Studies on the Water-Insoluble Enzyme

Water-insoluble yeast invertase was prepared by binding native invertase to DEAE-cellulose. Some characteristics of the bound invertase and the continuous hydrolysis of sucrose by use of it are described. The activity of bound invertase corresponded to about 1/2 at pH 3.4 when compared with the maximum activity of free form and it could hydrolyze sucrose into invert sugar perfectly. The apparent optimum pH of bound invertase was shifted toward acid pH by about 2 pH units in comparison with free invertase. Stability of bound invertase to temperature was slightly less in comparison with free invertase at pH 5.2. The continuous sucrose hydrolysis was carried out using bound invertase at pH 3.6 and it could be used about ten times until the hydrolysis ratio decreased to the half of the initial.     

Immobilization of cane invertase on bentonite

Sugar-cane invertase (β-d-fructofuranoside fructohydrolase, EC 3.2.1.26) immobilized on bentonite clay in 0.05 m acetate buffer, pH 4.5, has been shown to be capable of hydrolysing sucrose. The bentonite-invertase (BI) complex gave 55.5% retention of enzyme activity on the surface. A further 17 and 22% increase in retention of enzyme activity was obtained using the covalent linking agents, cyanuric chloride and thionyl chloride, giving bentonite-cyanuric chloride-invertase (BCCI) and bentonite-thionyl chloride-invertase (BTCI) complexes. Concentrations of acetate buffer >0.2 M disrupt the bentonite-invertase complexes. The immobilized invertase complexes showed high temperature optima (60–65°C) and high thermal stability compared to the free enzyme. The pH profiles of the free and immobilized enzyme were the same. The rate of hydrolysis of sucrose was increased using immobilized enzymes, which required a higher substrate concentration than the free enzyme. The insoluble enzyme conjugate-carrier complexes when used for sucrose hydrolysis in a batch process showed 53.1 (BI), 57.4 (BCCI) and 59.6% (BTCI) conversions, respectively, in 12 h, compared to 42.3% conversion in 24 h with the free enzyme. The immobilized invertase complexes can be used for sucrose inversion for about five cycles. The application of this immobilization procedure may help in the removal of invertase from cane juice to reduce sugar losses in industry.     

Conversion of cellobiose to glucose using immobilized β-glucosidase reactors

Cellobiose is an intermediate in the enzymatic hydrolysis of cellulose to glucose and acts as an inhibitor for the cellulase enzymes. The conversion of cellobiose to glucose was studied with β-glucosidase adsorbed on Amberlite DP-1, a cation-exchange resin. The best overall pH for adsorption and reactor operation was near 5.0. The K_m values increased with increasing enzyme loading due to competitive inhibition. The maximum practical enzyme loading was about 28 units/g resin. The immobilized enzyme was operated continously in both packed bed and fluidized bed reactors, giving half-lives between 200 and 375 h.     

Tris–sucrose buffer system: a new specially designed medium for extracellular invertase production by immobilized cells of isolated yeast Cryptococcus laurentii MT-61

The aims of the present study were to isolate new yeasts with high extracellular (exo) invertase activity and to investigate the usability of buffer systems as invertase production media by immobilized yeast cells. Among 70 yeast isolates, Cryptococcus laurentii MT-61 had the highest exo-invertase activity. Immobilization of yeast cells was performed using sodium alginate. Higher exo-invertase activity for immobilized cells was achieved in tris–sucrose buffer system (TSBS) compared to sodium acetate buffer system and potassium phosphate buffer system. TSBS was prepared by dissolving 30 g of sucrose in 1 L of tris buffer solution. The optimum pH, temperature, and incubation time for invertase production with immobilized cells were determined as 8.0, 35 °C and 36 h in TSBS, respectively. Under optimized conditions, maximum exo-invertase activity was found to be 28.4 U/mL in sterile and nonsterile TSBS. Immobilized cells could be reused in 14 and 12 successive cycles in sterile and nonsterile TSBS without any loss in the maximum invertase activity, respectively. This is the first report which showed that immobilized microbial cells could be used as a biocatalyst for exo-invertase production in buffer system. As an additional contribution, a new yeast strain with high invertase activity was isolated.     

