Invertase embedded-PVC tubing as a flow-through reactor aimed at conversion of sucrose into inverted sugar

A simple flow-through reactor system is prepared by covalent linking of a biomolecule on the inner surface of a polyvinyl chloride (PVC) tube. This is achieved by introducing an active functional group on the surface of an inert PVC tube through 1-fluoro-2-nitro-4-azidobenzene (FNAB), a precursor of highly reactive nitrene, which can insert to any C–H bond. CCl₄ lacking C–H bond is taken as a solvent for loading FNAB solution into the tube. FNAB loaded tube is then allowed to expose to sunlight for 20 min during which azido group of FNAB generates nitrene and attaches itself to PVC tube through insertion reaction. Invertase is immobilized in the activated PVC tube at 50 °C in 45 min. Invertase embedded-PVC tube is used as a flow-through reactor to convert sucrose to invert sugar. The flow-through reactor converted sucrose into invert sugar with 97% yield as shown by HPLC analysis. The reactor is reused for eight cycles with 17% loss of its initial activity. The reactor system is cheap as PVC tube is working both as a carrier of biomolecule and a reaction vessel. This reactor system overcomes the problem of back pressure and can be used for any enzymatic conversion in a flow-through system.     

Effect of deglycosylation on the properties of thermophilic invertase purified from the yeast Candida guilliermondii MpIIIa

Invertase from Candida guilliermondii MpIIIa was purified and biochemically characterized. The purified enzyme (INV3a-N) is a glycoprotein with a carbohydrate composition comprising nearly 74% of its total molecular weight (MW) and specific activity of 82,027 U/mg of protein. The enzyme displayed optimal activity at pH 5.0 and 65 ˚C. The Km and V_max values for INV3a-N were 0.104 mM and 10.9 μmol/min/mg of protein, respectively, using sucrose as the substrate. The enzyme retained 50% and 20% of its maximal activity after 168 h and 30 days, respectively, at 50 ˚C. INV3a-N was fully active at sucrose concentrations of 400 mM and the activity of the enzyme dropped slowly at higher substrate concentration. Interestingly, the deglycosylated form of INV3a-N (INV3a-D) displayed 76–92% lower thermostability than that of INV3a-N at all temperatures assayed (50–70 ˚C), and was inhibited at sucrose concentrations of 200 mM. Findings here indicate glycosylation plays an important role, not only in the thermostability of INV3a-N, but also in the inhibition of the enzyme by sucrose. Since the enzyme is active at high sucrose concentrations, INV3a-N may be considered a suitable candidate for numerous industrial applications involving substrates with high sugar content or for improvement of ethanol production from cane molasses.     

Dilute sulfuric acid cycle spray flow-through pretreatment of corn stover for enhancement of sugar recovery

A cycle spray flow-through reactor was designed and used to pretreat corn stover in dilute sulfuric acid medium. The dilute sulfuric acid cycle spray flow-through (DCF) process enhanced xylose sugar yields and cellulose digestibility while increasing the removal of lignin. Within the DCF system, the xylose sugar yields of 90–93% could be achieved for corn stover pretreated with 2% (w/v) dilute sulfuric acid at 95 °C during the optimal reaction time (90 min). The remaining solid residue exhibited enzymatic digestibility of 90–95% with cellulase loading of 60 FPU/g glucan that was due to the effective lignin removal (70–75%) in this process. Compared with flow-through and compress-hot water pretreatment process, the DCF method produces a higher sugar concentration and higher xylose monomer yield. The novel DCF process provides a feasible approach for lignocellulosic material pretreatment.     

Production of isomaltulose using Erwinia sp. D12 cells: Culture medium optimization and cell immobilization in alginate

