Purification and in situ immobilization of lipase from of a mutant of Trichosporon laibacchii using aqueous two-phase systems

The crude intracellular lipase (cell homogenate) from Trichosporon laibacchii was subjected to partial purification by aqueous two-phase system (ATPS) and then in situ immobilization by directly adding diatomites as carrier to the top PEG-rich phase of ATPS. A partition study of lipase in the ATPS formed by polyethylene glycol–potassium phosphate has been performed. The influence of system parameters such as molecular weight of PEG, system phase composition and system pH on the partitioning behaviour of lipase was evaluated. The ATPS consisting of PEG 4000 (12%) and potassium phosphate (K₂HPO₄, 13%) resulted in partition of lipase to the PEG-rich phase with partition coefficient 7.61, activity recovery 80.4%, and purification factor of 5.84 at pH of 7.0 and 2.0% NaCl. Moreover, the in situ immobilization of lipase in PEG phase resulted in a highest immobilized lipase activity of 1114.6 U g^?1. The above results show that this novel lipase immobilization procedure which couples ATPS extract and enzyme immobilization is cost-effective as well as time-saving. It could be potentially useful technique for the purification and immobilization of lipase.     

Synthesis and application of two light-sensitive copolymers forming recyclable aqueous two-phase systems

Recycling aqueous two-phase systems (ATPS) are hopeful application techniques in bioseparation and biocatalysis engineering areas. In this study, two novel light-sensitive and reversible water-soluble copolymers were synthesized and used in recycling ATPS. Polymer P_NBAC was polymerized by using N-isopropylacrylamide (NIPA), n-butylmethacrylate (BMA), acrylic acid (AA) and chlorophyllin sodium copper salt (CHL) as monomers. Copolymer P_NDBC was synthesized by NIPA, 2-(dimethylamino) ethylmethacrylate (DMAEMA), BMA and CHL as monomers. The synthesis yields of two copolymers are 66.9% and 77.2%, respectively. It can be calculated from ¹H NMR graph that the molar ratios of monomers in P_NBAC (NIPA:BMA:AA:CHL) and P_NDBC (NIPA:DMAEMA:BMA:CHL) was 82:4:1:10 and 16:4:3:1, respectively. They could be precipitated by laser irradiation in 488 nm with the least light density of 1.70 × 10⁵ W/m². The precipitate energy is 1.79 kJ and 3.52 kJ/g, respectively. Five batches of average recoveries of two copolymers in the ATPS are 96.6% and 97.4%. BSA and l-phenylalanine were partitioned in the novel P_NDBC–P_NBAC ATPS, and their partition coefficients were 2.1 and 0.52. By applying this ATPS to partition of penicillin, the best partition coefficient K is 4.25.     

Two phase partitioning and collagen hydrolysis of bromelain from pineapple peel Nang Lae cultivar

Extraction of bromelain from pineapple peel (Nang Lae cultv.) using aqueous two phase system (ATPS) was optimized. Some biochemical properties including collagen hydrolysis were also investigated. Bromelain predominantly partitioned to the polyethylene glycol (PEG)-rich phase. The highest enzyme activity recovery (113.54%) and purification fold (2.23) were presented in the top phase of 15% PEG2000–14% MgSO₄. Protein pattern and activity staining showed the molecular weight (MW) of bromelain to be about 29 kDa. The extracted bromelain showed the highest relative activity at pH 7.0 and 55 °C. Its activity was decreased continuously by increasing NaCl concentration (up to 1.5% (w/v)). The bromelain extract was applied to hydrolyze the skin collagen of beef and giant catfish (0–0.3 units). The β, α₁, α₂ of giant catfish skin collagen extensively degraded into small peptides when treated with 0.02 units of the bromelain extract. Bovine collagen was hydrolyzed using higher bromelain up to 0.18 units. This study showed the ATPS can be employed to partially purify bromelain from Nang Lae pineapple peel and the enzyme effectively hydrolyzed the collagens.     

Large-scale separation of clavine alkaloids from Ipomoea muricata by pH-zone-refining centrifugal partition chromatography

Centrifugal partition chromatography in the pH-zone-refining mode was successfully applied to the separation of alkaloids, directly from a crude extract of Ipomoea muricata. The experiment was performed with a two-phase solvent system composed of methyl tert-butyl ether (MtBE)–acetonitrile–water (4:1:5, v/v) where triethylamine (10 mM) was added to the upper organic stationary phase as a retainer and trifluoroacetic acid (10 mM) to the aqueous mobile phase as an eluter. From 4 g of crude extract, 210 mg lysergol and 182 mg chanoclavine were obtained in 97% and 79.6% purities. Total yield recovery was >95%. Isolated alkaloids were characterized on the basis of their ¹H, ¹³C NMR and ESI-MS data.     