Properties and use of invertase entrapped in fibers

Invertase was entrapped in cellulose triacetate fibers and the properties of the insoluble derivative were studied. Fiber-entrapped invertase was found very stable under operating conditions. For some insoluble preparations a half-life value of 5,300 days was calculated; a sample of invertase fibers, continuously hydrolyzing sucrose, maintained unchanged its activity for five years. The activity displayed by invertase fibers was 15–65% of that of the free enzyme, depending on the amount of entrapped enzyme and on the porosity of the fibers. At very high substrate concentrations the activity of the entrapped invertase approximated to that of the free enzyme. The pH optimum for activity was around 4.5 for the free and entrapped invertase. The native and entrapped enzyme was unstable at temperatures higher than 35°C. The continuous hydrolysis of sucrose using invertase fiber was studied and the potential industrial application of entrapped enzyme is discussed.     

Hydrolysis of concentrated sucrose syrups by invertase immobilized on anion exchanger waste cotton thread.

Yeast invertase was immobilized on polyethyleneimine-coated cotton thread by adsorption followed by crosslinking with glutaraldehyde. The thread-bound invertase was used as an easily retrievable system for the hydrolysis of 80% w/v commercial sucrose syrups. The immobilized enzyme was stable for over 90 days to a temperature of 50 degrees C, only when stored in 80% sucrose solution. Above this temperature, inactivation of enzyme was observed. The cotton threads were used in a batch reactor for hydrolysis of sucrose in about 30 batches carried out over a period of 50 days without loss in activity. The threads could also be used in a packed bed reactor (1.51) for 97% hydrolysis of 80% sucrose syrups at 50 degrees C at a rate of about 360 kg per month for a period of 3 months.     

Characterization of the co-purified invertase and β-glucosidase of a multifunctional extract from Aspergillus terreus

The filamentous fungus Aspergillus terreus secretes both invertase and β-glucosidase when grown under submerged fermentation containing rye flour as the carbon source. The aim of this study was to characterize the co-purified fraction, especially the invertase activity. An invertase and a β-glucosidase were co-purified by two chromatographic steps, and the isolated enzymatic fraction was 139-fold enriched in invertase activity. SDS-PAGE analysis of the co-purified enzymes suggests that the protein fraction with invertase activity was heterodimeric, with subunits of 47 and 27 kDa. Maximal invertase activity, which was determined by response surface methodology, occurred in pH and temperature ranges of 4.0–6.0 and 55–65 °C, respectively. The invertase in co-purified enzymes was stable for 1 h at pH 3.0–10.0 and maintained full activity for up to 1 h at 55 °C when diluted in water. Invertase activity was stimulated by 1 mM concentrations of Mn²⁺ (161 %), Co²⁺ (68 %) and Mg²⁺ (61 %) and was inhibited by Al³⁺, Ag⁺, Fe²⁺ and Fe³⁺. In addition to sucrose, the co-purified enzymes hydrolyzed cellobiose, inulin and raffinose, and the apparent affinities for sucrose and cellobiose were quite similar (K_M = 22 mM). However, in the presence of Mn²⁺, the apparent affinity and V_max for sucrose hydrolysis increased approximately 2- and 2.9-fold, respectively, while for cellobiose, a 2.6-fold increase in V_max was observed, but the apparent affinity decreased 5.5-fold. Thus, it is possible to propose an application of this multifunctional extract containing both invertase and β-glucosidase to degrade plant biomass, thus increasing the concentration of monosaccharides obtained from sucrose and cellobiose.     

Continuous sucrose hydrolysis by an immobilized whole yeast cell biocatalyst

An immobilized biocatalyst with invertase activity prepared by immobilization of whole yeast cells without use of any insoluble carrier was tested in tubular fixed-bed reactors from the point of view of possible application for continuous full-scale sucrose hydrolysis. At inlet sucrose concentration above 60% (w/w) and reaction temperature 60–70°C, total sucrose hydrolysis was achieved at a flow rate of 0.6–1.5 bed volumes per hour. At a flow rate about 10 bed volumes per hour, the conversion was still 0.5. The specific productivity of the biocatalyst was 3–25 h⁻¹; the productivity of the reactor was 1–9 kg l⁻¹ h⁻¹. The half-life of the biocatalyst invertase activity was 815 h at 70°C. The specific pressure drop over the biocatalyst bed was less than 23 kPa m⁻¹. The biocatalyst was proved to be fully capable of continuous sucrose hydrolysis in fixed-bed reactors.     