Isomaltulose is a structural isomer of sucrose commercially used in food industries. Glucosyltransferase produced by Erwinia sp. D12 catalyses an intramolecular transglucosylation of sucrose giving isomaltulose. An experimental Design and Response Surface Methodology were applied for the optimization of the nutrient concentration in the culture medium for enzyme production in shaken flasks at 200 rpm and 30 °C. A higher production of glucosyltransferase (7.47 Uml⁻¹) was observed in the culture medium containing sugar cane molasses (160 gl⁻¹), bacteriological peptone (20 gl⁻¹) and yeast extract Prodex Lac SD^® (15 gl⁻¹) after 8 h, at 30 °C. The highest production of glucosyltransferase in the 6.6-l bioreactor (14.6 Uml⁻¹) was obtained in the optimized culture medium after 10 h at 26 °C. When Erwinia sp. D12 cells were immobilized in sodium alginate, it was verified that sodium alginate solution A could be substituted by a cheaper one, sodium alginate solution B. Using a 40% cell suspension and 2% sodium alginate solution B for cell immobilization in a packed-bed reactor, 64.1% conversion of sucrose to isomaltulose was obtained. The packed-bed reactor with immobilized cells plus glutaraldehyde and polyethylenimine solutions remained in a pseudo-steady-state for 180 h.     

Succinic acid production from sucrose and molasses by metabolically engineered E. coli using a cell surface display system

To achieve sucrose-metabolizing capability, different sucrose utilization operons have been introduced into E. coli that cannot utilize sucrose. However, these engineered strains still suffer from low growth rates and low sucrose uptake rates. In this study, cell surface display system was adopted in engineered E. coli AFP111 for succinic acid production from sucrose and molasses directly. Invertase (CscA) from E. coli W was successfully anchored to outer membrane by fusion with OmpC anchoring motif, and the displayed CscA showed high extracellular activity. Compared with the sucrose permease system, the cell surface display system consumed less ATP during sucrose metabolism. When less ATP was consumed by AFP111/pTrcC-cscA, the succinic acid productivity from sucrose was 23% higher than that by AFP111/pCR2.1-cscBKA that having the sucrose permease system. As a result, 41 g L⁻¹ and 36.3 g L⁻¹ succinic acid were produced by AFP111/pTrcC-cscA from sucrose and sugarcane molasses respectively at 34 h in 3-L fermentor during dual-phase fermentation. In addition, 79 g L⁻¹ succinic acid was accumulated with recovered AFP111/pTrcC-cscA cells at the end of dual-phase fermentation in 3-L fermentor, and the overall yield was 1.19 mol mol⁻¹ hexose.     

Sugar gustatory thresholds and sugar selection in two species of Neotropical nectar-eating bats

Nectar-feeding bats play an important role in natural communities acting as pollinators; however, the characteristics that affect their food selection are unclear. Here we explore the role that sugar gustatory thresholds and sugar concentration play on sugar selection of Glossophaga soricina and Leptonycteris yerbabuenae. We offered bats paired feeders containing sugar solutions of sucrose (S), glucose (G) or fructose (F) vs. pure water, and sucrose vs. 1:1 equicaloric solutions of glucose–fructose at 5, 15 and 35% (wt./vol.). To see the effect of sweetness on sugar selection, we habituated the bats with a diet containing either sucrose or hexoses and subsequently evaluated sugar preferences. Sugar thresholds were S < G,F for G. soricina and G < S < F for L. yerbabuenae. These thresholds did not match with sugar preferences when the bats fed on dilute nectars. L. yerbabuenae changed its sugar preferences with concentration while G. soricina did not. Finally, the bats consistently preferred the sugar they were habituated to. Our results suggest that bats become accustomed to the sugar found in the most abundant plants they use, and thus prefer the most common sugars included in their diet. This could confer an advantage by allowing them shifting sugar preferences on the most common food present in their environment.     

Ozone effects on carbon metabolism in sensitive and insensitive Phaseolus cultivars

An ozone treatment of 165 nL L^?1 for 3 h evoked differential responses in the primary leaves of two bean cultivars of the common bean (Phaseolus vulgaris L.). While cv ‘Cannellino’ showed visible symptoms of injury within 24 h of exposure, no visible symptoms at all were evident in the cv ‘Top Crop’. In primary leaves of the sensitive cultivar Cannellino, we observed an increase in carbon breakdown (an increase in PFK and Fumarase) and a reduction in CO₂ photoassimilation, linked also to the diminished synthesis of sucrose (a decrease in SPS activity) and to the stimulation of the degradation of this sugar (an increase in SuSy and Invertase activities). A strong stimulation of PEPcase activity indicates both an increased synthesis of OAA and an enhanced replenishment of the tricarboxylic acid cycle. Finally, in Cannellino leaves the activity of NADP-malic enzyme increased indicating a stimulation of enzymes delivering NADPH. The findings of this research suggest that the visible symptoms in Cannellino represent an active response that this cultivar initiates to cope with excess oxidative load. The pattern in Top Crop was different. This cultivar did not show visible symptoms of injury, nor any responsive changes at the physiological and biochemical levels. Oxidative pathways are partially enhanced, e.g., increases in Invertase, PFK and IDH. There were also increases in some enzyme linked to the production of cytosolic NADPH as G6PD, probably caused by the slight increase in activity of the enzymes SKDH and PAL involved in synthesis of phenolic compounds. However, the absence of visible injury in Top Crop leaves is confirmation that, in this cultivar, the need to produce carbon skeleton and NADPH used in detoxification and repair process is lower.     