Comparison of oxygen mass transfer coefficient in simple and extractive fermentation systems

Aeration and agitation are important variables to ensure effective oxygen transfer rate during aerobic bioprocesses; therefore, the knowledge of the volumetric mass transfer coefficient (k_La) is required. In view of selecting the optimum oxygen requirements for extractive fermentation in aqueous two-phase system (ATPS), the k_La values in a typical ATPS medium were compared in this work with those in distilled water and in a simple fermentation medium, in the absence of biomass. Aeration and agitation were selected as the independent variables using a 2² full factorial design. Both variables showed statistically significant effects on k_La, and the highest values of this parameter in both media for simple fermentation (241 s⁻¹) and extractive fermentation with ATPS (70.3 s⁻¹) were observed at the highest levels of aeration (5 vvm) and agitation (1200 rpm). The k_La values were then used to establish mathematical correlations of this response as a function of the process variables. The exponents of the power number (N³D²) and superficial gas velocity (V_s) determined in distilled water (α = 0.39 and β = 0.47, respectively) were in reasonable agreement with the ones reported in the literature for several aqueous systems and close to those determined for a simple fermentation medium (α = 0.38 and β = 0.41). On the other hand, as expected by the increased viscosity in the presence of polyethylene glycol, their values were remarkably higher in a typical medium for extractive fermentation (α = 0.50 and β = 1.0). A reasonable agreement was found between the experimental data of k_La for the three selected systems and the values predicted by the theoretical models, under a wide range of operational conditions.     

Purification of a thermostable laccase from Leucaena leucocephala using a copper alginate entrapment approach and the application of the laccase in dye decolorization

Laccase from a tree legume, Leucaena leucocephala, was purified to homogeneity using a quick two-step procedure: alginate bead entrapment and celite adsorption chromatography. Laccase was purified 110.6-fold with an overall recovery of 51.0% and a specific activity of 58.5 units/mg. The purified laccase was found to be a heterodimer (∼220 kDa), containing two subunits of 100 and 120 kDa. The affinity of laccase was found to be highest for catechol and lowest for hydroquinone, however, highest K_cat and K_cat/K_m were obtained for hydroquinone. Purified laccase exhibited pH and temperature optima of 7.0 and 80 °C, respectively. Mn²⁺, Cd²⁺, Fe²⁺, Cu²⁺ and Na⁺ activated laccase while Ca²⁺ treatment increased laccase activity up to 3 mM, beyond which it inhibited laccase. Co²⁺, Hg²⁺, DTT, SDS and EDTA showed an inhibition of laccase activity. The Leucaena laccase was found to be fairly tolerant to organic solvents; upon exposure for 1 h individually to 50% (v/v) each of ethanol, DMF, DMSO and benzene, more than 50% of the activity was retained, while in the presence of 50% (v/v) each of methanol, isopropanol and chloroform, a 40% residual activity was observed. The purified laccase efficiently decolorized synthetic dyes such as indigocarmine and congo red in the absence of any redox mediator.     

Production of adenoviral vectors and its recovery

The current demands for adenoviral vectors are increasing to satisfy pre-clinical and clinical gene therapy protocols. Consequently, there is a necessity of methodologies to improve production and recovery of intact particles with the minimum effect upon bioactivity. The production of adenoviral vectors in HEK 293 cells and the potential of an alternative aqueous two-phase system (ATPS) composed of PEG 300-phosphate in recovery of adenoviral vectors were investigated. The production of adenoviral vectors was carried out using a 2 L bioreactor equipped with two Rushton impellers. Different parameters including initial cell density, harvesting time and the addition of a buffer (HEPES) were studied in order to improve the production of adenoviral vectors in HEK 293 cells. A yield of 8 × 10¹¹ infective particles was achieved under the conditions characterized by the addition of Pluronic F-68, inoculation at an initial cell density of 3.5 × 10⁵ cells/mL and harvest of infected cells at 48 h post infection (hpi). This material was used for the evaluation of the ATPS recovery processes. It was demonstrated that the chemical components of the ATPS did not have a significant effect upon the infectivity of the adenoviral vectors and a total recovery of approximately 90% was obtained. These findings contribute to the process development for the manufacture of adenoviral vectors and other nanoparticulate bioproducts.     