Microencapsulation of recombinant Saccharomyces cerevisiae cells with invertase activity in liquid-core alginate capsules

As a means of integrating cell growth and immobilization, recombinant Saccharomyces cerevisiae cells with invertase activity were immobilized in liquid-core alginate capsules and cultured to a high density. S. cerevisiae cells of SEY 2102 (MAT alpha ura3-52 leu2-3, 112 his4-519) harboring plasmid pRB58 with the SUC2 gene coding for invertase were grown to 83 g/L of liquid-core volume inside the capsule on a dry weight basis. The cloned invertase was expressed well in the immobilized cells with slightly higher activity than the free cells in a batch culture. Invertase in the immobilized cells showed slightly more improved thermal stability than in the free cells. Storage in a Na-acetate buffer at 4 degrees C and 10 degrees C for 1 month resulted in 7% and 8% loss in activity, respectively. The sucrose hydrolysis reaction was stably maintained for 25 repeated batches for 7 days at 30 degrees C. Continuous hydrolysis of 0.3 M sucrose was carried out in a packed bed reactor with a conversion of more than 90% at a maximum productivity of 55.5 g glucose/L per hour for 7 days. In a continuous stirred tank reactor, the maximum productivity of 80.8 g glucose/L per hour was achieved at a conversion of 59.1% using 1.0 M sucrose solution, and 0.5 M sucrose solution was hydrolyzed for 1 week with a 95% conversion at a productivity of 48.8 g/L per hour. (c) 1996 John Wiley & Sons, Inc.     

Application of immobilized invertase to continuous hydrolysis of concentrated sucrose solutions

Invertase immobilized onto corn grits was utilized in the hydrolysis of highly concentrated sucrose solutions producting liquid sugar solutions containing glucose and fructose. Comparisons of conversion efficiencies of this immobilized invertase in a continuous stirredtank reactor and a plug-flow reactor indicated that the plug-flow reactor has an higher efficiency. Continuous sucrose hydrolysis was then performed in 0.1- and 1-L tubular reactors. This tenforld scaling-up was achieved without any noticeable loss in efficiency. This process thus was scaled-up to a 17.6-L pilot reactor set in a cane sugar refinery. This reactor was fed with highly concentrated sucrose solutions [71% (w/w)] to produce invert sugar syrup with the desired inversion degree. It allows a productivity equal to 9.1 kg sucrose hydrolyzed/h in the case of a 69% (w/w) sucrose initial concentration with a 72% conversion rate.     

Sulfite pretreatment to overcome recalcitrance of lignocellulose (SPORL) for robust enzymatic saccharification of hardwoods

This study demonstrates sulfite pretreatment to overcome recalcitrance of lignocellulose (SPORL) for robust bioconversion of hardwoods. With only about 4% sodium bisulfite charge on aspen and 30‐min pretreatment at temperature 180°C, SPORL can achieve near‐complete cellulose conversion to glucose in a wide range of pretreatment liquor of pH 2.0–4.5 in only about 10 h enzymatic hydrolysis. The enzyme loading was about 20 FPU cellulase plus 30 CBU β‐glucosidase per gram of cellulose. The production of fermentation inhibitor furfural was less than 20 mg/g of aspen wood at pH 4.5. With pH 4.5, SPORL avoided reactor corrosion problem and eliminated the need for substrate neutralization prior to enzymatic hydrolysis. Similar results were obtained from maple and eucalyptus. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Kinetics of invertase immobilised on poly(phe-lys) coated polystyrene beads

Summary Surface of polystyrene beads was modified by poly(phe-lys) for invertase immobilisation. The optimum immobilisation conditions of invertase were; 0.01% (w/v) poly(phe-lys), 2% (v/v) glutaraldehyde at 25 °C and pH 4.5. The kinetics of sucrose hydrolysis by free and immobilised invertase in a batch reactor at pH 4.5 and 55 °C gave K_m and V_max values for sucrose with free and immobilised invertase of 81, 114 mM and 10.1, 9.2 mol glucose/min.mg enzyme, respectively. The deactivation rate constants of free and immobilised invertase were 0.0347 and 0.0098 min^–1, respectively.     

