Abstract: Previously, a Saccharomyces cerevisiae strain was engineered for xylose assimilation by the constitutive overexpression of the Orpinomyces xylose isomerase, the S. cerevisiae xylulokinase, and the Pichia stipitis SUT1 sugar transporter genes. The recombinant strain exhibited growth on xylose, under aerobic conditions, with a specific growth rate of 0.025 h(-1), while ethanol production from xylose was achieved anaerobically. In the present study, the developed recombinant yeast was adapted for enhanced growth on xylose by serial transfer in xylose-containing minimal medium under aerobic conditions. After repeated batch cultivations, a strain was isolated which grew with a specific growth rate of 0.133 h(-1). The adapted strain could ferment 20 g l(-1) of xylose to ethanol with a yield of 0.37 g g(-1) and production rate of 0.026 g l(-1) h(-1). Raising the fermentation temperature from 30 degrees C to 35 degrees C resulted in a substantial increase in the ethanol yield (0.43 g g(-1)) and production rate (0.07 g l(-1) h(-1)) as well as a significant reduction in the xylitol yield. By the addition of a sugar complexing agent, such as sodium tetraborate, significant improvement in ethanol production and reduction in xylitol accumulation was achieved. Furthermore, ethanol production from xylose and a mixture of glucose and xylose was also demonstrated in complex medium containing yeast extract, peptone, and borate with a considerably high yield of 0.48 g g(-1).
Abstract: The cDNA sequence of the gene for xylose isomerase from the rumen fungus Orpinomyces was elucidated by rapid amplification of cDNA ends. The 1,314-nucleotide gene was cloned and expressed constitutively in Saccharomyces cerevisiae. The deduced polypeptide sequence encoded a protein of 437 amino acids which showed the highest similarity to the family II xylose isomerases. Further, characterization revealed that the recombinant enzyme was a homodimer with a subunit of molecular mass 49 kDa. Cell extract of the recombinant strain exhibited high specific xylose isomerase activity. The pH optimum of the enzyme was 7.5, while the low temperature optimum at 37 degrees C was the property that differed significantly from the majority of the reported thermophilic xylose isomerases. In addition to the xylose isomerase gene, the overexpression of the S. cerevisiae endogenous xylulokinase gene and the Pichia stipitis SUT1 gene for sugar transporter in the recombinant yeast facilitated the efficient production of ethanol from xylose.
Abstract: A hairy root line of Linum album LYR2i was obtained via the genetic transformation of a cotyledon segment of the plant by cocultivating it with Agrobacterium rhizogenes and culturing it in hormone-free B5 Gamborg liquid medium. Characteristic changes in root morphology associated with variations in biosynthetic capabilities were achieved by adding different combinations of phytohormones to the basal medium. A reversible system between hairy roots and its cultures with a diversified morphology was established by including and excluding phytohormones in the basal medium. The medium containing indole 3 acetic acid (IAA) at a concentration of 3 mg/l (MI3) induced thicker root tips and that containing 2,4-dichlorophenoxy acetic acid (2,4-D) at a concentration of 1 mg/l (MD1) induced compact green callus. Podophyllotoxin and 6-methoxypodophyllotoxin content increased by 1.86-fold and 1.45-fold as a result of adding IAA (MI3) and 2,4-D (MD1) to the basal medium, respectively. After regeneration, the hairy roots regained their original morphology and biosynthetic capability on hormone-free basal medium. The transformation status of the regenerated hairy roots was confirmed by PCR analysis.
Abstract: Cyathus bulleri, a ligninolytic fungus, produces a single laccase the internal peptides (3) of which bear similarity to laccases of several white rot fungi. Comparison of the total amino acid composition of this laccase with several fungal laccases indicated dissimilarity in the proportion of some basic and hydrophobic amino acids. Analysis of the circular dichroism spectrum of the protein indicated 37% alpha-helical, 26% beta-sheet and 38% random coil content which differed significantly from that in the solved structures of other laccases, which contain higher beta-sheet structures. The critical role of the carboxylic group containing amino acids was demonstrated by determining the kinetic parameters at different pH and this was confirmed by the observation that a critical Asp is strongly conserved in both Ascomycete and Basidiomycete laccases. The enzyme was denatured in the presence of a number of denaturing agents and refolded back to functional state with copper. In the folding experiments under alkaline conditions, zinc could replace copper in restoring 100% of laccase activity indicating the non-essential role of copper in this laccase. The laccase was expressed in Escherichia coli by a modification of the ligation-anchored PCR approach making it the first fungal laccase to be expressed in a bacterial host. The laccase sequence was confirmed by way of analysis of a 435 bp sequence of the insert.