Biodegradation of microcrystalline cellulose in pH–pH recyclable aqueous two-phase systems with water-soluble immobilized cellulase

Product inhibition is a barrier for enzymatic conversion of cellulose into reducing sugar in single aqueous phase. In addition, the difficulty in the recovery of cellulase also leads to high cost for the enzymatic hydrolysis of cellulose. In this study, enzymatic degradation of cellulose was carried out in pH–pH recyclable aqueous two-phase systems (ATPS) composed by copolymers poly (AA-co-DMAEMA-co-BMA) (abbreviated P_ADB3.8) and poly (MAA-co-DMAEMA-co-BMA) (abbreviated P_MDB). In the systems, cellulase was immobilized on pH-response copolymer P_MDB by using 1-Ethyl-3-(3-dimethyllaminopropyl)-carbodiimide hydrochloride (EDC) as cross-linker. Optimized partition coefficient of product in the systems was 2.45, in the presence of 40 mM (NH₄)₂SO₄. Insoluble substrate and immobilized enzyme were biased to bottom phase, while the product was partitioned to top phase. Microcrystalline cellulose was hydrolyzed into reducing sugar, and the product entered into top phase. The yield of saccharification in ATPS could reach 70.57% at the initial substrate concentration of 0.5% (w/v), and the value was 9.3% higher than that in the single aqueous phase. Saccharification yield could reach 66.15% after immobilized cellulase was recycled five times in ATPS.     

Separation and purification of laccases from two different fungi using aqueous two-phase extraction

Selective purification still poses a challenge in the downstream processing of biomolecules such as proteins and especially enzymes. In this study a polyethylene glycol 3000 (PEG 3000)–phosphate aqueous two-phase system at 25 °C and pH 7 was successfully used for laccase purification and separation. Initially, the effect of phase forming components on enzyme activities in homogenous systems was studied. In the course of the extraction experiments tie lines, enzyme source, initial enzyme activities, phase ratio and sodium chloride concentrations were varied and their influence on the activity partitioning was determined. Partitioning results were validated using clear-native-PAGE and isoelectric focusing. Based on these results, the separation of laccases from Trametes versicolor and Pleurotus sapidus was investigated using the principle of superposition. Sodium chloride was used to adjust laccase partitioning in the applied aqueous two-phase system (ATPS). Finally, two modes of operation are proposed depending on the aim of the purification task. One mode with 0.133 g g⁻¹ of PEG3000, 0.063 g g⁻¹ of phosphate and without sodium chloride separates P. sapidus laccases from T. versicolor laccases with clearance factors of 5.23 and 6.45, respectively. The other mode of operation with 0.124 g g⁻¹ of PEG3000, 0.063 g g⁻¹ of phosphate and 0.013 g g⁻¹ of sodium chloride enables a partitioning of both laccases into the bottom phase of the ATPS resulting in a purification factor of 2.74 and 96% activity recovery.     

Partitioning of protease from stomach of albacore tuna (Thunnus alalunga) by aqueous two-phase systems

Partitioning of protease from stomach of albacore tuna using an aqueous two-phase system (ATPS) was investigated. The best ATPS conditions for protease partitioning from stomach extract (SE) and acidified counterpart (ASE) were 25% PEG1000–20% MgSO₄ and 15% PEG2000–15% MgSO₄, which increased the purity by 7.2-fold and 2.4-fold with the recovered activity of 85.7% and 89.1%, respectively. Electrophoretic study revealed that SE had a major protein with a molecular weight (MW) of 40.6 kDa, while protein with MW of 32.7 kDa was predominant in ASE and ATPS fractions. Pepsinogen in SE might be activated to pepsin by acidification and partitioning process. SE was quite stable at 0 and 4 °C up to 14 days. The loss in protease activity in ASE and selected ATPS fractions was more pronounced when storage time and temperature increased. Therefore, ATPS can be effectively used to recover and purify protease from albacore tuna stomach.     