Enhanced ethanol production by continuous fermentation in a two-tank system with cell recycling

An experimental method for producing ethanol continuously was designed and tested with a cell-recycling two-tank system, which was composed of two fermentors, each of which was individually equipped with a settler for recycling flocculent yeast. This system was effective for the continuous fermentation of ethanol from sucrose at high cell-recycling (r = 0.8–0.9) and dilution (up to 0.48 h^?1) rates. The system has several advantages; the high cell concentration in the fermentors and relief of substrate and product inhibition. Thus, the enhanced productivity using this continuous fermentation with the two-tank cell-recycling system was significantly higher compared with that of the batch fermentation. The results indicate that increased recycling ratios caused an increase in biomass concentration and subsequently, product concentration in the tank. The ethanol productivity increased with the dilution rate, but higher dilution rates could render increasing amounts of sugar unconverted. Continuous fermentation with the sugar feed concentration of 160 g/l at r = 0.9 and dilution rate of 0.2 h^?1 achieved the highest productivity with less than 2% of the unconverted sugar in the product steam. Under the same cell recycling ratios a productivity range of 6.9–7.5 g/l h^?1 could be achieved with feeding concentrations of 80–200 g/l, while batch fermentation at these sugar concentrations led to productivities of 3.85–4.48 g/l h^?1.     

Microencapsulating aerial conidia of Trichoderma harzianum through spray drying at elevated temperatures

Conidia of Trichoderma harzianum produced from either solid or liquid fermentation must be dried to prevent spoilage by microbial contamination, and to induce dormancy for formulation development and prolonged self-life. Drying conidia of Trichoderma spp. in large scale production remains the major constraint because conidia lose viability during the drying process at elevated temperatures. Moreover, caking must be avoided during drying because heat generated by milling conidial chunks will kill conidia. It is ideal to dry conidia into a flow-able powder for further formulation development. A method was developed for microencapsulation of Trichoderma conidia with sugar through spray drying. Microencapsulation with sugars, such as sucrose, molasses or glycerol, significantly (P < 0.05) increased the survival percentages of conidia after drying. Microencapsulation of conidia with 2% sucrose solution resulted in the highest survival percentage when compared with other sucrose concentrations and had about 7.5 × 10¹⁰ cfu in each gram of dried conidia, and 3.4 mg of sucrose added to each gram of dried conidia. The optimal inlet/outlet temperature setting was 60/31 °C for spray drying and microencapsulation. The particle size of microencapsulated conidia balls ranged from 10 to 25 μm. The spray dried biomass of T. harzianum was a flow-able powder with over 99% conidia, which could be used in a variety of formulation developments from seed coatings to sprayable formulations.     

Functional characterization of the sucrose isomerase responsible for trehalulose production in plant-associated Pectobacterium species

Fifty-three plant-associated microorganisms were investigated for their ability to convert sucrose to its isomers. These microorganisms included one Dickeya zeae isolate and 7 Enterobacter, 3 Pantoea, and 43 Pectobacterium species. Eleven out of the 53 strains (21%) showed the ability to transform sucrose to isomaltulose and trehalulose. Among those, Pectobacterium carotovorum KKH 3-1 showed the highest bioconversion yield (97.4%) from sucrose to its isomers. In this strain, the addition of up to 14% sucrose in the medium enhanced sucrose isomerase (SIase) production. The SIase activity at 14% sucrose (47.6 U/mg dcw) was about 3.6-fold higher than that of the negative control (13.3 U/mg dcw at 0% sucrose). The gene encoding SIase, which is comprised a 1776 bp open reading frame (ORF) encoding 591 amino acids, was cloned from P. carotovorum KKH 3-1 and expressed in Escherichia coli. The recombinant SIase (PCSI) was shown to have optimum activity at pH 6.0 and 40 °C. The reaction temperature significantly affected the ratio of sucrose isomers produced by PCSI. The amount of trehalulose increased from 47.5% to 79.1% as temperature was lowered from 50 °C to 30 °C, implying that SIase activity can be controlled by reaction temperature.     

