Production of poly-β-hydroxybutyrate by Alcaligenes eutrophus on different carbon sources

Poly--hydroxybutyrate was produced in shake cultures by Alcaligenes eutrophus H16 on fructose, xylose, and fumaric, itaconic, lactic and propionic acids in a three-stage process. The maximum polymer concentration of 6.9 g l^–1 (69% of cell dry matter) was obtained with 20g l^–1 of fructose with a volumetric productivity of about 0.22 g l^–1 h^–1 at 24h. Up to about 3 g l^–1 (about 50% of cell dry matter) of polymer was also produced on lactic and propionic acids as the sole carbon source during the production phase. In multivatiate optimization employing an orthogonal 2³-factorial central composite experimental design with fructose as the substrate in a single-stage process, the optimal initial fructose concentration decreased from 35 g l^–1 to 24 g l^–1 when the incubation time was increased from about 35 h to 96 h. The optimal shaking speed range was 90–113 rpm. Correspondence to: S. Linko     

<Emphasis Type="Italic">Narcissus</Emphasis> bulblet formation <Emphasis Type="Italic">in vitro</Emphasis>: effects of carbohydrate type and osmolarity of the culture medium

Shoot clump cultures of Narcissus cultivars St. Keverne and Hawera were used to investigate the effects of culture medium carbon supply, type of carbohydrate and osmolarity on in vitro bulblet development. Increasing the medium osmolarity using mannitol or sorbitol, which did not act as substrates for growth, failed to stimulate bulblet formation with either cultivar. An exception to this was a relatively small increase in total bulblet dry weight per culture, in the cultivar Hawera only, caused by adding 30 g l ^–1 sorbitol in combination with 30 g l^–1 sucrose. Simultaneously increasing the medium osmolarity and carbon supply using the metabolisable carbohydrate sources, sucrose, glucose, fructose or an equimolar mixture of glucose and fructose stimulated bulblet production, total dry matter accumulation and partitioning into bulblets. At comparable levels of carbon supply up to 19.0 g l^–1, bulblet development of both cultivars was similar with monosaccharide and sucrose media. This indicates that substrate supply is more important for bulblet development than osmolarity of the culture medium. The cultivar Hawera also showed similar responses to monosaccharide and sucrose media supplying 37.9 g C l^–1, despite the high osmolarity of monosaccharide media (c. 650 m Osm kg^–1, equivalent to –1.6 MPa, compared to 380 m Osm kg^–1 for sucrose medium). However in St. Keverne total dry matter accumulation and dry weight per bulblet were further stimulated only by increasing the sucrose supply from 19.0 to 37.9 g C l^–1, not by increasing the monosaccharide supply. Implications of the findings for Narcissus micropropagation are discussed.     

Plant Regeneration from Mesophyll Protoplasts of Echinacea Purpurea

An efficient plant regeneration system was developed from isolated protoplasts of Echinacea purpurea L. using an alginate block/liquid culture system. Viable protoplasts could be routinely isolated from young leaves of Echinacea seedlings in an isolation mixture containing 1.0% cellulase Onozuka R-10, 0.5% pectinase and 0.3 mol l^–1 mannitol. Purified protoplasts were embedded in 0.6% Na-alginate block at a density of 1 × 10⁵/ml and cultured in a modified MS medium containing 0.3 mol l^–1 sucrose, 2.5 µmol l^–1 BA and 5.0 µmol l^–1 2,4-D. Cell colonies were observed after 4 weeks of culture, and the protoplast-derived colonies formed calluses when transferred onto 0.25% gellan gum-solidified MS medium supplemented with 1.0 µmol l^–1 BA and 2.0 µmol l^–1 IBA. Shoot organogenesis from protoplast-derived callus was induced on MS medium supplemented with 5.0 µmol l^–1 BA and 2.0 µmol l^–1 IBA. Complete plantlets were obtained from the regenerated shoots on MS basal medium. The protoplast to plant regeneration protocol developed in this study provides the prerequisite for creating novel genotypes of this valuable medicinal species through genetic manipulation.     

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.     

Age and Physiological Condition of Donor Plants Affect in vitro Morphogenesis in Leaf Explants of Passiflora edulis f. flavicarpa

The regeneration potential of D.alata L. germplasm preserved in vitro was compared with the micropropagation of fresh material. Nodal cuttings were conserved for 9 months in different treatments based on D-571 culture medium modified, using several variable components (mannitol, benzylaminopurine and activated charcoal). Regeneration at 8 weeks, assessed by means of percentage of explant regenerating and the multiplication at 5 weeks through the shoot length and de novo bud count formation per explant were determined. The results showed high rates (100 and 98%) of explant regeneration and micropropagation from in vitro material maintained in D-571 medium with 1.5% of mannitol + 0.1 or 1 mg l^–1 of benzylaminopurine + 2 g l^–1 of activated charcoal, respectively.     