Abstract: The effects of aeration within the range of 0.2-0.5 vvm on transformed and high yielding cell cultures of Linum album were investigated in a 5-L stirred tank bioreactor equipped with low shear Setric impeller. The kinetics of cell growth, substrate utilization, and production of lignans, namely, podophyllotoxin and 6-methoxypodophyllotoxin, were established. Maximum biomass of 23.2 g/L and lignan accumulation levels of 176.3 mg/L podophyllotoxin and 10.86 mg/L 6-methoxypodophyllotoxin were obtained with initial air flow rate of 0.3 vvm. Specified oxygen demand of cells was estimated to be 1.35 g O(2)/g biomass. The optimum oxygen transfer coefficient was found to be 16.7 h(-1) (,) which corresponded to aeration rate of 0.3 vvm. The effect of minimum dissolved oxygen (DO) concentration was investigated with respect to biomass and lignan production by comparing identically aerated and agitated bioreactor cultivations at dissolved oxygen concentrations of 10%, 30%, and 50%. Cell growth and podophyllotoxin accumulation were not affected significantly at these DO levels, but 6-methoxypodophyllotoxin production was enhanced when cells were cultivated at 30% DO level. The maximum volumetric productivities of 18.2 mg/L day and 3.2 mg/L day for podophyllotoxin and 6-methoxypodophyllotoxin, respectively, were obtained. These results establish the key role of oxygen on mass scale production of anticancer lignans by cell cultures of L. album. It may serve as a suitable parameter for scale-up.
Abstract: Various cell and hairy root cultures of L. album were developed and analyzed for podophyllotoxin content. Transformed callus and hairy root cultures developed from infection of stem portions of in vitro-germinated L. album plant with Agrobacterium rhizogenes NCIM 5140 strain were selected on the basis of high podophyllotoxin content and growth. Based on the integration of Ri T(L)-DNA and T(R)-DNA, integration of only the ags and not the rol gene in transformed cell culture indicated fragmented integration pattern. The effect of different cultivation media and carbon source on growth and podophyllotoxin production were studied in shake-flask suspension cultures. Detailed batch growth and production kinetics with sugar consumption profile were also established. Maximum volumetric productivity of 4.40 and 2.75 mg/L per day was obtained in cell suspension and hairy root cultures, respectively.
Abstract: Cell suspension cultures of Linum album were developed from internode portions of in vitro germinated plant in Gamborg's B5 medium supplemented with 0.4 mg naphthalene acetic acid/l. The highest biomass was 8.5 g/l with podophyllotoxin and 6-methoxypodophyllotoxin at 29 and 1.9 mg/l, respectively after 12 d cultivation. Co-cultures of L. album cells with axenically cultivable arbuscular mycorrhiza-like fungi, Piriformospora indica and Sebacina vermifera, were established for the first time. These enhanced podophyllotoxin and 6-methoxypodophyllotoxin production by about four- and eight-fold, respectively, along with a 20% increase in biomass compared to the control cultures.
Abstract: Many fungi (particularly the white rot) are well suited for treatment of a broad range of textile dye effluents due to the versatility of the lignin-degrading enzymes produced by them. We have investigated decolourization of a number of recalcitrant reactive azo and acid dyes using the culture filtrate and purified laccase from the fungus Cyathus bulleri. For this, the enzyme was purified from the culture filtrate to a high specific activity of 4,022 IU mg(-1) protein, produced under optimized carbon, nitrogen and C/N ratio with induction by 2,6-dimethylaniline. The protein was characterized as a monomer of 58+/-5.0 kDa with carbohydrate content of 16% and was found to contain all three Cu(II) centres. The three internal peptide sequences showed sequence identity (80-92%) with laccases of a number of white rot fungi. Substrate specificity indicated highest catalytic efficiency (k(cat)/K(M)) on guaiacol followed by 2,2'-azino-bis(3-ethylthiazoline-6-sulfonic acid) (ABTS). Decolourization of a number of reactive azo and acid dyes was seen with the culture filtrate of the fungus containing predominantly laccase. In spite of no observable effect of purified laccase on other dyes, the ability to decolourize these was achieved in the presence of the redox mediator ABTS, with 50% decolourization in 0.5-5.4 days.