Physical characterisations of a single-stage Kühni-type aqueous two-phase extraction column

The main parameters which influence the behaviour of phase separation in a single-stage Kühni-type aqueous two-phase extraction column containing polyethylene (PEG) and di-potassium hydrogen phosphate were characterised. Two aqueous two-phase system (ATPS) composed of 12% (w/w) PEG 1450 and 12% (w/w) di-potassium hydrogen phosphate (designated as 12/12) and 12% (w/w) PEG 1450 and 11% (w/w) di-potassium hydrogen phosphate (designated as 12/11) were chosen in this study. The hold-up ɛ_D increased with increasing impeller speeds and mobile phase flow rates. Phase separation for the 12/11 system was slower than that for the 12/12 system, which resulted in higher dispersed phase hold-up values for the 12/11 system. For 12/12 system, mass transfer of plasmid DNA (pDNA) from the dispersed mobile phase to the stationary phase increased rapidly with increasing impeller speeds of 130, 160 and 200 rpm which was reflected in the decreased values for C_T/C_To. The degree of back-mixing quantified by the axial dispersion coefficient D_ax was estimated to be 2.7 × 10⁻⁶ m² s⁻¹.     

Application of TMA-PEG to promote C-phycocyanin extraction from S. platensis in the PEG ATPS

A novel aqueous two phase system (ATPS) using trimethylamine-polyethylene glycols (TMA-PEG) to promote the extraction of C-phycocyanin (C-PC) from S.platensis was introduced. The purity of C-PC (EP) obtained in the ATPS of PEG1000/Na₃PO₄ was increased 2.1 times by the addition of TMA-PEG1000. The purification factor was enhanced from 2.9 to 10.1 when 65% TMA-PEG1000 was added in the system. The ATPS operation must be carried out in the pH range of 6.0-7.0 and at temperatures less than 35 °C for maintaining the stability of C-PC. The partition coefficient and recovery ratio of C-PC increased with the increasing concentration of TMA-PEG. The system parameters like TMA-PEG1000 content, tie line length (TLL), pH, temperature and phase volume ratio (V_r) were screened and optimized using the fractional factorial design and Box-Behnken experiment design. The optimized system is composed of 11.8% PEG1000/TMA-PEG1000 (w/w), 64.42% TMA-PEG1000 (w/w PEG1000) and 9.5% Na₃PO₄ (w/w) with 38.19% TLL (w/w) and 0.89 V_r at pH 6.5 and 25 °C. The obtained value of EP was 5.21 in one-stage ATPS and 6.7 in two-stage ATPS. The recovery ratio of C-PC in the new ATPS extraction system was more than 97%.     

Two-step process for initial capture of plasmid DNA and partial removal of RNA using aqueous two-phase systems

In this paper, a two-step process for initial capture of plasmid DNA (pDNA) and partial removal of RNA using polyethylene glycol (PEG) and di-potassium hydrogen phosphate aqueous two-phase systems (ATPS) has been investigated. A Kühni-type ATPS extraction column was prepared with 50 ml (12% (w/w) PEG 1450, 12% (w/w) phosphate) of stationary phase and loaded with crude mobile phase (26% (w/w) PEG 1450, 4% (w/w) phosphate and 70% (w/w) lysate) at a flow rate of 6 ml min⁻¹ at an impeller speed of 200 rpm. The experiment was terminated after 100 min, and after complete resettling of the phases, 45 ml of stationary phase was harvested. During a subsequent second extraction step contained 18% (w/w) PEG 300 and 14% (w/w) phosphate, a proportion of RNA, which was also concentrated during the column process, was removed. It was demonstrated that the recovery of pDNA in the second bottom phase was 89.4%, which was similar to the initial recovery after column extraction (92.1%).     

Solid-phase extraction of tanshinones from Salvia Miltiorrhiza Bunge using ionic liquid-modified silica sorbents

New ionic liquid-modified silica sorbents were developed by the surface chemical modification of the commercial silica using synthesized ionic liquids. The obtained ionic liquid-modified particles were successfully used as a special sorbent in solid-phase extraction process to isolation of cryptotanshinone, tanshinone I and tanshinone IIA from Salvia Miltiorrhiza Bunge. Different washing and elution solvents such as water, methanol and methanol–acetic acid (90/10, v/v) were evaluated. A comparison of ionic liquid-modified silica cartridges and traditional silica cartridge show that higher recovery was observed using ionic liquid-modified silica sorbents. A quantitative analysis was conducted by high-performance liquid chromatography using a C₁₈ column (5 μm, 150 mm × 4.6 mm) with methanol–water (78:22, v/v, and containing 0.5% acetic acid) as a mobile phase. Good linearity was obtained from 0.5 × 10^?4 to 0.5 mg/mL (r² > 0.999) with the relative standard deviations less than 4.8%.     

