances increased by 140%. Bioluminescence was higher in the batch culture. A shift of P. luminescens to phase II variants was not detected.
3-Carbamoyl-α-picolinic acid production by imidase-catalyzed regioselective hydrolysis of 2,3-pyridinedicarboximide in a water-organic solvent, two-phase system by J. Ogawa; C.-L. Soong; M. Ito; T. Segawa; T. Prana; M. S. Prana; S. Shimizu (pp. 331-334).
3-Carbamoyl-α-picolinic acid, a versatile building block for the synthesis of agrochemicals and pharmaceuticals, was prepared by imidase-catalyzed regiospecific hydrolysis of 2,3-pyridinedicarboximide with intact Arthrobacter ureafaciens O-86 cells. Reactions were carried out in a water-organic solvent, two-phase system containing cyclohexanone at low pH to avoid spontaneous random hydrolysis. Under the optimized conditions, with the periodic addition of 2,3-pyridinedicarboximide (in total, 40 mM), the 3-carbamoyl-α-picolinic acid yield reached 36.6 mM in the water phase, with a molar conversion yield of 91.5% and a regioisomeric purity of 94.5%, in 2 h at pH 5.5.
Immobilisation of Thiobacillus ferrooxidans cells on nickel alloy fibre for ferrous sulfate oxidation by J. M. Gómez; D. Cantero; C. Webb (pp. 335-340).
The immobilisation of the iron-oxidising bacteria Thiobacillus ferrooxidans on nickel alloy fibre as support is described. This matrix showed promise for application in iron oxidation under strongly acidic conditions. The influence on the colonisation process of T. ferrooxidans exerted by the initial pH of the medium and by temperature has also been studied. Results showed that immobilisation of T. ferrooxidans cells was affected by changes of temperature between 30 °C and 40 °C and in pH from 1.4 to 2.0.
Saccharide production from methanol by transposon 5 mutants derived from the extracellular polysaccharide-producing bacterium Methylobacillus sp. strain 12S by T. Yoshida; M. Horinouchi; H. Habe; Y. Ayabe; T. Yamaguchi; N. Shibuya; H. Nojiri; H. Yamane; T. Omori (pp. 341-347).
A CH3OH-utilizing bacterium that has the ability to produce extracellular polysaccharide (EPS) was isolated from a soil sample, and was identified as the obligate methylotroph Methylobacillus sp. strain 12S on the basis of its 16S rDNA sequence and growth-substrate specificity. The EPS produced by strain 12S was purified and the sugar composition was analysed by GC-MS and HPLC to reveal that the EPS was a heteropolymer composed of glucosyl, galactosyl, and mannosyl residues in the molar ratio 3:1:1. In order to produce mono- and/or oligosaccharides by single-step fermentation from CH3OH, stain 12S was mutagenized by transposon 5. Among eleven EPS-deficient mutants, three strains were found to accumulate significant amounts of reducing sugars in the media. The amounts of the reducing sugars produced by the mutants (>ca. 700 mg glucose equivalent/l) were >11–22 times higher than those produced by the wild-type strain (
Overproduction of d-hydantoinase and carbamoylase in a soluble form in Escherichia coli by Y.-P. Chao; C.-J. Chiang; T.-E. Lo; H. Fu (pp. 348-353).
The production of d-hydantoinase and carbamoylase from Agrobacterium radiobacter NRRL B11291 using T7 and trc promoters, respectively, was found to cause protein aggregates in Escherichia coli. We initiated a systematic study aimed at overproducting these two proteins in a soluble form. As a result, the protein aggregate from carbamoylase overproduction could be alleviated with the aid of GroEL/GroES. In contrast, the production of a high level of d-hydantoinase in an active form can be achieved at low temperature (25 °C) or by the coproduction of DnaJ/DnaK. Overall, with such approaches both recombinant proteins gain more than a four-fold increase in enzyme activity. In addition, by fusion with thioredoxin, d-hydantoinase activity can be increased 25% more than the unfused counterpart in the presence of DnaJ/DnaK. These results indicate the success of our approaches to overproducing d-hydantoinase and carbamoylase in a soluble form in E. coli.
Molecular cloning and characterization of a chitosanase from the chitosanolytic bacterium Burkholderia gladioli strain CHB101 by M. Shimosaka; Y. Fukumori; X.-Y. Zhang; N.-J. He; R. Kodaira; M. Okazaki (pp. 354-360).