Plant regeneration of rose (Rosa hybridia) from embryogenic cell-derived protoplasts

Culture conditions are described for sustained cell division and plant regeneration from protoplasts of rose (Rosa hybrida L. `Sumpath'). Protoplasts were enzymatically isolated from 2-week-old embryogenic cell suspension cultures. Freshly isolated protoplasts were plated as a thin layer onto protoplast culture medium (half-strength 21 Murashige and Skoog's medium containing 60 g l^–1 myo-inositol, 4.4 M BA, and 1.4 M 2,4-D) at a density of 5×10⁴ protoplasts ml^–1. The plating efficiency reached 3.9% after 2 weeks of culture. However, few protoplasts underwent cell division when cultured in protoplast culture medium in which 60 g l^–1 myo-inositol was replaced with the same osmolarity of 90 g l^–1 mannitol, indicating that myo-inositol is essential for sustained cell division of protoplasts. Colonies were formed after 8 weeks of culture at a frequency of 0.2%. Colonies were then transferred to colony culture medium (0.4% Gelrite-solidified protoplast culture medium) and maintained by subculturing at 4-week intervals to form embryogenic calluses. Upon transfer to half-strength MS basal medium, embryogenic calluses gave rise to numerous somatic embryos. Somatic embryos were transferred to half-strength MS basal medium containing 48 mg l^–1 ferric ethylenediamine di-(o-hydroxyphenylacetate), where they subsequently developed into plantlets at a frequency of 30.9%. The plantlets had the same chromosome number of 2n=3x=21 as the source plant. They were successfully transplanted to potting soil and grown to maturity in a greenhouse.     

Extracellular production of a glycolipid biosurfactant, mannosylerythritol lipid, from Candida antarctica

Candida antarctica (sp. SY16) required avegetable oil as the carbon source to produce a biosurfactant, mannosylerythritol lipid (MEL-SY16). Biosurfactant production was 31 g l^–1 after 7 days in a batch culture and was not growth associated. In a two-stage culture, glycerol and oleic acid were used as an initial and a feeding carbon source, respectively, and 41 g l^–1 biosurfactant was produced after 8 days.     

Production of medium chain length polyhydroxyalkanoates by fed-batch culture of Pseudomonas oleovorans

Pseudomonas oleovorans was cultivated to produce medium chain length polyhydroxyalkanoates (MCL-PHAs) from octanoic acid and ammonium nitrate as carbon and nitrogen source, respectively, by a pH-stat fed-batch culture technique. The octanoate in the culture broth was maintained below 4 g l^–1 by feeding the mixture of octanoic acid and ammonium nitrate when the culture pH rose above 7.1. The final cell concentrations of 63, 55 and 9.5 g l^–1, PHA contents of 62, 75 and 67% of dry cell wt, and productivities of 1, 0.63 and 0.16 g l^–1 h^–1 were obtained when the C/N ratios in the feed were 10, 20 and 100 g octanoic acid g^–1 ammonium nitrate, respectively.     

Ca<Superscript>2+ </Superscript>and Cu<Superscript>2+ </Superscript>supplementation increases mannitol production by <Emphasis Type="Italic">Candida magnoliae</Emphasis>

Supplementation with CaCl₂·2H₂O (50 mg l⁻¹) or CuSO₄·5H₂O (10 mg l⁻¹) improved mannitol production by Candida magnoliae by 14.5 and 18.6% (25 and 32 g/L), respectively. When used in combination, they acted synergistically: Ca²⁺ decreased the intracellular concentration of mannitol 30%, whereas Cu²⁺ increased the intracellular activity of mannitol dehydrogenase 1.6-times more than control. Ca²⁺ probably works by altering the permeability of cells to mannitol, whereas, Cu²⁺ increases the activity of an enzyme responsible for mannitol biosynthesis.     

