Acceptor reactions of a novel transfructosylating enzyme from Bacillus sp.

Many different oligosaccharides were produced by transferring the fructose residue of sucrose to maltose, cellobiose, lactose and sucrose (self-transfer), where their yields of fructosylated acceptor products accounted for 26–30% (w/w). The maximum conversion yield (30%) was obtained in fructosyl cellobioside formation with 500 g sucrose l^–1 (substrate) and 200 g cellobiose l^–1 (acceptor). These four acceptors gave various products having DP (degree of polymerization) 2–7 by successive transfer reactions.     

Synthesis of recombinant human interleukin-2 via controlled feed of lactose-complex media in fed-batch cultures of Escherichia coli BL21(DE3)[pT7-G3IL2]

Using lactose as an inducer, recombinant human interleukin-2 (rhIL-2) was synthesized with an N-terminus fusion partner, G3 (three tandem-arranged glucagon peptides) in fed-batch cultures at high cell concentration (60–90 g l^–1) of Escherichia coli BL21(DE3) [pT7-G3IL2]. With batch additions of lactose (4 × 13.5 g), the fusion rhIL-2 was synthesized up to 9.3 g l^–1. However, if all the lactose (54 g) was added at once to the culture, synthesized fusion rhIL-2 decreased to 5.4 g l^–1 with a decreased cell growth rate. A statistical optimization of the production medium containing glucose, yeast extract, and lactose led to fusion rhIL-2 being produced at > 9 g l^–1.     

Decolorization of textile dyestuffs by a mixed bacterial consortium

A mixed anaerobic bacterial culture decolorized Drimaren Orange K-GL, Everzol Red RBN and Everdirect Supra Yellow PG dyestuffs at 200 mg dyestuff l^–1 over 24 h. Improved performance with complete decolorization within 24 h was achieved by incubation with 5 g yeast extract l^–1 compared to glucose, lactose and sucrose though 50 mg yeast extract l^–1 supplemented with 5 g lactose l^–1 or 5 g sucrose l^–1 also resulted in complete decolorization within 24 h.     

Production of poly(3-hydroxybutyrate) from whey by fed-batch culture of recombinant Escherichia coli in a pilot-scale fermenter

Production of poly(3-hydroxybutyrate) [P(3HB)] from wheyby fed-batch culture of recombinant Escherichia coli CGSC 4401 harboring a plasmid containing the Alcaligenes latus polyhydroxyalkanoate (PHA) biosynthesis genes was examined in a 30 l fermenter supplying air only. With lactose below 2 g l^–1, cells grew to 12 g dry cell l^–1 with 9% (w/w) P(3HB) content. Accumulation of P(3HB) could be triggered by increasing lactose to 20 g l^–1. By employing this strategy, 51 g dry cell l^–1 was obtained with a 70% (w/w) P(3HB) content after 26 h. The productivity was 1.35 g P(3HB) l^–1 h^–1. The same fermentation strategy was used in a 300 l fermenter, and 30 g dry cell l^–1 with 67% (w/w) P(3HB) content was obtained in 20 h.     

Production of fructosylxyloside by the new fructosyltransferase from Bacillus macerans EG-6

The new fructosyltransferase (FTase) from Bacillus maceransEG-6 showed a broad acceptor specificity, and resulted in the formation of fructosylxyloside (FX) with d-xylose being the most effective acceptor. The optimal FTase concentration for FX production was 0.6 unit per g sucrose, which gave the highest transfer ratio, 83%, of fructosyl moiety from sucrose to d-xylose. Maximum yield of FX was 114 g l^–1with 200 g sucrose l^–1and 300 g d-xylose l^–1.     

Production of cellulases in batch culture using a mutant strain of Trichoderma reesei growing on soluble carbon source

Trichoderma reesei Rut-C30 is a highly derepressed mutant which synthesised active cellulases in culture media containing glucose and lactose as the only carbon sources. The maximum biomass, filter paper and specific filter paper activities for cell growth on 20 g glucose l^–1 were 20 g dry cell wt l^–1, 1.9 FPU ml^–1 and 4.8 FPU mg^–1 protein respectively, while on 40 g glucose l^–1 were 25 g dry cell wt l^–1, 4.5 FPU ml^–1 and 6.2 FPU mg^–1 protein, respectively. This strain had a higher specific filter paper activity (6.2 FPU mg^–1 protein) than was produced by other T. reesei mutants (3.6 FPU mg^–1 protein).     