A chitosanase was purified from the culture fluid of the chitino- and chitosanolytic bacterium Burkholderia gladioli strain CHB101. The purified enzyme (chitosanase A) had a molecular mass of 28 kDa, and catalyzed the endo-type cleavage of chitosans having a low degree of acetylation (0–30%). The enzyme hydrolyzed glucosamine oligomers larger than a pentamer, but did not exhibit any activity toward N-acetyl-glucosamine oligomers and colloidal chitin. The gene coding for chitosanase A (csnA) was isolated and its nucleotide sequence determined. B. gladioli csnA has an ORF encoding a polypeptide of 355 amino acid residues. Analysis of the N-terminal amino acid sequence of the purified chitosanase A and comparison with that deduced from the csnA ORF suggests post-translational processing of a putative signal peptide and a possible substrate-binding domain. The deduced amino acid sequence corresponding to the mature protein showed 80% similarity to the sequences reported from Bacillus circulans strain MH-K1 and Bacillus ehimensis strain EAG1, which belong to family 46 glycosyl hydrolases.
Fed-batch production of recombinant human calcitonin precursor fusion protein using Staphylococcus carnosus as an expression-secretion system by S. Dilsen; W. Paul; A. Sandgathe; D. Tippe; R. Freudl; J. Thömmes; M.-R. Kula; R. Takors; C. Wandrey; D. Weuster-Botz (pp. 361-369).
A pH-auxostatic fed-batch process was developed for the secretory production of a fusion protein consisting of the pro-part of Staphylococcus hyicus lipase and two synthetic human calcitonin (hCT) precursor repeats under the control of a xylose-inducible promotor from Staphylococcus xylosus. Using glycerol as the energy source and pH-controlled addition of yeast extract resulted in the production of 2000 mg l−1 of the fusion protein (420 mg l−1 of the recombinant hCT precursor) within 14 h, reaching 45 g l−1 cell dry mass with Staphylococcus carnosus in a stirred-tank reactor. Product titer and space-time yield (30 mg calcitonin precursor l−1 h−1) were thus improved by a factor of 2, and 4.5, respectively, compared to Escherichia coli expression-secretion systems for the production of calcitonin precursors. Two hundred grams of the fusion protein was secreted by the recombinant S. carnosus on a 150-l scale (scale-up factor of 50) with a minimum use of technical-grade yeast extract (40 mg fusion protein g−1 yeast extract).
Regulation of xyn3 gene expression in Trichoderma reesei PC-3–7 by J. Xu; M. Nogawa; H. Okada; Y. Morikawa (pp. 370-375).
The characteristics of regulation of the gene encoding the third xylanase (Xyn III) of a filamentous fungus, Trichoderma reesei PC-3–7, were studied by Northern blot analysis. A partial DNA sequence (185 bp) of the xyn3 gene was obtained by PCR amplification of genomic DNA of T. reesei PC-3–7 and sequenced. This xyn3 gene fragment was used as a probe for Southern and Northern blot analysis. The expression of the xyn3 gene was regulated at the transcriptional level. The xyn3 mRNA was expressed in mycelia of T. reesei PC-3–7 induced by Avicel, l-sorbose and sophorose, but not by xylose, xylooligosaccharides and birchwood xylan. Furthermore, it was observed that xyn3 was synchronously expressed with egl1 but not with xyn1 and xyn2 by l-sorbose, indicating that the xyn3 gene may be coordinately expressed with cellulase genes. By Southern blot analysis, the xyn3 gene was confirmed to exist as a single copy in both strains of T. reesei PC-3–7 and QM9414. However, no xyn3 mRNA appeared in the mycelia induced by any kind of inducers in T. reesei QM9414 even when total RNA was used in large excess, suggesting that the xyn3 gene in T. reesei QM9414 is in the dormant state and cannot be expressed. Therefore, T. reesei PC-3–7 may be a very useful strain for elucidating the induction mechanism of xylanase biosynthesis by cellulosic and xylanosic substrates, and also the regulatory correlation between cellulase and xylanase induction.
Isolation, identification, and accumulation of 2-acetamidophenol in liquid cultures of the wheat take-all biocontrol agent Pseudomonas fluorescens 2-79 by P. J. Slininger; K. D. Burkhead; D. A. Schisler; R. J. Bothast (pp. 376-381).