Biotransformation of 2-phenylethanol to phenylacetaldehyde in a two-phase fed-batch system

Phenylacetaldehyde (PA) can be produced by the oxidation of 2-phenylethanol (PE) through biotransformation. In order to prevent substrate and product inhibitions and the transformation of the PA to phenylacetic acid (PAA), utilization of a two-phase system is very attractive. Gluconobacter oxydans B-72 was used as the microorganism and iso-octane as the solvent. The effect of initial substrate concentration on the PA production was investigated in single- and two-phase systems. In the single-phase system, substrate inhibition occurred above 5 g/l, and in the two-phase system, above 7.5 g/l. Substrate inhibition kinetics were also studied in the two-phase system and kinetic constants were determined as r_max=0.64 g/l min, K_M=8.15 g/l, K_PA=2.5 g/l. Because it was observed that two-phase system is insufficient to remove the substrate inhibition effect, fed-batch operation was utilised in this study. For 7.5 g/l of PE, 1.65, 3.85, and 7.35 g/l of PA were obtained in the single-phase, two-phase, and two-phase three fed-batch systems, respectively. Effect of biotransformation time, initial substrate concentration, agitation speed, and fed-batch number on the PA production was investigated in a two-phase fed-batch system by the response surface methodology (RSM). The optimum values were found as 3 fed-batch number, 2.75 g/l initial substrate concentration, 150 rpm agitation speed, and 65 min of one batch biotransformation time. In order to verify these results, an experiment was performed at these optimum conditions and 7.10 g/l of PA concentration was obtained.     

Variation in polyphenolic profile and in vitro antioxidant activity of eastern teaberry (Gaultheria procumbens L.) leaves following foliar development

Seasonal dynamics in the polyphenolic composition, antioxidant activity, and their relationships during plant development were evaluated for eastern teaberry (Gaultheria procumbens L.) leaves, a traditional herbal medicine of North American natives. With the complementary UHPLC-PDA-ESI-MS³, HPLC-PDA-fingerprint, Folin-Ciocalteau, and n-butanol/HCl assays of methanol-water (75:25, v/v) extracts, the dried leaf samples harvested monthly across the growing season under Polish climate conditions were found rich in structurally diverse polyphenols (149.2–210.7 mg/g DW) including the dominating salicylates (64.6–107.5 mg/g DW), proanthocyanidins (53.0–66.8 mg/g DW), and flavonoids (17.3–25.3 mg/g DW), and the accompanying chlorogenic acid isomers (2.4–4.4 mg/g DW) and simple phenolic acids (0.9–1.1 mg/g DW). Among 28 detected analytes, gaultherin (64.6–107.5 mg/g DW), miquelianin (14.6–21.1 mg/g DW), procyanidin A-type trimer (5.5–9.5 mg/g DW), and (–)-epicatechin (5.8–7.8 mg/g DW) were the most abundant. The phenolic levels and antioxidant activity parameters in the DPPH (EC₅₀, 15.0–18.2 μg DW/mL; 0.95–1.16 mmol Trolox equivalents/g DW) and FRAP (2.3–3.4 mmol Fe ²⁺/g DW; 0.86–1.26 mmol Trolox equivalents/g DW) assays showed parallel seasonal trends with maxima in September and October. As the subsequent correlation studies confirmed the determinative impact of polyphenols on the leaf antioxidant activity and its seasonal fluctuations, the Fall season could be recommended as optimal for harvesting the plant material for medicinal purposes and cost-effective production of natural health products.     

Determination of mildronate by LC–MS/MS and its application to a pharmacokinetic study in healthy Chinese volunteers

A simple, rapid and accurate liquid chromatography–tandem mass spectrometry (LC–MS/MS) method has been developed and validated for the determination of mildronate in human plasma. Following a simple protein precipitation with methanol, the analyte was separated on a C₁₈ column by isocratic elution with methanol and 10 mM ammonium acetate (55:45; v/v), and then analyzed by mass spectrometry in the positive ion MRM mode. Good linearity was achieved over a wide range of 0.01–20 μg/mL. The intra- and inter-batch precisions (as RSD, %) were less than 7.1%. The average extraction recovery was 87.5%. The method described above has been used, for the first time, to reveal the pharmacokinetics of mildronate injection in healthy subjects. After single intravenously administration of 250, 500 and 1000 mg mildronate, the elimination half-life (t_1/2) were (5.56 ± 1.55), (6.46 ± 1.07) and (6.55 ± 1.17) h, respectively. The Student–Newman–Keuls test results showed that peak plasma concentration (C_max) and the area under the plasma concentration versus time curve from time 0 to 24 h (AUC_0–24) were both linearly related to dose. The pharmacokinetics of mildronate fitted the linear dynamic feature over the dose range studied. The essential pharmacokinetic parameters of multidoses administration intravenously (500 mg, b.i.d) were as follows: t_1/2 was (15.34 ± 3.14) h; C_max was (25.50 ± 3.63) μg/mL; AUC_0–24 was (58.56 ± 5.57) mg h/L. The t_1/2 and AUC of multidoses administration intravenously were different from those of single-dose administration significantly. These findings suggested that accumulation of mildronate in plasma occurred.     