Abstract: The production of methionine by submerged fermentation using a mutant strain of Corynebacterium lilium was studied to determine suitable conditions for obtaining high productivity. The mutant strain resistant to the methionine analogues ethionine, norleucine, methionine sulfoxide and methionine methylsulfonium chloride produced 2.34 g l(-1) of methionine in minimal medium containing glucose as carbon source. The effect of cysteine on methionine production in a 15 l bioreactor was studied by supplementing cysteine intermittently during the course of fermentation. The addition of cysteine (0.75 g l(-1)h(-1)) every 2 h to the production medium increased the production of methionine to 3.39 g l(-1). A metabolic flux analysis showed that during cysteine supplementation the ATP consumption reduced by 20%. It also showed that the increase in flux from phosphoenol pyruvate to oxaloacetate leads to higher methionine production. Results indicate that controlling the respiratory quotient close to 0.75 will produce the highest amount of methionine and that regulatory mutants also resistant to analogues of cysteine would be better methionine over producers.
Abstract: Beta-glucosidase II (Bgl II), encoded by the betaglu2 gene of the thermo-tolerant yeast Pichia etchellsii, was purified from recombinant Escherichia coli pBG22:JM109. The enzyme had a molecular mass of 176 kDa and was a dimer with an apparent subunit mass of 83 kDa. It exhibited broad substrate specificity and hydrolyzed beta-linked gluco-disaccharides and oligosaccharides, salicin, and cyanogenic glucoside amygladin. The unusually high hydrolytic activity of 7,680 units min(-1) g(-1) protein was obtained on sophorose. Competition experiments performed using differently linked beta-disaccharides indicated these to be hydrolyzed at the same active site. Transglycosylation activity leading to the biosynthesis of several disaccharides and oligosaccharides was observed. The enzyme was placed in glycosyl hydrolase family 3, based on a statistical approach using amino acid composition data. The involvement of His as a catalytically important residue was confirmed by diethylpyrocarbonate modification. Pre-incubation of the purified enzyme with 5 mM p-nitrophenyl-beta-D-glucoside offered 2.5-fold higher residual activity compared with unbound enzyme, indicating protection at the active site. The feasibility of this enzyme as a biocatalyst of choice for the synthesis of glyco-conjugates is discussed.
Abstract: The biosynthetic activity of yeast Pichia etchellsii beta-glucosidase II (BglII) expressed in recombinant Escherichia coli was utilized for synthesis of cellooligosaccharides, alkyl and terpene glucosides. Cellooligosaccharides with a degree of polymerization of 3 and greater were resolved by thin-layer chromatography (TLC) using an ethyl acetate:1-propanol:2-propanol:water (8:5:1:1) solvent system followed by visualization with 0.2% naphthoresorcinol reagent. Using 2M cellobiose and 15 IU of partially purified BglII, 57 mmol/L of oligosaccharides (comprising mostly cellotriose and cellopentaose) was synthesized in 16 h. Similarly, alkyl glucosides with chain lengths from 6 to 10 carbons were synthesized and products extracted to near purity by ethyl acetate extraction. The same extraction method was employed to separate, to near purity, various monoterpenyl (nerol, geraniol, citronellol) glucosides. A reliable and simple method for separation of cellooligosaccharides using a combination of Bio-Gel P-2 gel filtration and charcoal celite adsorption chromatography was developed. The cellooligosaccharides were separated to purity as confirmed by TLC. The enzyme was among the very few that could synthesize a wide variety of glycoconjugates.
Abstract: The natural lignan podophyllotoxin, a dimerized product of two phenylpropanoid moieties which occurs in a few plant species, is a pharmacologically important compound for its anticancer activities. It is used as a precursor for the chemical synthesis of the anticancer drugs etoposide, teniposide and etopophose. The availability of this lignan is becoming increasingly limited because of the scarce occurrence of its natural sources and also because synthetic approaches for its production are still commercially unacceptable. Biotechnological production using cell culture may be considered as an alternative source. Selection of the best performing cell line, its maintenance and stabilization are necessary prerequisites for its production in bioreactors and subsequent scale-up of the cultivation process to the industrial level. Scale-up of growth and product yield depends on a multitude of factors, such as growth medium, physicochemical conditions, seed inoculum, type of reactor and processing conditions. The composition of the growth medium, elicitors and precursors, etc. can markedly influence the production. Optimum levels of parameters that facilitate high growth and product response in cell suspensions of Podophyllum hexandrum have already been determined by statistical design. P. hexandrum cells have successfully been cultivated in a 3-l stirred-tank bioreactor under low shear conditions in batch and fed-batch modes of operation. The batch kinetic data were used to identify the mathematical model which was then used to develop nutrient-feeding strategies for fed-batch cultivation to prolong the productive log phase of cultivation. An improvement in the production of podophyllotoxin to 48.8 mg l(-1) in a cell culture of P. hexandrum was achieved, with a corresponding volumetric productivity of 0.80 mg l(-1) day(-1), when the reactor was operated in continuous cell-retention mode. Efforts are being made to further enhance its production levels by the development of hairy root culture or by varying the channeling of precursors towards the desired biosynthetic pathway by molecular approaches.