Pseudomonas fluorescens strain 2-79 (NRRL B-15132) is a classic biological control agent known to produce phenazine-1-carboxylic acid (PCA) as its primary means of suppressing take-all disease of wheat. In addition to PCA, an unknown metabolite was discovered in a liquid culture used to produce the biocontrol agent. The objective of the current study was to isolate, identify, and evaluate the accumulation of this compound in production cultures. Upon centrifugal fractionation of a production culture, thin-layer chromatography (TLC) analyses of extracts of the cells and cell-free supernatant indicated the compound to be primarily in the supernatant. Purified compound was obtained by extraction of culture supernatant, followed by flash chromatography of the extract and preparative TLC. The 1H and 13C nuclear magnetic resonance and electron impact mass spectra indicated the compound to be 2-acetamidophenol (AAP). Measured by reversed-phase HPLC, the accumulations of AAP and PCA in cultures of strain 2-79 reached 0.05 g/l and 1 g/l, respectively. The accumulations of AAP and PCA in liquid cultures were linearly correlated (P < 0.001), as shown by studies of cultures stimulated to yield varying levels of PCA by controlling levels of oxygen transfer, pH, and growth medium composition. In this study, oxygen limitation, a defined amino-acid-free medium, and neutral pH stimulated maximal production of both AAP and PCA. Furthermore, a transposon mutant of 2-79 [2A40 2-79 (phz–)] unable to produce PCA did not accumulate AAP. These findings indicate that AAP and PCA are likely to share a common segment of biosynthetic pathway. This is the first report of AAP production by a strain of P. fluorescens. Possible routes of AAP production are discussed relative to current knowledge of the phenazine biosynthetic pathway of strain 2-79. The pertinence of AAP to the design of commercial seed inoculants of phenazine-producing bacteria for controlling wheat take-all is also considered.
Phospholipid compositional changes of five pseudomonad archetypes grown with and without toluene by J. Fang; M. J. Barcelona; P. J. J. Alvarez (pp. 382-389).
Bacterial physiological responses to toluene exposure were investigated in five reference pseudomonad strains that express different toluene degradation pathways: Pseudomonas putida mt-2, Pseudomonas putida F1, Burkholderia cepacia G4, Burkholderia pickettii PKO1, and Pseudomonas mendocina KR1. The intact phospholipids of these archetypes, grown with and without toluene, were characterized using liquid chromatography/electrospray ionization/mass spectrometry. All strains showed significant changes in phospholipid content and composition as an adaptive response to toluene exposure, as well as considerable diversity in response mechanisms. For example, the phospholipid content of toluene-grown PKO1, F1, and KR1 were 10.9–34.7% of that found in succinate-grown strains, while the phospholipid content of mt-2 and G4 increased by 56% and 94%, respectively, when grown on toluene. In addition, PKO1, F1, and mt-2 responded to the presence of toluene by synthesizing more phosphatidylglycerol, whereas G4 and KR1 synthesized phospholipids with polyunsaturated fatty acids (C18:2) on one or both of the sn-2 positions. These changes in phospholipid composition and concentration probably reflect the sensitivity and degree of tolerance of these strains to toluene, and suggest that different mechanisms are utilized by dissimilar bacteria to maintain optimal lipid ordering in the presence of such environmental pollutants.
Screening for and characterization of phospholipase A1 hypersecretory mutants of Tetrahymena thermophila by M. Hartmann; A. Guberman; M. Florin-Christensen; A. Tiedtke (pp. 390-396).
We have described a procedure for the isolation of mutants of Tetrahymena thermophila with hyperscretion of phospholipase A1 (PLA1). Using random chemical mutagenesis, uniparental cytogamy, genetic crossing and a new, fast and effective screening procedure, four PLA1-hypersecretory mutants were isolated. The screening procedure is based on the formation of a halo appearing around cylindrical holes in a lecithin-containing agar plate filled with cell-free supernatants. About 3,940 clones were tested with this procedure in primary screening for hypersecretory features, of which 60 putative hypersecretory mutants were isolated, subcloned and tested in a secondary screening. Of these, four selected mutants showed 1.8–2.2 more PLA1 activity in the cell-free supernatants compared to the wild-type strain CU 438.1. Hypersecretion was only observable for PLA1; no increased activity for two other lysosomal enzymes could be detected. These hypersecretory mutants of T. thermophila can be very useful for increasing the yield of PLA1 in fermentation processes. This is particularly relevant because, in contrast to other phospholipases, PLA1 is not available on the commercial market for fine chemicals and little is known about the role of PLA1 in cell signaling and metabolism.
Purification, characterization, and primary structure of a chitinase from Pseudomonas sp. YHS-A2 by H.-S. Lee; D.-S. Han; S.-J. Choi; S.-W. Choi; D.-S. Kim; D.-H. Bai; J.-H. Yu (pp. 397-405).