Improvement of cephalomanine production in Taxus chinensis cells by a combination of sucrose and methyl jasmonate

Cell suspension cultures of Taxus chinensis, supplemented with 25 g sucrose l^–1, produced 11 mg cephalomanine l^–1, 21 g biomass l^–1 and 19 nkat geranylgeranyl diphosphate (GGPP) synthase activity g protein^–1. Supplementation of the cultures with 100 M methyl jasmonate (MJA) produced 17 mg cephalomanine l^–1, 6 g biomass l^–1 and 78 nkat GGPP synthase activity g protein^–1. Addition of sucrose and MJA together produced 24 mg cephalomanine l^–1, 18 g biomass l^–1 and 55 nkat GGPP synthase activity g protein^–1.     

Effects of activated charcoal, explant size, explant position and sucrose concentration on plant and shoot regeneration of Lilium longiflorum via young stem culture

An efficient system for the in vitro plant and shootregeneration of Lilium longiflorum was developed andaccomplished using transverse thin cell layers (tTCL) of young stems.tTCLs were cut transversely along young stems from which the shoot-tipshad been removed. Sections were measured accurately using a graded gridand were cut in 4 mm × 4 mm × 1 mm cubes, eliminatingepidermal tissue, and were cultured on one-half MS medium containing 8 gl^–1 agar, different sucrose concentrations (10, 20, 30 or 40g l^–1), and with or without 1 mg l^–1 activatedcharcoal (AC). Plants formed on the surface of tTCLs within 60 days onone-half MS medium containing 8 g l^–1 agar and 20 gl^–1 sucrose. Sections of 1 mm taken just below the apicalarea developed buds within 15 days, whereas the sections closer to thebase required about 45 days. Shoot regeneration was enhanced whensucrose concentration was used at 30 or 40 g l^–1 after 60days of culture. No root formation occurred. Both shooting and rootingoccurred when sucrose was used at 20 g l^–1. The plantletswere transferred to soil and grew well under greenhouseconditions.     

Production of poly(3-hydroxybutyrate) from whey by cell recycle fed-batch culture of recombinant Escherichia coli

A new fermentation strategy using cell recycle membrane system was developed for the efficient production of poly(3-hydroxybutyrate) (PHB) from whey by recombinant Escherichia coli strain CGSC 4401 harboring the Alcaligenes latus polyhydroxyalkanoate (PHA) biosynthesis genes. By cell recycle, fed-batch cultivation employing an external membrane module, the working volume of fermentation could be constantly maintained at 2.3 l. The final cell concentration, PHB concentration and PHB content of 194 g l^–1, 168 g l^–1 and 87%, respectively, were obtained in 36.5 h by the pH-stat cell recycle fed-batch culture using whey solution concentrated to contain 280 g lactose l^–1 as a feeding solution, resulting in a high productivity of 4.6 g PHB l^–1 h^–1.     

Lactic acid fermentation by Lactobacillus casei in free cell form and immobilised on gluten pellets

A comparative study of the fermentation of a range of carbohydrate substrates, at various temperatures, was carried out using a commercial Lactobacillus casei strain in a free cell form and immobilised on gluten pellets. This strain required yeast extract, l-cysteine HCl and Mn²⁺ at 5, 0.5 and 0.1 g l^–1, respectively, for maximum growth and lactic acid production. Sugar fermentation using free cells showed preference in the order glucose, sucrose, fructose while lactose was poorly utilised. Optimum temperature for growth and lactic acid production over (18–30 h) was 43 °C. L. casei was successfully immobilised on gluten pellets and fermented glucose and sucrose in a shorter time (18 h) with increased lactic acid production (42 and 41 g l^–1 on glucose and sucrose, respectively).     

Batch propagation of Lactobacillus helveticus for production of lactic acid from lactose concentrated cheese whey with microaeration and nutrient supplementation