Abstract: Podophyllotoxin was produced by cell culture of Podophyllum hexandrum under in vitro culture conditions. A maximum of 4.26 mg/L of podophyllotoxin was produced when P. hexandrum was cultivated in 3 L stirred tank bioreactor. The compound extracted from the cell culture was applied to the human breast cancer cell line (MCF-7) and 1 nM podophyllotoxin was able to inhibit the growth of the cancer cells by 50%. The most profound inhibitory effect of podophyllotoxin was observed when it was applied in the beginning of cell growth.
Abstract: The effect of major medium ingredients (sugar, nitrogen source and phosphate) in Podophyllum hexandrum suspension cultures was investigated in order to increase the production of podophyllotoxin, the raw material in the synthesis of anticancer drugs. Amongst B5, Eriksson, MS, Nitsch, Street and White's medium, MS medium resulted in high growth and podophyllotoxin accumulation. The optimum level of nitrogen was found to be 60 mM, with a combination of ammonium salts and nitrate in the ratio of 1:2. The highest level of podophyllotoxin was obtained at 60 g glucose/l and at 1.25 mM phosphate after 30 days. Statistical design was adopted to determine the optimum levels of the parameters for cell growth and podophyllotoxin production.
Abstract: The rhizomes of the rare plant Podophyllum hexandrum contain podophyllotoxin, which is a precursor of the anticancer drugs etoposide and teniposide. Batch cultivation of Podophyllum hexandrum was conducted using optimized medium in a 3 L bioreactor, which resulted in biomass and podophyllotoxin concentrations of 21.4 g/L and 13.8 mg/L in 24 and 26 days, respectively. The batch kinetics was used to identify the mathematical model. The model was extrapolated to identify the nutrient feeding rate (150 mL/d) and substrate concentration (105 g/L) in the incoming feed for nonlimiting and noninhibitory glucose concentration in the cell retention bioreactor. An improvement in cell growth to 53 g/L and intracellular podophyllotoxin accumulation of 48.8 mg/L was achieved in 60 days, when the bioreactor was operated in continuous cell retention cultivation mode.
Abstract: Xylanase of Melanocarpus albomyces IIS 68 was immobilized on Eudragit L-100. The latter is a copolymer of methacrylic acid and methyl methacrylate and is a pH-sensitive smart polymer. The immobilization was carried out by gentle adsorption and an immobilization efficiency of 0.82 was obtained. The enzyme did not leach off the polymer even in the presence of 1 M NaCl and 50% ethylene glycol. The K(m) of the enzyme changed from 5.9 mg ml(-1) to 9.1 mg ml(-1) upon immobilization. The V(max) of the immobilized enzyme showed an increase from 90.9 micro mol ml(-1) min(-1) (for the free enzyme) to 111.1 micro mol ml(-1) min(-1). The immobilized enzyme could be reused up to ten times without impairment of the xylanolytic activity. The immobilized enzyme was also evaluated for its application in pre-bleaching of eucalyptus kraft pulp.
Abstract: The hydrolysis and biosynthetic reactions of partially purified Pichia etchellsii beta-glucosidase II from recombinant Escherichia coli pBG22:JM109 are described. With 167 mmol/L of initial glucose, the products of synthetic reactions, glucobiose and glucotriose, accumulated to 18 and 6 mmol/L, respectively. In transglycosylation reactions with 79 mmol/L of initial cellobiose, glucotriose and glucopentaose were obtained at 4.5 and 2 mmol/L, respectively. The effects of incubation time and substrate concentration were studied on the yield of synthesized oligosaccharides. In a reaction time of 24 h with 468 mmol/L of initial cellobiose, glucotriose and glucopentaose levels of 21.6 and 6.6 mmol/L, respectively, were obtained. The addition of dimethyl sulfoxide (DMSO) further increased the yields of the products by 10%. Detailed kinetic analysis indicated a significant (about twofold) increase in Vmax/KM of synthetic reactions in the presence of DMSO. A study of other disaccharides in transglycosylation reactions indicated biosynthetic activity in the order of sophorose > gentiobiose > cellobiose.