A chitinase gene (chiA) from Pseudomonas sp. YHS-A2 was cloned into Escherichia coli using pUC19. The nucleotide sequence determination revealed a single open reading frame of chiA comprised of 1902 nucleotide base pairs and 633 deduced amino acids with a molecular weight of 67,452 Da. Amino acid sequence alignment showed that ChiA contains two putative chitin-binding domains and a single catalytic domain. Two proline-threonine repeat regions, which are linkers between catalytic and substrate-binding domains in some cellulases and xylanases, were also found. From E. coli, ChiA was purified 12.8-fold relative to the periplasmic fraction. The Michaelis constant and maximum initial velocity for p-nitrophenyl-N,N′-diacetylchitobiose were 1.06 mM and 44.4 μmol/h per mg protein, respectively. The purified ChiA binds not only to colloidal chitin but also to other substrates (avicel, chitosan, and xylan), but the binding affinity of avicel, chitosan, and xylan is around 10 times lower than that of colloidal chitin. The reaction of ChiA with colloidal chitin and chitooligosaccharides (trimer-hexamer) produced an end product of N,N′-diacetylchitobiose, indicating that ChiA is a chitobiosidase.
A cephalosporin C acetylhydrolase is present in the cultures of Nocardia lactamdurans by R. E. Cardoza; J. Velasco; J. F. Martín; P. Liras (pp. 406-412).
Two protein bands with strong esterase activity are present in broths of Nocardia lactamdurans MA4213 cultures. One of them shows cephalosporin C acetylhydrolase (CAH) activity. This activity is maximal at 48 h of growth and shows a pattern of regulation slightly different from that of cephamycin production in medium supplemented with glucose (166 mM), glycerol (326 mM) or ammonium chloride (60 mM). The CAH activity was purified to homogeneity by DEAE-Sepharose ion-exchange, Sephadex G-75 gel filtration, and phenyl-Sepharose hydrophobic interaction chromatography. It showed a molecular mass of 72,100 Da. The N-terminus of the protein was determined and showed the amino acid sequence GGAAPGGPGAHPLWLPAGKD. The enzyme showed K m values of 7.0 mM and 8.3 mM for cephalosporin C and 7-aminocephalosporanic acid respectively but was not active on cephamycin C.
Application of an amperometric immunosensor for the enumeration of Nitrobacter in activated sludge by B. Sandén; G. Dalhammar (pp. 413-417).
A competitive immunosensor using a monoclonal antibody has been developed for the enumeration of Nitrobacter in activated sludge and other environmental samples. Its cross-reactivity was tested against a number of bacterial strains and isolates. All strains of the nitrite-oxidising genera Nitrobacter and Nitrococcus reacted strongly with the monoclonal antibody. The nitrite-oxidising Nitrospira moscoviensis, as well as the ammonia oxidising bacteria and the heterotrophic bacteria tested, did not show any affinity towards the antibody in the immunosensor. The numbers of Nitrobacter were analysed in sludge samples from several wastewater treatment plants in Sweden. Detectable amounts were found in all samples. This study shows the adequacy of using this immunosensor for the enumeration of Nitrobacter in natural environments.
Use of microorganism-immobilized polyurethane foams to absorb and degrade oil on water surface by Y.-S. Oh; J. Maeng; S.-J. Kim (pp. 418-423).
Highly oil-absorbent polyurethane foam (PUF) materials were obtained by polymerizing polyether polyol mixture and carbodiimide-modified d-methyl diisocyanate in a weight ratio of 10:2. The foam materials were prepared to contain inorganic nutrients (slow-release fertilizer; SRF) and oil-degrading yeast cells, Yarrowia lipolytica 180, to be applied for removal of oil films on surface waters through absorption and biodegradation after oil spills. PUFs absorbed 7–9 times their own weight of Arabian light crude oil and the oil absorbency appeared to improve as the ratio of surface area to foam weight increased. PUFs showed excellent floatability which was maintained for more than 6 months in sea water, and less than 5% of the absorbed oil was released when the foams were left on water for more than 10 days. For immobilization of yeast cells into PUFs, various immobilization techniques were tested to compare their oil degrading ability and the maintenance thereof. All immobilized cells showed oil degrading abilities as good as those of free cells immediately after the preparation of PUFs, however, the activity of chitin-immobilized cells remained at a high level for the longest period of preservation. The high efficiency of oil absorption and oil degradation by PUF-immobilized yeast cells suggested that PUF-immobilized cells have a high potential as a bioremediation technique for the treatment of oil films on surface waters.
Biodegradation of propanol and isopropanol by a mixed microbial consortium by M. T. Bustard; E. M. McEvoy; J. A. S. Goodwin; J. G. Burgess; P. C. Wright (pp. 424-431).