Comparison of CSTR and UASB reactor configuration for the treatment of sulfate rich wastewaters under acidifying conditions

The effects of lowering the operational pH from 6 to 5 on mesophilic (30 °C) sulfate reduction during the acidification of sucrose at an organic loading rate of 5 gCOD (l_reactor d)⁻¹ and at a COD/SO₄²⁻ ratio of 4 were evaluated in a CSTR and in a UASB reactor. The HRT was 24 h and 10 h, respectively. Acidification was complete in both reactors at pH 6 and the lowering of the operational pH to 5 did not affect the acidification efficiency in the CSTR but decreased the acidification efficiency of the UASB to 72%. The decrease to pH 5 caused an increase in the effluent butyrate and ethanol concentrations in both reactors. Lowering the pH from 6 to 5 caused a decrease in sulfate reduction efficiencies in both reactors, from 43% to 25% in the CSTR and from 95% to 34% in the UASB reactor. The acidification and sulfate reduction efficiencies at pH 5 could be increased to 94% and 67%, respectively, by increasing the HRT of the UASB reactor to 24 h.     

Processing characteristics of submerged fermentation of Antrodia cinnamomea in airlift bioreactor

Three 5-L airlift bioreactors including airlift reactor with solid draft tube (ALs), airlift reactor with net draft tube (ALn) and bubble column reactor (BC) were investigated for their suitability for cultivating Antrodia cinnamomea, and a stirred tank reactor (ST) was used for comparison. Results indicated that after 7 days fermentation, ALs yielded the highest mycelium content (313 mg/100 mL) and had the lowest dissolved oxygen in the broth. Among different aeration rates (0.025, 0.05, 0.1, 0.5, 1 vvm) used during cultivation of A. cinnamomea in ALs, the aeration rate 0.1 vvm resulted in a volumetric oxygen transfer coefficient of 10.8 h⁻¹ and produced the highest mycelium content. When the optimal conditions were used for the fermentation of A. cinnamomea in an industrial 500-L ALs, the mycelium content in the broth reached 542 mg/100 mL in 28 days. The IC₅₀ values of the ethanol extracts of A. cinnamomea mycelium cultivated in 5-L and 500-L ALs for 28 days were 23 and 17 μg/mL, respectively, for hepatocellular carcinoma cells HepG2. And after 42 days cultivation in 500-L ALs, the IC₅₀ value of the mycelium ethanol extract was reduced to 10 μg/mL.     

Palatinose production by free and Ca-alginate gel immobilized cells of Erwinia sp.

Palatinose is a non-cariogenic disaccharide obtained from the enzymatic conversion of sucrose, used in food industries as a sugar substitute. Free and Ca-alginate immobilized cells of Erwinia sp. D12 were used to produce palatinose from sucrose. Palatinose production was studied in a repeated-batch process using different immobilized biocatalysts: whole cells, disrupted cells and glucosyltransferase. Successive batches were treated with the immobilized biocatalyst, but a decrease in palatinose production was observed. A continuous process using a packed-bed reactor was investigated, and found to produce 55–66% of palatinose during 17 days using immobilized cells treated with glutaraldehyde and a substrate flow speed of 0.56 ml min⁻¹. However, immobilized cells in a packed-bed reactor failed to maintain the palatinose production for a prolonged period. The free cells showed a high conversion rate using batch fermentation, obtaining a palatinose yield of 77%. The cells remained viable for 16 cycles with high palatinose yields (65–77%). Free Erwinia sp. D12 cells supported high production levels in repeated-batch operations, and the results showed the potential for repeated reuse.     