Abstract: Beta-glucosidases constitute a major group among glycosylhydrolase enzymes. Out of the 82 families classified under glycosylhydrolase category, these belong to family 1 and family 3 and catalyze the selective cleavage of glucosidic bonds. This function is pivotal in many crucial biological pathways, such as degradation of structural and storage polysaccharides, cellular signaling, oncogenesis, host-pathogen interactions, as well as in a number of biotechnological applications. In recent years, interest in these enzymes has gained momentum owing to their biosynthetic abilities. The enzymes exhibit utility in syntheses of diverse oligosaccharides, glycoconjugates, alkyl- and aminoglucosides. Attempts are being made to understand the structure-function relationship of these versatile biocatalysts. Earlier reviews described the sources and properties of microbial beta-glucosidases, yeast beta-glucosidases, thermostable fungal beta-glucosidase, and the physiological functions, characteristics, and catalytic action of native beta-glucosidases from various plant, animal, and microbial sources. Recent efforts have been directed towards molecular cloning, sequencing, mutagenesis, and crystallography of the enzymes. The aim of the present article is to describe the sources and properties of recombinant beta-glucosidases, their classification schemes based on similarity at the structural and molecular levels, elucidation of structure-function relationships, directed evolution of existing enzymes toward enhanced thermostability, substrate range, biosynthetic properties, and applications.
Abstract: The root explants of the germinated seedlings of Podophyllum hexandrum were grown in MS medium supplemented with indole acetic acid (IAA) (2 mg/L) and activated charcoal (0.5%), and healthy callus culture was obtained after incubation for 3 wk at 20 degrees C. The cultivation of plant cells in shake flask was associated with problems such as clumping of cells and browning of media, which were solved by the addition of pectinase and polyvinylpyrrolidone. The effect of major media components and carbon source was studied on the growth and podophyllotoxin production in suspension culture. It was found that glucose was a better carbon source than sucrose and that NH4+:NO3- ratio (total nitrogen concentration of 60 mM) and PO4(3-) did not have much effect on the growth and product formation. The relative effect of culture parameters (inoculum level, pH, IAA, glucose, NH4+:NO3- ratio, and PO4(3-)) on the overall growth and product response of the plant cell suspension culture was further investigated by Plackett-Burman design. This indicated that inoculum level, glucose, IAA, and pH had significant effects on growth and production of podophyllotoxin. To identify the exact optimum concentrations of these parameters on culture growth and podophyllotoxin production, central composite design experiments were formulated. The overall response equations with respect to growth and podophyllotoxin production as a function of these culture parameters were developed and used to determine the optimum concentrations of these parameters, which were pH 6.0, 1.25 mg/L of IAA, 72 g/L of glucose, and inoculum level of 8 g/L.
Abstract: Submerged cultivation of Podophyllum hexandrum for the production of podophyllotoxin was carried out in a 3l stirred tank bioreactor fitted with a low-shear Setric impeller. The specific requirements of the medium, such as carbon source (sugar) and light, were established for the growth of and podophyllotoxin production by P. hexandrum in suspension cultures. Substitution of sucrose by glucose resulted in higher growth and podophyllotoxin production. The biosynthesis of podophyllotoxin was favored when plant cells were cultivated in the dark. An agitation speed of 100 rpm was sufficient to mix the culture broth in the bioreactor without causing any significant cell damage. Biomass and podophyllotoxin accumulation in 3 l bioreactor under batch growth conditions were 6.5 g/l and 4.26 mg/l, respectively, in 22 d. This resulted in an overall podophyllotoxin productivity of 0.19 mg/(l.d), which represented an increase of 27% in comparison to its productivity in a shake flask. Podophyllotoxin production was found to be a combined growth-associated and non-growth associated process.
Abstract: The solid-state bioconversion of wheat straw by Phanerochaete chrysosporium for the production of animal feed was studied. This study was performed based on a central composite experimental design. The conditions of the seed culture most suitable for rapid induction of the ligninolytic activity of the fungus, when the seed culture is subsequently used for solid-state bioconversion of wheat straw, were determined. When the seed culture with an initial pH of 5.8 was grown under agitated conditions at 130 rpm in baffled flasks at 38 degrees C, it was predicted to give lignin degradation of 19.5% and cellulose degradation of 17.8%. A time profile study of the solid-state bioconversion of wheat straw indicated that the highest lignin and lowest cellulose degradation levels occurred on the sixth day of cultivation. The desirability coefficient for this process also passed through a maximum of 0.705 on the sixth day.