The aerobic biodegradation of high concentrations of 1-propanol and 2-propanol (IPA) by a mixed microbial consortium was investigated. Solvent concentrations were one order of magnitude greater than any previously reported in the literature. The consortium utilized these solvents as their sole carbon source to a maximum cell density of 2.4 × 109 cells ml−1. Enrichment experiments with propanol or IPA as carbon sources were carried out in batch culture and maximum specific growth rates (μmax) calculated. At 20 °C, μ max values were calculated to be 0.0305 h−1 and 0.1093 h−1 on 1% (v/v) IPA and 1-propanol, respectively. Growth on propanol and IPA was carried out between temperatures of 10 °C and 45 °C. Temperature shock responses by the microbial consortium at temperatures above 45 °C were demonstrated by considerable cell flocculation. An increase in propanol substrate concentration from 1% (v/v) to 2% (v/v) decreased the μ max from 0.1093 h−1 to 0.0715 h−1. Maximum achievable biodegradation rates of propanol and IPA were 6.11 × 10−3% (v/v) h−1 and 2.72 × 10−3% (v/v) h−1, respectively. Generation of acetone during IPA biodegradation commenced at 264 h and reached a maximum concentration of 0.4% (v/v). The results demonstrate the potential of mixed microbial consortia in the bioremediation of solvent-containing waste streams.
Development of a rapid and sensitive bioassay device using human cells immobilized in macroporous microcarriers for the on-site evaluation of environmental waters by R. Shoji; Y. Sakai; A. Sakoda; M. Suzuki (pp. 432-438).
We developed a novel disposable bioassay device based on the fluorescein isothiocyanate-labelled low-density lipoprotein-uptake activity of human hepatoblastoma Hep G2 cells. The cells were cultured in porous microcarriers at a high cell density and packed in a filter tip that has a hydrophobic membrane. Upon evaluation of water samples, the culture medium was decanted by pipetting it down with a micropipet, and the samples were then introduced to the cell-immobilizing part of the tip only by pipetting them up after mixing them with ×10 concentrated culture medium. The new device enabled us to detect almost the same toxicity levels of river water within 2 h of exposure as those detected by a conventional 48-h cell-survival assay. This is the first bioassay device for the rapid on-site evaluation of environmental waters using cultured human cells, and therefore promising for water-quality management based on risk to humans.
Thermophilic acidification of dairy wastewater by H. Q. Yu; H. H. P. Fang (pp. 439-444).
Acidification of simulated dairy wastewater was conducted in an upflow reactor at 55 °C. Results showed that the degree of acidification decreased with the increase in chemical oxygen demand (COD) loading rate, from 60.8% at 4 g l−1 day−1 to 27.1% at 24 g l−1 day−1. Carbohydrate was readily degraded at all loading rates, but degradation of protein and lipid decreased with the increase in loading rate. Most carbohydrate degradation occurred at the reactor bottom, whereas protein was degraded mainly after the carbohydrate became depleted. The predominant acidification products were acetate, propionate, butyrate and ethanol, whereas formate, i-butyrate, valerate, i-valerate, caproate, lactate, methanol, propanol and butanol were present in lesser quantities. The increase in loading rate resulted in the increase of propionate and the decrease of acetate, but had little effect on ethanol and butyrate productions. Only 2.5–8.8% of influent COD was converted to hydrogen and methane. The biomass yield was 0.30–0.43 mg VSS mg−1 COD.
Screening of hexavalent chromium biosorbent from marine algae by D.-C. Lee; C.-J. Park; J.-E. Yang; Y.-H. Jeong; H.-I. Rhee (pp. 445-448).
A high-chromate-selective biosorbent with high adsorption capacity was sought by examining the chromate adsorption capacities of 48 species of red, brown, or green marine algae sampled from the east coast of Korea. Screening showed a red marine alga to have the most excellent adsorption characteristics among them, and it was identified as Pachymeniopsis sp. The period at which Pachymeniopsis sp. was sampled did not affect the adsorption capacity of the alga, but the optimum period for mass collection was April to May. The alga also showed high selectivity for chromate since its adsorption capacity for other heavy metal ions such as cadmium and manganese ions was relatively low. An investigation of the adsorption isotherm of dried powder of Pachymeniopsis sp. for chromate adsorption at 25 °C showed a Langmuir-type dependence. The maximum chromate adsorption capacity of the selected alga was about 225 mg/g. Desorption of the adsorbed chromate from Pachymeniopsis sp. was done by treating the sample with 1 N NaOH. It was confirmed that ion exchange type adsorption was observed with an anion exchanger but not with a cation exchanger. It is therefore believed that the chromate adsorption is based on anionic exchange of Pachymeniopsis sp.