Continuous mix batch bioreactors were used to study the kinetic parameters of lactic acid fermentation in microaerated-nutrient supplemented, lactose concentrated cheese whey using Lactobacillus helveticus. Four initial lactose concentrations ranging from 50 to 150 g l^–1 were first used with no microaeration and no yeast extract added to establish the substrate concentration above which inhibition will occur and then the effects of microaeration and yeast extract on the process kinetic parameters were investigated. The experiments were conducted under controlled pH (5.5) and temperature (42 °C) conditions. The results indicated that higher concentrations of lactose had an inhibitory effect as they increased the lag period and the fermentation time; and decreased the specific growth rate, the maximum cell number, the lactose utilization rate, and the lactic acid production rate. The maximum lactic acid conversion efficiency (75.8%) was achieved with the 75 g l^–1 initial lactose concentration. The optimum lactose concentration for lactic acid production was 75 g l^–1 although Lactobacillus helveticus appeared to tolerate up to 100 g l^–1 lactose concentration. Since the lactic acid productivity is of a minor importance compared to lactic acid concentration when considering the economic feasibility of lactic acid production from cheese whey using Lactobacillus helveticus, a lactose concentration of up to 100 g l^–1 is recommended. Using yeast extract and/or microaeration increased the cell number, specific growth rate, cell yield, lactose consumption, lactic acid utilization rate, lactic acid concentration and lactic acid yield; and reduced the lag period, fermentation time and residual lactose. Combined yeast extract and microaeration produced better results than each one alone. From the results it appears that the energy uncoupling of anabolism and catabolism is the major bottleneck of the process. Besides lactic acid production, lactose may also be hydrolysed into glucose and galactose. The -galactosidase activity in the medium is caused by cell lysis during the exponential growth phase. The metabolic activities of Lactobacillus helveticus in the presence of these three sugars need further investigation.     

Lactic acid production using two food processing wastes,canned pineapple syrup and grape invertase,as substrate and enzyme

Canned pineapple syrup, a food processing waste, was utilized as a substrate for lactic acid production by Lactococcus lactis. To improve the utilization of sucrose from the syrup, grape invertase from grape juice derived from wine production was used for sucrose hydrolysis. The highest lactic acid concentrations achieved were 20 and 92 g l^–1 from 20 and 100 g total sugars l^–1, respectively, without a lag period for sucrose consumption.     

Micropropagation of zedoary (<Emphasis Type="Italic">Curcuma zedoaria</Emphasis> Roscoe) – a valuable medicinal plant

Tissue culture propagation system was developed for zedoary (Curcuma zedoaria Roscoe), a valuable medicinal plant, using rhizome sprout cultures. Shoots were induced from rhizomes on basal MS medium containing 20 g l^–1 sucrose and 5 g l^–1 agar, supplemented with 20 (v/v) coconut water (CW) and benzylaminopurine (BA) concentrations from 0.5 to 5.0 m g l^–1. The excised shoots were subcultured on Murashige-Skoog (MS) medium with 20 (v/v) CW and different concentrations of BA and kinetin (Kin), either alone or in combination with indolebutyric acid (IBA) or naphthaleneacetic acid (NAA). MS medium with 20 (v/v) CW, 3 mg l^–1 BA, and 0.5 mg l^–1 IBA resulted in a multiplication rate per shoot; 5.6 shoots per explant were obtained on average after 30 days of culture. Well-developed shoots (30–40 mm in length) were rooted on MS medium containing 20 g l^–1 sucrose and 8 g l^–1 agar, supplemented with 20 (v/v) CW and 2 mg l^–1 NAA. More than 95 of the rooted plants were established in pots after hardening.     

Induced Activity of Superoxide Dismutase and Peroxidase of in vitro Plants by Low Concentrations of Ethanol

A rapid micropropagation protocol was established for Aloe vera L. var. chinensis (Haw.) Berger, Chinese Aloe. The effects of three factors, namely BA, NAA and sucrose, on bud initiation were evaluated by L₉ (3⁴) orthogonal design. The variance analysis of the experimental results showed that the actions of the three factors were all considerable. Among the three factors, sucrose was the most important for bud initiation followed by BA, and NAA had the weakest effect. The best medium for bud initiation was semi-solid MS supplemented with 2.0 mg l^–1 BA, 0.3 mg l^–1 NAA, 30 g l^–1 sucrose and 0.6 g l^–1 PVP (pH 5.8), on which Chinese aloe could multiply 15 times in 4 weeks. Some shoots rooted spontaneously on 1/2 strength MS medium, but the rooting percentage was improved in the presence of 0.2 mg l^–1 NAA. Rooted plantlets were acclimatized to greenhouse conditions. The young plantlets from tissue culture were transplanted successfully. In vitro propagation can be a useful tool in the conservation of this endangered medicinal species.     

Levan production using mutant strains of Zymomonas mobilis in different culture conditions

Several levan hyperproducing mutants of Zymomonas mobilis strains were selected by mutagenesis with N-methyl-N-nitro-nitrosoguanidine and caffeine. Highest levan production (41 g l^–1) was obtained with a mutant strain HL 29 in a culture medium containing 200 g sucrose l^–1 and 0.5 g (NH₄)₂SO₄ l^–1 stored at 7 °C for 29 days. This is the first report describing the levan synthesis by Z. mobilis at 7 °C.     