Abstract: Xylanase production by the thermophilic fungus, Melanocarpus albomyces IIS68, during solid state fermentation of wheat straw was studied and the effects of various variables were observed. Using the response surface methodology and the multivariant statistical approach, the optimum levels of the variables affecting xylanase production were determined. The optimum levels of the variables were 600-850 microm particle size, 43 h inoculum age, 1.37% Tween 80, 86% initial moisture content, 5.1% urea, 0.74% yeast extract and a harvest time of 96 h. Under these optimized conditions, xylanase activity of 7760 U/g initial dry substrate was obtained which was in very good agreement with the value predicted by the quadratic model (7890 U/g initial dry substrate).
Abstract: Simultaneous isomerisation and fermentation (SIF) of xylose and simultaneous isomerisation and cofermentation (SICF) of a glucose/xylose mixture was carried out by Saccharomyces cerevisiae in the presence of xylose isomerase. The SIF of 50 g I(-1) xylose gave an ethanol concentration and metabolic yield of 7.5 g l(-1) and 0.36 g (g xylose consumed)(-1). These parameters improved to 13.4 g l(-1) and 0.40 respectively, when borate was added to the medium. The SICF of a mixture of 50 g l(-1) glucose and 50 g l(-1) xylose gave an ethanol concentration and metabolic yield of 29.8 g l(-1) and 0.42 respectively, in the presence of borate. Temperature modulation from 30 degrees C to 35 degrees C during fermentation further enhanced the above parameters to 39 g l(-1) and 0.45 respectively. The approach was extended to the bioconversion of sugars present in a real lignocellulose hydrolysate (peanut-shell hydrolysate) to ethanol, with a fairly good yield.
Abstract: India has embarked upon a very ambitious program in biotechnology with a view to harnessing its available human and unlimited biodiversity resources. It has mainly been a government sponsored effort with very little private industry participation in investment. The Department of Biotechnology (DBT) established under the Ministry of Science and Technology in 1986 was the major instrument of action to bring together most talents, material resources, and budgetary provisions. It began sponsoring research in molecular biology, agricultural and medical sciences, plant and animal tissue culture, biofertilizers and biopesticides, environment, human genetics, microbial technology, and bioprocess engineering, etc. The establishment of a number of world class bioscience research institutes and provision of large research grants to some existing universities helped in developing specialized centres of biotechnology. Besides DBT, the Department of Science & Technology (DST), also under the Ministry of S&T, sponsors research at universities working in the basic areas of life sciences. Ministry of Education's most pioneering effort was instrumental in the creation of Biochemical Engineering Research Centre at IIT Delhi with substantial assistance from the Swiss Federal Institute of Technology, Zurich, Switzerland to make available state-of-the-art infrastructure for education, training, and research in biochemical engineering and biotechnology in 1974. This initiative catalysed biotechnology training and research at many institutions a few years later. With a brief introduction, the major thrust areas of biotechnology development in India have been reviewed in this India Paper which include education and training, agricultural biotechnology, biofertilizers and biopesticides, tissue culture for tree and woody species, medicinal and aromatic plants, biodiversity conservation and environment, vaccine development, animal, aquaculture, seri and food biotechnology, microbial technology, industrial biotechnology, biochemical engineering and associated activities such as creation of biotechnology information system and national repositories. Current status of intellectual property rights has also been discussed. Contribution to the India's advances in biotechnology by the industry, excepting a limited few, has been far below expectations. The review concludes with some cautious notes.
Abstract: The ascomycetous fungus Melanocarpus albomyces when grown on wheat straw produced seven extracellular xylanase isoenzymes, designated as la, Ib, Ic, IIa, lib, llc, and lId. All seven xylanases were purified to homogeneity by gel filtration and ion-exchange chromatography. The molecular mass (kDa) of la, lb, Ic, Ila, lIb, lIc, and lId were estimated to be 22.9, 20.7, 18.6, 31.3, 25.4, 38.5, and 34.3, respectively by SDS-PAGE, and 23.7, 20.5, 17.1, 31.7, 25.1, 39.8, and 32.2, respectively by gel filtration. The isoelectric points of Ia, lb, Ic, Ila and IIb were found to be 6.2, 6.3, 6.4, 3.7, and 4.4, respectively. The activity of the isoenzymes was dependent on the type of the xylan substrates; Xylanases Ia, lb, and Ic showed highest specific activity toward larchwood xylan (an arabinoglucuronoxylan), IIa and Ilc toward birchwood xylan (a glucuronoxylan), and llb and IId toward beechwood xylan (a glucuronoxylan). Four isoenzymes la, lb, Ic, and Ila had an arabinose-releasing property on larchwood xylan. Application of specific isoenzymes as prebleaching agents in paper manufacture is proposed.