Sugar concentration and timing of feeding affect feeding characteristics and survival of a parasitic wasp

The availability of food sources is important for parasitoid survival, especially for those that inhabit ecosystems where nectar and honeydew are spatially or temporally scarce. Therefore, the value of even a single meal can be crucial for survival. Psyttalia lounsburyi is a parasitoid, and biological control agent, of the olive fruit fly, Bactrocera oleae. In order to improve our understanding of the basic nutritional ecology of P. lounsburyi and its role in survival we evaluated the effect of a single sucrose meal on the longevity of female and male wasps. We measured the duration of feeding, volume ingested, sucrose consumption, energy content, and longevity of wasps provided with different concentrations of sucrose (0.5, 1, and 2 M) at different times after emergence (0, 1, 2 or 3 days after emergence). Our results showed that longevity was significantly influenced by sucrose concentration and timing of feeding. For females, feeding on sucrose increased the likelihood of survival to varying degrees, ranging from 32.3% to 95.4%, compared to water-only controls. The longest duration of feeding was observed for the highest sucrose concentrations and oldest wasps. The amount of sugar ingested and energy uptake increased, up to a point, as sugar concentration increased. Our results suggest that P. lounsburyi derived greatest benefit from the intermediate concentration (1 M) of sucrose provided 2 or 3 days after emergence. Our study emphasizes the importance of finding balance between increasing longevity and limiting the duration of feeding, and concomitant uptake of nutrients, that is fundamental for survival of the wasp in nature.     

Combined industrial and domestic wastewater treatment by periodic allocating water hybrid hydrolysis acidification reactor followed by SBR

A pilot-scale hybrid hydrolysis acidification reactor (HHAR) with periodic water allocation mode operation followed by sequencing batch reactor (SBR) in anoxic and aerobic metabolic function was evaluated for the treatment of low-biodegradable combined industrial and domestic wastewater. The HHAR combines the advantages of both the UASB reactor and AF, omitting the three-phase separator. Furthermore, it has lower average up-flow velocity (0.38–0.92 m/h) and higher periodic up-flow velocity (6 m/h), which made the reactor keep higher MLSS concentration (more than 10,000 mg/L) and sludge-bed is in periodic “expansion-sedimentation-expansion” state. When HRT less than 10 h, the B/C variation was positive and reached the maximum value of 0.07 at 8 h. SBR with a total cycle period of 4.5 h was applied as the post-treatment process to remove residual COD, NH₃-N and TN. At steady stage, the pilot-scale SBR effluent COD, NH₃-N and TN concentration was 65, 0.75 and 17.71 mg/L, corresponding in this case to full-scale SBR plant effluent was 93, 16.4 and 34 mg/L. Comparison results indicated that the application of HHAR–SBR system to treat combined industrial and domestic wastewater can improve effluent quality significantly.     

Production of β-fructofuranosidases by Aspergillus niveus using agroindustrial residues as carbon sources: Characterization of an intracellular enzyme accumulated in the presence of glucose

The production of β-fructofuranosidases by Aspergillus niveus, cultivated under submerged fermentation using agroindustrial residues, was investigated. The highest productivity of β-fructofuranosidases was obtained in Khanna medium supplemented with sugar cane bagasse as carbon source. Glucose enhanced the production of the intracellular enzyme, whereas that of the extracellular one was decreased. The intracellular β-fructofuranosidase was a trimeric protein of approximately 141 kDa (gel filtration) with 53.5% carbohydrate content, composed of 57 kDa monomers (SDS-PAGE). The optimum temperature and optimum pH were 60 °C and 4.5, respectively. The purified enzyme showed good thermal stability and exhibited a half-life of 53 min at 60 °C. β-Fructofuranosidase activity was slightly activated by Cu²⁺, Mn²⁺, Mg²⁺, and Na⁺ at 1 mM concentration. The enzyme hydrolyzed sucrose, raffinose, and inulin, with K_d values of 5.78 mM, 5.74 mM, and 1.74 mM, respectively.     