Formation of phenylethanoid glycosides by Cistanche deserticola callus grown on solid media

The optimal growth of Cistanche deserticola callus and formation of phenylethanoid glycosides (PeG) was at 25°C with light irradiation intensity of 24 mol m^–2 s^–1 on solidified B5 media supplemented with 0.5 mg 6-benzylaminopurine l^–1, 10 mg gibberellin l^–1, 800 mg casein hydrolysate l^–1 and 20 g sucrose l^–1. After 30 d culture, the biomass reached 15.5 g dry wt callus l^–1 medium and its PEG content was 10.7% (w/w). The PeG content was 42%–127% higher than those in explants.     

Sophorolipid Production with High Yields on Whey Concentrate and Rapeseed Oil without Consumption of Lactose

Sophorolipids were produced by single-step batch cultivation of Candida bombicola ATCC 22214 on deproteinized whey concentrate and repeated feed of rapeseed oil. A mild sterilization method for whey was developed. High yields of 280 g dry sophorolipids l^–1 were obtained from deproteinized whey concentrate containing 100 g lactose l^–1 and 300 g rapeseed oil l^–1. Surprisingly, the whey lactose was not consumed by the organism. Growth only on the oil was assumed and a high lipase activity of 24 U per g cell dry weight resulted.     

A reproducible procedure for plant regeneration from seedling hypocotyl protoplasts of Vigna sublobata L.

Viable protoplasts of Vigna sublobata L. were isolated enzymatically from hypocotyls of axenic seedlings. Protoplast yields were dependent upon seedling age, with maximum yields (2.25 ± 0.35 × 10⁶ g fwt^–1) from seedlings aged 6 d. Protoplasts regenerated cell walls and underwent sustained divisions when cultured in either agarose-solidified or liquid K8P medium. The plating density affected the division frequency and plating efficiency; the division frequency (68 ±0 6.0%) was maximum at 4.0 × 10⁴ ml^–1 while plating efficiency was maximum (1.3 ± 0.1%) at 5.0 × 10⁴ ml^–1. Dividing protoplasts developed into microcalli, which produced glossy green compact nodular calli on transfer to 8.0 gl^–1 w/v agar-solidified medium containing MS salts, B5 organic components, 30 g l^–1 sucrose, NAA (0.2–0.5 mg l^–1), zeatin riboside (0.5–2.0 mg l^–1) and GA₃ (0.5–1.0 mg l^–1). These calli, after sub-culture on the same medium, produced shoot buds which underwent elongation following transfer of tissues to 6.0 g l^–1 agar-solidified B5 medium containing 30g l^–1 sucrose, IBA (0.01 mg l^–1) and BAP (1.0 mg l^–1). Elongated shoots developed roots after transfer to 8.0g l^–1 agar-solidified, hormone-free MS medium with 30 g l^–1 sucrose.Abbreviations IAA indole-3-acetic acid - IBA indole-3-butyric acid - BAP 6-benzyladenine or benzylaminopurine - B5 medium after Gamborg et al (1968) - 2,4-D 2,4-dichlorophenoxyacetic acid - GA³ gibberellic acid - 2,i-P 6-(--dimethylallylamino) purine - MS medium after Murashige and Skoog (1962) - NAA 1-naphthaleneacetic acid     

Invertase production by Aspergillus niger in submerged and solid-state fermentation

Three Aspergillus nigerstrains were grown in submerged and solid state fermentation systems with sucrose at 100 g l^–1. Average measurements of all strains, liquid vs solid were: final biomass (g l^–1), 11 ± 0.3 vs 34 ± 5; maximal enzyme titres (U l^–1) 1180 ± 138 vs 3663 ± 732; enzyme productivity (U l^–1h^–1) 20 ± 2 vs 87 ± 33 and enzyme yields (U/gX) 128 ± 24 vs 138 ± 72. Hence, better productivity in solid-state was due to a better mould growth.     

Exopolysaccharide biosynthesis and related enzyme activities of the medicinal fungus, Ganoderma lucidum, grown on lactose in a bioreactor

Exopolysaccharide (EPS) production and biosynthesis were studied in Ganoderma lucidum, a fungus used in traditional Chinese medicine, grown with lactose in a bioreactor. -Galactosidase activity, which implies the existence of a lactose permease system, was induced by lactose. Lactose feeding also increased -phosphoglucomutase activity and EPS accumulation but decreased phosphoglucose isomerase activity and lactate concentration in the culture broth. A maximum cell density of 22 g l^–1 and EPS at 1.25 g l^–1 were obtained in fed-batch bioreactor culture.