Abstract: Lignocellulosic materials containing cellulose, hemicellulose, and lignin as their main constituents are the most abundant renewable organic resource present on Earth. The conversion of both cellulose and hemicellulose for production of fuel ethanol is being studied intensively with a view to develop a technically and economically viable bioprocess. The fermentation of glucose, the main constituent of cellulose hydrolyzate, to ethanol can be carried out efficiently. On the other hand, although bioconversion of xylose, the main pentose sugar obtained on hydrolysis of hemicellulose, to ethanol presents a biochemical challenge, especially if it is present along with glucose, it needs to be fermented to make the biomass-to-ethanol process economical. A lot of attention therefore has been focussed on the utilization of both glucose and xylose to ethanol. Accordingly, while describing the advancements that have taken place to get xylose converted efficiently to ethanol by xylose-fermenting organisms, the review deals mainly with the strategies that have been put forward for bioconversion of both the sugars to achieve high ethanol concentration, yield, and productivity. The approaches, which include the use of (1) xylose-fermenting yeasts alone, (2) xylose isomerase enzyme as well as yeast, (3) immobilized enzymes and cells, and (4) sequential fermentation and co-culture process are described with respect to their underlying concepts and major limitations. Genetic improvements in the cultures have been made either to enlarge the range of substrate utilization or to channel metabolic intermediates specifically toward ethanol. These contributions represent real significant advancements in the field and have also been adequately dealt with from the point of view of their impact on utilization of both cellulose and hemicellulose sugars to ethanol.
Abstract: Precursor feeding strategy for increasing the yield of conessine, a steroidal alkaloid of Holarrhena antidysenterica, was established in cell suspension culture. A total of 50 mg/L added cholesterol was converted into 43 mg/L of alkaloid, 90% of which constituted the conessine. By applying the precursor feeding policy to the cell suspension culture in modified Murashige and Skoog (MS) medium, a total of 143 mg/L of alkaloid was produced in 8 days. In this way the alkaloid content of the cells was increased more than six times compared to that obtained in the standard MS medium. The steps leading to biotransformation of cholesterol into alkaloids were unaffected by phosphate. The shake flask data were successfully transferred to a bench scale 6-L stirred tank bioreactor in which the specific biosynthetic rate of alkaloid production was 110 mg/100 g dry cell weight per day, about 160 times higher than that of whole plant.
Abstract: The effect of major nutrients on growth and alkaloid production by plant cell culture of Holarrhena antidysenterica was studied with a view to increasing the yield of the alkaloid conessine, a therapeutic drug used for treatment of dysentery and helminthic disorders. The studies resulted in development of a modified Murashige and Skoog (MS) medium that contained 60 mM total nitrogen with a NH(4) (+)-to-NO(3) (-) ratio of 5:1, 0.25 mM phosphate, and 40 g/L sucrose. The growth regulators 2,4-dichlorophenoxy acetic acid (2,4-D) and kinetin (Kn) were also found to affect the synthesis of alkaloid. Using an optimal level of inoculum (3 g/L), the modified medium resulted in alkaloid synthesis of 0.66 g/100 g dry cell weight, which represented a 4.25-fold increase over that obtained in standard MS medium.
Abstract: A simple differential method based on measurement of an intracellular pigment of Aspergillus wentii was developed for estimation of the individual growths of two fungi, Trichoderma reesei and A. wentii, in mixed-culture fermentation of an insoluble cellulosic substrate.