Inversion of sucrose with β-d-fructofuranosidase (invertase) immobilized on bead DEAHP-cellulose: Batch process

The inversion of sucrose with β-d-fructofuranosidase (EC 3.2.1.26) immobilized by an ionic bond on bead cellulose containing weak basic N,N-diethylamino-2-hydroxypropyl groups has been investigated. The immobilized enzyme is strongly bound at an ionic strength up to 0.1 M in the pH range 3–6. The amount adsorbed is proportional to porosity and to the exchange capacity of the ion exchange cellulose, reaching values up to 200 mg/g dry carrier, with an activity in 10% sucrose solution at 30°C, pH 5, >8000 μmol min^?1 g^?1. The inversion of sucrose with immobilized β-d-fructofuranosidase was carried out in a stirred reactor. The dependence of activity on pH (3–7), temperature (0–70°C) and concentration of the substrate (2–64 wt%) were determined, and the inversion was compared with that obtained using non-immobilized enzyme under similar conditions. The rate of inversion at low substrate concentration (2–19 wt%) was described by Michaelis-Menten kinetics.     

Continuous sucrose hydrolysis by yeast cells immobilized to wool

A novel immobilized biocatalyst with invertase activity was prepared by adhesion of yeast cells to wool using glutaraldehyde. Yeast cells could be immobilized onto wool by treating either the yeast cells or wool or both with glutaraldehyde. Immobilized cells were not desorbed by washing with 1 M KCl or 0.1 M buffers, pH 3.5–7.5. The biocatalyst shows a maximum enzyme activity when immobilized at pH 4.2–4.6 and 7.5–8.0. The immobilized biocatalyst was tested in a tubular fixed-bed reactor to investigate its possible application for continuous full-scale sucrose hydrolysis. The influence of temperature, sugar concentration and flow rate on the productivity of the reactor and on the specific productivity of the biocatalyst was studied. The system demonstrates a very good productivity at a temperature of 70 °C and a sugar concentration of 2.0 M. The increase of the volume of the biocatalyst layer exponentially increases the productivity. The productivity of the immobilized biocatalyst decreases no more than 50% during 60 days of continuous work at 70 °C and 2.0 M sucrose, but during the first 30 days it remains constant. The cumulative biocatalyst productivity for 60 days was 4.8 × 10³kg inverted sucrose/kg biocatalyst. The biocatalyst was proved to be fully capable of continuous sucrose hydrolysis in fixed-bed reactors. Received: 8 November 1996 / Received revision: 31 January 1997 / Accepted: 31 January 1997     

Sucrose inversion by gelatin-entrapped cells of yeast (Saccharomyces cerevisiae)

Summary Sucrose hydrolysis by invertase-active yeast cells (S. cerevisiae) entrapped in gelatin was investigated using different types of miniaturized reactors. The entrapped preparations showed the highest operational stability in a continuous stirred-tank reactor. The invertase activity of the entrapped preparation was found to be almost independent of the buffer concentration so that sucrose invermay be conducted in a non-buffered medium.     

Stimulatory effects of 2,4-dichlorophenoxyacetic acid and of 1-naphthylacetic acid on sucrose level,invertase activity and sucrose utilization in the latex ofHevea brasiliensis

Summary Treatment of the bark ofHevea brasiliensis with 2,4-dichlorophenoxyacetic acid (2,4-D) or l-naphthylacetic acid (NAA) greatly increases sucrose level, invertase activity and sucrose utilization in the latex; the efficacy of 2,4-D is considerably greater than that of NAA. The greater sucrose utilization is the consequence of increased invertase activity. The changes occur as soon as the first tapping following bark treatment. It is suggested that the rise in both sucrose level and utilization in the latex serum mediate the effect of auxins on latex production. This is most likely related to a faciliation of latex outflow resulting from an increase in the osmotic and turgor pressure in the laticiferous tissue, as well as to enhanced regeneration of latex.The latex invertase has been found to be of a weakly alkaline type, with a sharp pH optimum at 7.15–7.20 in citrate-phosphate buffer. Its activity falls of rapidly on the acid side, being almost zero at pH 6.4. Since the natural pH of latex generally varies between pH 6.5 and 7.0, it is suggested that pH is an important factor in the regulation of invertase activity in the latex, and that the limiting nature of invertase-mediated sucrose hydrolysis in latex serum is caused by unfavourable conditions for invertase activity rather than by a scarcity of this enzyme.Expert of the International Atomic Energy Agency.     