Selective production of bikaverin in a fluidized bioreactor with immobilized Gibberella fujikuroi

The best culture medium composition for the production of bikaverin by Gibberella fujikuroi in shake-flasks, i.e. 100 g glucose l^–1; 1 g NH₄Cl l^–1; 2 g rice flour l^–1; 5 g KH₂PO₄ l^–1 and 2.5 g MgSO₄ l^–1, was obtained through a fractional factorial design and then scaled-up to a fluidized bioreactor. The effects of carbon and nitrogen concentrations, inoculum size, aeration, flow rate and bead sizes on batch bikaverin production using immobilized G. fujikuroi in a fluidized bioreactor were determined by an orthogonal experimental design. Concentrations of up to 6.83 g bikaverin l^–1 were obtained when the medium contained 100 g glucose l^–1 and 1 g NH₄Cl l^–1 with an inoculum ratio of 10% v/v, an aeration rate of 3 volumes of air per volume of medium min^–1, and a bead size of 3 mm. Based on dry weight, the bikaverin production was 30–100 times larger than found in submerged culture and approximately three times larger than reported for solid substrate fermentation.     

Optimization of glycerol feeding for clavulanic acid production by Streptomyces clavuligerus with glycerol feeding

Glycerol at 10–20 g l^–1 increased clavulanic acid production by Streptomyces clavuligerus in shake-flask culture. The biosynthesis of clavulanic acid continued for longer by feeding glycerol and production increased to 250 mg l^–1 compared with 115 mg l^–1 without feeding. In fermenter batch culture, degradation of clavulanic acid began after 72 h. With glycerol feeding in fed-batch culture, clavulanic acid production was not only increased further to about 280 mg l^–1 but also remained stable up to 130 h.     

Bioconversion of linoleic acid into conjugated linoleic acid during fermentation and by washed cells of Lactobacillus reuteri

Conjugated linoleic acid (CLA) was produced at 300 mg l^–1 after 24 h culture of Lactobacillus reuteri in de Man–Rogosa–Sharpe medium containing 0.9 g linoleic acid (LA) l^–1 and 1.67% (v/v) Tween 80. CLA was mainly located in the extracellular space of the cells. Washed cells previously grown on LA were less active than unadapted washed cells in converting LA into CLA. Most of the CLA transformed by washed L. reuteri cells was located in cells or associated with cells. CLA production by washed L. reuteri cells was most efficient in conversion with 0.45 g LA l^–1 at pH 9.5 and 37°C for 1 h.     

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.     

Impact of carbon and nitrogen nutrition on the quality, yield and composition of blastospores of the bioinsecticidal fungus Paecilomyces fumosoroseus

The impact of growing cultures of Paecilomyces fumosoroseus in liquid media containing four combinations of glucose and casamino acids (8 g l^–1 or 80 g l^–1 glucose, 1.32 g l^–1 or 13.2 g l^–1 casamino acids) was evaluated, based on blastospore production, germination rate, viability after freeze-drying and short-term storage stability. When blastospores were produced using a high casamino acid concentration, blastospore yields and germination rates were significantly higher (13.2–18.5×10⁷ blastospores ml^–1, 50–60% germination after 4 h), compared to cultures grown in media containing lower casamino acid concentrations (0.4–2.3×10⁷ blastospores ml^–1, 10–20% germination after 4 h). Chemical analyses of blastospore composition showed that accelerated blastospore germination may be related to increased proteinaceous reserves rather than to glycogen or lipid accumulation. Tolerance to freeze-drying by blastospores suspended in spent medium was enhanced by a high initial casamino acid concentration in the culture medium (75% survival) and by the residual glucose concentrations in the spent medium. Under the conditions of this study, the storage stability of blastospores of P. fumosoroseus was unaffected by the nutritional condition in which they were produced.     

Plant regeneration from protoplasts isolated from embryogenic suspension cultured cells of Cinnamomum camphora L.

An efficient and reproducible protocol is described for the regeneration of Cinnamomum camphora protoplasts isolated from cultured embryogenic suspension cells. Maximum protoplast yield (13.1±2.1×10⁶/g FW) and viability (91.8±3.8%) were achieved using a mixture of 3% (w/v) cellulase Onozuka R10 and 3% (w/v) macerozyme Onozuka R10 in 12.7% (w/v) mannitol solution containing 0.12% (w/v) MES, 0.36% (w/v) CaCl₂·2H₂O, and 0.011% (w/v) NaH₂PO₄·2H₂O. First divisions occurred 7–10 days following culture initiation. The highest division frequency (24.6±2.9%) and plating efficiency (6.88±0.8%) were obtained in liquid medium (MS) supplemented with 30 g l^–1 sucrose, 0.7M glucose, 0.1 mg l^–1 NAA, 1.0 mg l^–1 BA, and 1.0 mg l^–1 GA₃. After somatic embryo induction and then shoot induction, the protoplast-derived embryos produced plantlets at an efficiency of 17.5%. Somatic embryos developed into well-rooted plants on MS medium supplemented with 1.0 mg l^–1 3-indole butyric acid (IBA). Regenerated plants that transferred to soil have normal morphology.     