Anaerobic treatment of saline wastewater by Halanaerobium lacusrosei

An upflow anaerobic packed bed reactor was operated continuously with synthetic saline wastewater at different initial COD concentrations (COD₀ = 1900–6300 mg/L), salt concentrations (0–5%, w/v) and hydraulic retention times (θ_H = 11–30 h) to investigate the effect of those operating parameters on COD removal from saline synthetic wastewater. Anaerobic salt tolerant bacteria, Halanaerobium lacusrosei, were used as dominant microbial culture in the process. The percent COD removal reached up to 94% at COD₀ = 1900 mg/L, 19 h hydraulic retention time and 3% salt concentration. No substrate inhibition effect was observed at high feed CODs. Increasing hydraulic retention time from 11 h to 30 h resulted in a substantial improvement in the COD removal from 60% to 84% at around COD₀ = 3400 mg/L and 3% salt concentration. Salt inhibition effect on COD utilization was observed at above 3% salt concentration. Modified Stover–Kincannon model was applied to the experimental data to determine the biokinetic coefficients. Saturation value constant, and maximum utilization rate constant of Stover–Kincannon model for COD were determined as K_B = 5.3 g/L day, U_max = 7.05 g/L day, respectively.     

Isolation and purification of salvianolic acid A and salvianolic acid B from Salvia miltiorrhiza by high-speed counter-current chromatography and comparison of their antioxidant activity

Water-soluble salvianolic acid A (Sal A) and salvianolic acid B (Sal B) were successfully isolated and purified from the crude extract of Salvia miltiorrhiza by high-speed counter-current chromatography (HSCCC). The solvent system was n-hexane–ethyl acetate–methanol–water (3:6:6:10, v/v/v/v). 4.27 mg of Sal A and 32.09 mg of Sal B were obtained from 260 mg of the crude sample. The purities of Sal A and Sal B were 96.67% and 97.43%, respectively. Their structures were identified by ¹H NMR and ¹³C NMR. Antioxidant activities of Sal A and Sal B were also evaluated and compared by the methods of 1,1-diphenyl-2-picrylhydrazyl (DPPH) radical scavenging assay and 2,2-azino-bis-(3-ethylbenzothiazoline-6-sulfonic acid (ABTS⁺) radical cation decolourisation assay. Both Sal A and Sal B showed high radical scavenging activities with their EC₅₀ values being 1.43 ± 0.09 and 1.81 ± 0.01 μg/ml in DPPH radical method. The ABTS results showed that Sal A and Sal B exhibited high total antioxidant activities, their EC₅₀ values were 1.35 ± 0.00 and 1.43 ± 0.01 μg/ml, respectively.     

Culture parameters affecting xylitol production by Debaryomyces hansenii immobilized in alginate beads

Yeast immobilization offers operational advantages such as high cell concentration, and some drawbacks related to cell leaking and restricted mass transfer inside particles. The influence of bead size, chitosan, bead charge, volume of liquid media, and the use of corncob hydrolyzates and vinasses as culture medium were analyzed on xylitol production by Debaryomyces hansenii immobilized in alginate beads. The results showed a profuse growth of free cells, accounting 75–95% of total biomass, but electron micrographs revealed the generation of a dense biofilm with hyphal morphology at the bead surface and a very low intraparticular growth. Xylitol production was not affected by the size of particle; however chitosan had a negative effect. The use of corn cob as carbon source and twofold diluted vinasses as economic nutrients incremented xylitol concentration to 13.7 g L^?1 (Y_P/S = 0.56 g g^?1; Q_P = 0.29 g L^?1 h^?1). The best conditions corresponded to high bead charges and intermediate liquid volumes (44 g Na-alginate and 110 mL liquid medium). These results showed the feasibility of employing these cheap substrates, reflected the importance of the microaerobical conditions, and pointed to the favorable effect of cell immobilization on the metabolism of xylitol production.