FORMATION AND CHARACTERIZATION OF THREE TYPES OF YEAST INVERTASE

Three types of invertase (invertase I, II and III) are separatedfrom the soluble and insoluble fractions (4,500xg, 10 min supernatantand pellets of the homogenate, respectively) of baker's yeastby a DEAE cellulose column chromatography. The invertases Iand II are eluted with 0.1 M sodium acetate buffer (pH 3.9)and with 0.1 M sodium acetate buffer (pH 6.2) containing 0.1M NaCl from DEAE cellulose respectively, whereas the invertase-IIIremains adsorbed on the cellulose under these conditions. Theyare present in proportions of 2.5: 1 : 0.06 in the soluble fractionand 1.4: 1 : 0.12 in the insoluble fraction of the fresh baker'syeast cells. While in-vertase-II remains at a constant level,invertases I and III in the soluble fraction increase upon incubationof cells for the formation of invertase under the continuoussupply of sucrose. Invertases I and II differ from each other considerably in theoptimum pH and slightly in the response to (activation and inactivationby) crude papain and are identical with respect to the heatstability and probably to the affinity for sucrose. ¹Present address: Chemical Laboratory, Nippon Medical School,Konodai, Ichikawa-shi, Chiba-ken.     

An approach to cellulase recovery from enzymatic hydrolysis of pretreated sugarcane bagasse with high lignin content

The possibility of recovering the cellulases used for enzymatic hydrolysis of sugarcane bagasse was evaluated. A strategy was adopted to maximize the enzyme recovery: desorption of the enzymes adsorbed in the solid residue after hydrolysis, and re-adsorption of the enzymes from the liquid medium onto a fresh substrate. The use of surfactant during the enzymatic hydrolysis was important to improve the glucose release from the material structure and also to facilitate the enzyme desorption from the solid residue after hydrolysis. The temperature and pH used during desorption influenced the enzymes recovery, with the best results (90% adsorbed cellulase) being achieved at 45?°C and pH 5.5. The enzymes present in the liquid medium after enzymatic hydrolysis were partially recovered (77%) by adsorption onto the fresh substrate and used in new enzymatic hydrolysis batches. It was concluded that it is possible to recycle cellulases from an enzymatic medium for use in subsequent hydrolysis processes.     

Kinetics of the enzymatic hydrolysis of cellulose: 2. A mathematical model for the process in a plug-flow column reactor

The kinetics of enzymatic cellulose hydrolysis in a plug-flow column reactor catalysed by cellulases [see 1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] from Trichoderma longibrachiatum adsorbed on cellulose surface have been studied. The maximum substrate conversion achieved was 90–94%. The possibility of enzyme recovery for a reactor of this type is discussed. A mathematical model for enzymatic cellulose hydrolysis in a plug-flow column reactor has been developed. The model allows for the component composition of the cellulase complex, adsorption of cellulases on the substrate surface, inhibition by reaction products, changes in cellulose reactivity and the inactivation of enzymes in the course of hydrolysis. The model affords a reliable prediction of the kinetics of d-glucose and cellobiose formation from cellulose in a column reactor as well as the degree of substrate conversion and reactor productivity with various amounts of adsorbed enzymes and at various flow rates.     

Immobilized Sclerotinia sclerotiorum invertase to produce invert sugar syrup from industrial beet molasses by product

The fungus Sclerotinia sclerotiorum produces invertase activity during cultivation on many agroindustrial residues. The molasses induced invertase was purified by DEAE-cellulose chromatography. The molecular mass of the purified enzyme was estimated at 48 kDa. Optimal temperature was determined at 60 °C and thermal stability up to 65 °C. The enzyme was stable between pH 2.0 and 8.0; optimum pH was about 5.5. Apparent K_m and V_max for sucrose were estimated to be respectively 5.8 mM and 0.11 μmol/min. The invertase was activated by β-mercaptoethanol. Free enzyme exhibited 80 % of its original activity after two month’s storage at 4 °C and 50 % after 1 week at 25 °C. In order to investigate an industrial application, the enzyme was immobilized on alginate and examined for invert sugar production by molasses hydrolysis in a continuous bioreactor. The yield of immobilized invertase was about 78 % and the activity yield was 59 %. Interestingly the immobilized enzyme hydrolyzed beet molasses consuming nearly all sucrose. It retained all of its initial activity after being used for 4 cycles and about 65 % at the sixth cycle. Regarding productivity; 20 g/l of molasses by-product gave the best invert sugar production 46.21 g/day/100 g substrate related to optimal sucrose conversion of 41.6 %.