High efficiency degradation of tetrahydrofuran (THF) using a membrane bioreactor: identification of THF-degrading cultures of<Emphasis Type="Italic"> Pseudonocardia</Emphasis> sp. strain M1 and<Emphasis Type="Italic"> Rhodococcus ruber</Emphasis> isolate M2

A mixed microbial culture capable of growing aerobically on tetrahydrofuran (THF) as a sole carbon and energy source was used as the inoculum in a 10 l working volume membrane bioreactor. Following start-up, the reactor was operated in batch mode for 24 h and then switched to continuous feed with 100% biomass recycle. On average, greater than 96% of THF fed to the reactor was removed during the 8-month study. THF loading rates ranged from 0.62 to 9.07 g l^–1 day^–1 with a hydraulic retention time of 24 h. THF concentrations as high as 800 mg/l were tolerated by the culture. Biomass production averaged 0.28 kg total suspended solids/kg chemical oxygen demand removed, i.e., comparable to a conventional wastewater treatment process. Periodic batch wasting resulted in a solids retention time of 7–14 days. Reactor biomass typically ranged from 4 to 10 g/l volatile suspended solids and the effluent contained no solids. Pure THF-degrading cultures were isolated from the mixed culture based on morphological characteristics, Gram-staining and THF degradation. Based on 16S rDNA analysis the isolates were identified as Pseudonocardia sp. M1 and Rhodococcus ruber M2.     

The control of in vitro direct main stem formation of Lilium longiflorum derived from receptacle culture, and rapid propagation by using in vitro stem nodes

The control of in vitro direct main stem formation by culturing receptacles, and a protocol for the micropropagation of Lilium longiflorum using in vitro main stem nodes derived from receptacle culture were developed. Receptacles from flowers cultured on MS medium containing 1.0 mg l^–1 gibberellic acid (GA₃) and 0.5 mg l^–1 6-benzyladenine (BA) resulted in direct main stem formation after 3 months culture. These stems were isolated and cut into nodal stem segments, which were then cultured on MS medium supplemented with 0.2 mg l^–1 BA. Shoots formed on each node after one month culture. These shoots were subcultured on MS medium containing 0.5 mg l^–1 BA for their mass propagation. An average of 30 vigorous and uniform shoots were formed per single shoot after each subculture. A cyclic and continuous system of propagation by multiplication of shoots was developed. Shoots were rooted on 1/2 MS medium containing 0.2 mg l^–1-naphthaleneacetic acid (NAA). One hundred plantlets that were acclimatized in the greenhouse had a 100% survival. A comparison was made with the traditional culture of explants derived from bulb-scales and with that from main stems.     

Glycerol production by Candida krusei employing NaCl as an osmoregulator in batch and continuous fermentations

Addition of 40 g NaCl l^–1 to a chemically defined medium containing 140 g glucose l^–1 in shake-flask culture improved glycerol production by Candida krusei from 16.5 g l^–1 to 47.7 g l^–1. With 40 g NaCl l^–1 at a dilution rate of 0.065 h^–1, glycerol concentration, glycerol yield (based on glucose consumed), and productivity in a four-stage cascade bioreactor were higher by 240%, 27% and 28%, respectively, than in a single-stage continuous culture system.     

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.     

Fermentative production of P(3HB-co-3HV) from propionic acid by Alcaligenes eutrophus in fed-batch culture with pH-stat continuous substrate feeding method

The feeding of propionic acid for production of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [P(3HB-co-3HV)] by Alcaligenes eutrophus ATCC17697 was optimized using a fed-batch culture system. The concentration of propionic acid was maintained at 3 g l^–1 as growth was inhibited by propionic acid in the broth. A pH-stat substrate feeding system was used in which propionic acid was fed automatically to maintain a pH of the culture broth at 7.0. By feeding a substrate solution containing 20% (w/v) propionic acid, 4.9% (w/v) ammonia water [at a molar ratio of carbon to nitrogen (C/N molar ratio) of 10] in cell growth phase, the concentration of propionic acid in the broth was maintained at 3 g l^–1 giving a specific growth rate of 0.4 h^–1. To promote P(3HB-co-3HV) production, two stage fed-batch culture which consisted of the stage for the cell growth and the stage for the P(3HB-co-3HV) accumulation was carried out. When the substrate solution whose C/N molar ratio was 50 was fed in P(3HB-co-3HV) accumulation phase, the cell concentration and the P(3HB-co-3HV) content in the cells reached 64 g l^–1 and 58% (w/w) in 55.5 h, respectively.