Abstract: The cellulase enzyme system consists of cellobiohydrolase, endoglucanase, and beta-glucosidase and has been extensively studied with respect to its biosynthesis, properties, mode of action, application, and, most recently, secretion mechanisms. A knowledge of the factors governing the biosynthesis and secretion of these enzymes at the molecular level will be useful in maximizing enzyme productivity in extracellular fluid. Among other topics, the regulatory effects of sorbose (a noninducing sugar which is not a product of cellulose hydrolysis) on cellulase synthesis and release are described. Cellulase genes have recently been cloned into a number of microorganisms with a view to understanding the gene structure and expression and to obtaining the enzyme components in pure form. The factors governing biosynthesis and secretion of cellulases in recombinant cells are also discussed. Cellulases are known to be glycoproteins, therefore, the role of O- and N-linked glycosylation on enzyme stability and secretion is also detailed.
Abstract: Bacillus amyloliquefaciens H produces a restriction endonuclease enzyme BamHl which is heat labile even at low temperatures. Studies were conducted to enhance thermal stability of BamHl using cross-linking reagents, namely, glutaraldehyde, dimethyl adipimidate (DMA), dimethyl suberimidate (DMS), and dimethyl 3,3'-dithiobispropionimidate (DTBP). Reaction with glutaraldehyde did not result in a preparation with enhanced thermal stability. However, the DMA-, DMS-, and DTBP-cross-linked preparations of BamHI exhibited significant improvement in thermal stability. Studies on thermal denaturation of the cross-linked enzyme preparations revealed that these do not follow a true first-order kinetics A possible deactivation scheme has been proposed in which the enzyme has been envisaged to go through a fully active but more susceptible transient state which, on prolonged heat exposure, exhibits a first-order decay kinetics. At 35 degrees C, which is close to the optimum reaction temperature of 37 degrees C for BamHl activity, the half-line of DMA-, DMS-, and DTBP-cross-linked preparations were 4.0, 5.25, and 5.5 h, respectively, whereas the native enzyme exhibited a half-line of 1.2 h only. The apparent values of deactivation rate constants for native, DMA-, DMS-, and DTBP-cross-linked BamHl were 1.13, 0.39, 0.29, and 0.26 h(-1), respectively, at the same temperature, and the apparent values of activation energies for denaturation of native, DMA-, DMS-, and DTBP-cross-linked BamHl were 2.63, 5.24, 6.55, and 9.2 kcal/mol, respectively. The DTBP-cross-linked Bam HI was, therefore, the best heat-stable preparation among those tested. The unusually low values of activation energies for denaturation of Bam Hl represent their highly thermolabile nature compared to other commonly encountered enzymes such as trypsin, having activation energies of more than 40 kcal/mol for their denaturation.
Abstract: A significant increase in extracellular xylanase activity was observed in the mixed culture fermentation of Trichoderma reesei D1-6 and Aspergillus wentii Pt 2804 when A. wentii inoculation was phased by 15 h. A. wentii produced a polysaccharide, chiefly consisting of glucose monomeric units, which was required for expression of maximum xylanase activity. Expression of high activity of xylanase in the A. wentii phased mixed culture compared to that in either T. reesei or A. wentii single cultures appeared to be controlled by the combined action of a polysaccharide produced by A. wentii and the relative growth of the two fungi in the mixed culture.
Abstract: Significant increase in extracellular cellulase and hemicellulase activities was observed in the biosynthesis of cellulase enzyme in mixed culture fermentation of Trichoderma reesei D 1-6 and Aspergillus wentii Pt 2804 when the A. wentii inoculation was phased by 15 h. The optimal conditions of fermentation by the mixed culture have been established. Presence of mannanase has been found to affect the release as well as activity of cellulase enzyme produced in mixed culture.
Abstract: Most cellulosic substances contain appreciable amounts of cellulose and hemicellulose, which on enzymatic hydrolysis mainly yield a mixture of glucose, cellobiose, and xylose. In this paper, studies on the mechanisms of hydrolysis of bagasse (a complex native cellulosic waste left after extraction of juice from cane sugar) by the cellulase enzyme components are described in light of their adsorption characteristics. Simultaneous adsorption of exo- and endoglucanases on hydrolyzable cellulosics is the causative factor of the hydrolysis that follows immediately after. It supports the postulate of synergistic enzyme action proposed by Eriksson. Xylanase pretreatment enhanced the hydrolysis of bagasse owing to the creation of more accessible cellulosic regions that are readily acted upon by exo- and endoglucanases. The synergistic action of the purified exoglucanase, endoglucanase, and xylanse has been found to be most effective for hydrolysis of bagasse but not for pure cellulose. Significant quantities of glucose are produced in beta-glucosidase-free cellulase action on bagasse. Individual and combined action of the purified cellulase components on hydrolysis of native and delignified bagasse are discussed in respect to the release of sugars in the hydrolysate.