Production of di-d-fructofranosyl-2,6′:2′,6-anhydride (DFA IV) by recombinant Bacillus subtilis carrying heterogenous levan fructotransferase from Arthrobacter nicotinovorans GS-9

We developed di-d-fructofranosyl-2,6′:2′,6-anhydride (DFA IV) production system with single culture of Bacillus subtilis directly from sucrose. This system can avoid the purification procedure of levan which organic solvent was used for precipitation. The levan fructotransferase (LFTase) gene was cloned from Arthrobacter nicotinovorans GS-9 (AHU1840, FERM P-15285) and expressed in levan producing B. subtilis 168. LFTase activity was detected in the culture supernatant of the transformant with maximal activity of 0.062 U/ml after 15.5 h post induction. Then sucrose was added as substrate and incubated. About 78 h after addition of sucrose, 20.5 g/l of DFA IV was produced from 139.3 g/l of sucrose consumed. The yield of DFA IV from sucrose was 14.7 wt.%.     

A recombinant levansucrase from Bacillus licheniformis 8-37-0-1 catalyzes versatile transfructosylation reactions

This work disclosed the broad transglycosylation capability of the levansucrase from Bacillus licheniformis 8-37-0-1 for the first time. The levansucrase was firstly purified from the strain 8-37-0-1 and found to be a monomer of ∼51 kDa with KETQDYKKSY as the N-terminus. Then, the gene encoding the enzyme was cloned and it contained an ORF of 1449 nucleotides, encoding a 482 amino-acid protein with a predicted 29 amino-acid signal peptide. The deduced mature protein without the signal showed the same N-terminus to the purified enzyme. The mature enzyme was subsequently expressed in Escherichia coli. The recombinant enzyme showed similar biochemical properties to the native one. It produced maximal yield of 7.1 mg/mL levan (M_r 9.6 × 10⁶) from 0.8 M sucrose (pH 6.5) at 40 °C for 24 h in vitro. When using sucrose as the donor, the enzyme displayed a wide range of acceptor specificity and was able to transfer fructosyl to a series of sugar acceptors including hexose, pentose, β- or α-disaccharides, along with the difficult branched alcohols that have not been investigated before. Chemical structures of the resultant products were analyzed by MS and NMR spectra.     

Chiral porphyrin complexes of cobalt(II) and ruthenium(II) in catalytic cyclopropanation and amination reactions

We report here the syntheses of two new metal complexes (M = Co, 2; M = Ru, 3) of the chiral porphyrin TmyrtP (1) (TmyrtP = dianion of the meso-tetrakis[(1R)-apopinen-2-yl]porphyrin). Both complexes exist as a mixture of atropisomers. Complexes 2 and 3 activate aromatic azides for the amination under mild conditions of unsaturated hydrocarbons. Even though the observed ee values are low, this is the first asymmetric transfer of the nitrene residue of aryl azides to a prochiral olefin catalyzed by a transition metal complex to be reported in the literature. Complex 3 also showed a good catalytic activity in cyclopropanation reactions with ethyldiazoacetate even at low temperatures (−30 °C) but a poor diastereo- and enantioselectivity were observed.     

Operation of a fixed-bed bioreactor in batch and fed-batch modes for production of inulinase by solid-state fermentation

This work is focused on the inulinase production by solid-state fermentation (SSF) in a fixed-bed reactor (34 cm diameter and 50 cm height) with working capacity of 2-kg of dry substrate operated in batch and fed-batch modes. It was investigated different strategies for feeding the inlet air in the bioreactor (saturated and unsaturated air) as alternative to remove the metabolic heat generated during the microbial growth by evaporative cooling. The kinetic evaluation of the process carried out in batch mode using unsaturated air showed that the evaporative cooling decreasing the mean temperature of the solid-bed, although the enzyme production was lower than that obtained using saturated air. Results showed that maximum enzyme activity (586 ± 63 U gds⁻¹) was obtained in the fed-batch mode using saturated air after 24 h of fermentation. The enzymatic extract obtained by fed-batch mode was characterized and presented optimum temperature and pH in the range of 52–57 °C and 4.8–5.2, respectively. For a temperature range from 40 to 70 °C the enzyme presented decimal reduction time, D-value, ranging from 5748 to 47 h, respectively. For a pH range from 3.5 to 5.5 the enzyme showed good stability, presenting D-values higher than 2622 h. In terms of Michaelis–Mentem parameters were demonstrated that the crude inulinase activity presented higher affinity for substrate sucrose compared to inulin.