Enzymatic hydrolysis of sodium-hydroxide-pretreated sallow in an ultrafiltration membrane reactor

An ultrafiltration membrane reactor was used to investigate the recovery of biocatalysts during enzymatic hydrolysis of pretreated sallow. Product inhibition could be eliminated by continuous removal of products through the ultrafiltration membrane, thus retaining the macromolecular substrate and enzymes. In this way, the degree of conversion was improved from 40% in a batch hydrolysis to 95% (within 20 h), and the initial hydrolysis rate was increased up to seven times. The recovery studies were focused on mechanical deactivation and irreversible adsorption on to the nonconvertible fraction of the substrate. Cellulase deactivation during mechanical agitation was not significant, and the loss of activity was attributed mainly to strong adsorption of the enzymes onto undigested material. This process was studied in semicontinuous hydrolyses, where fresh substrate was added intermittently. The amount of reducing sugars produced in this experiment was 25.7 g/g enzyme, compared to 4.7 g/g enzyme in a batch hydrolysis.     

Kinetics of continuous starch hydrolysis in a membrane reactor

Following a previous study on kinetics of enzymatic starch hydrolysis with Termamyl 120l (Novo Nordisk) in batch reactor, this paper deals with kinetics in a continuous recycled membrane reactor (CRMR). Starting from results obtained in various working conditions, an equation relating the production rates of small oligosaccharides (DP ranging from 1 to 5) to the sum of concentrations of oligosaccharides with a higher degree of polymerisation is proposed. This equation looks like the one already reported for a batch system, with the exception that in the CRMR the enzyme activity varies: an exponential decay of activity as a function of time must be introduced to smooth carefully data points.     

Enzymatic protein hydrolysis in a membrane reactor related to taste properties

Potato, Vicia faba and soybean proteins were hydrolysed enzymatically in a substrate feed membrane reactor system. Alkaline proteolytic enzymes and PM-10 membranes were used for the hydrolysis of potato protein. The taste of the ultrafiltrates, which was unpleasantly bitter and potato-like, was improved by application of gelatin. Also using PM-10 membranes, Vicia faba protein isolate was hydrolysed by alkaline and acid proteolytic enzymes. The bitterness of the ultrafiltrate decreased with the formation of an isoelectric precipitate, which was probably due to association of hydrophobic peptides. The reactor equipped with a cellulose acetate membrane delivered an acceptable enzymatic hydrolysate of Promine D during the first hours of ultrafiltration. This was not the case when similar processes were performed using non-cellulosic DM-5 membranes. The usefulness of ultrafiltration for obtaining bland protein hydrolysates seems to be limited to short-term processes with cellulose acetate membranes.     

Continuous enzymatic production of lactobionic acid using glucose-fructose oxidoreductase in an ultrafiltration membrane reactor

Glucose-fructose oxidoreductase from Zymomonas mobilis catalyzed the oxidation of various aldose sugars to the corresponding aldonic acids. The enzyme was used for the selective and high-yield conversion of lactose to lactobionic acid in batch, fed-batch and continous reaction mode. A productivity of 110 g L d was obtained in an ultrafiltration membrane reactor, operated for 70 h.     

Continuous hydrolysis of goat whey in an ultrafiltration reactor: generation of alpha-lactorphin

Bovine whey hydrolysate has been developed and applied to areas such as nutrition, culture media, and isolation of bioactive peptides. In order to produce such a type of hydrolysate, it is possible to use goat whey, which constitutes also a food processing by-product. Enzymatic hydrolysis of goat whey by pepsin was carried out in a continuous ultrafiltration reactor. The permeate contained peptide hydrolysate that was resolved by RPHPLC. Second order derivative spectroscopy, amino acid analysis, and mass spectrometry revealed the presence of a biologically active peptide called alpha-lactorphin. This constitutes preliminary information about goat whey enzymatic degradation for future applications.     

Production of high maltose syrup using an ultrafiltration reactor

Kinetics of enzymatic hydrolysis of starch to high maltose syrup (by simultaneous use of -amylase and isoamylase) has been studied here. Main product of dual-enzyme system, maltose, showed a competitive inhibition effect on apparent overall activity of enzymes. Thermal inactivation behavior could be expressed by an empirical exponential function. A mathematical model developed here has described performance of an ultrafiltration reactor (UFR) system by considering effects of product inhibition, enzyme deactivation, and formation of side-product. Effects of concentrations in substrate and enzymes, with residence time of substrate on the performance of UFR has been investigated. Proposed model has been successfully verified in simulating experimental data under various conditions. Operation stability of UFR has also been studied.     

Production of structured lipids by lipase-catalysed interesterification in an ultrafiltration membrane reactor

The application of membranes to the enzymatic production of structured lipids has been investigated using an ultrafiltration membrane reactor for a reaction between medium chain triacylglycerols (MCT) and n-3 polyunsaturated fatty acids from fish oil. Lipozyme IM was used as the biocatalyst. The incorporation of polyunsaturated fatty acids into MCT was increased by about 15% over 80 h by simultaneous separation of the released medium chain fatty acids compared to control.     

Enzymatic hydrolysis of sunflower oil in a standardized agitated tank reactor

This paper presents results on the kinetics of the hydrolysis of sunflower oil catalysed by the enzymes of Candida cylindracea. The influence of the agitation is focused, in a standardized reactor, with a Rushton turbine as the agitating element. It is proved that an increase of the agitation speed improves the kinetics of the reaction up to a certain value of the rotational speed where the agitation becomes turbulent. A large range of substrate concentrations is investigated and discussed compared to the usual conditions met in the literature.     

Performance of a membrane reactor for cellobiose hydrolysis

A continuous enzymatic hollow fiber reactor (HFR), obtained by immobilizing cellobiose active cells into the shell side of hollow-fiber modules, was studied. The HFR yield was monitored by glucose analysis resulting from hydrolysis of cellobiose. The residence time of substrate in the bioreactor to obtain convenient hydrolysis yields was calculated from tests carried out by varying the reactor dilution rate in the range 0.001-0.004 L/min. The glucose yield was measured for 300 h (continuous substrate flux). The yield decreased from 40 to 15%. This decrease was due to the loss of specific activity in the operating conditions and to the pressure drop increase from 0.2 to 1.7 atm. The pressure drop increase is in turn dependent on the cell loading (0.2-2.1 g dry cell) and the substrate flux.     

Enzymatic production of cyclodextrins from milled corn starch in an ultrafiltration membrane bioreactor

Cyclodextrin glycosyltransferase (CGTase) was found to be severely inhibited by cyclodextrins. In order to increase the conversion yield by reducing product inhibition and reuse the CGTase in the production of cyclodextrins from milled corn starch, an ultrafiltration membrane bioreactor system was employed. In a batch operation with ultrafiltration, the conversion yield was increased 57% compared with that without ultrafiltration. Operating conditions for the continuous production of cyclodextrins in the membrane bioreactor were optimized by taking into consideration the filtration rate and the conversion yield as follows: initial starch concentration, 7% (w/v); starch feeding rate, 240 mg/h; CGTase loading, 350 units/initial gram starch. When cyclodextrins were continuously produced in the membrane bioreactor under optimized conditions, 340 units of CGTase was require to produce 1 g of cyclodextrins for 48 h, while in the case of conventional batch operation, 1 g of cyclodextrins was produced for 24 h by 1410 units of CGTase. (c) 1993 John Wiley & Sons, Inc.     

Studies on enzymatic continuous production of cyclodextrins in an ultrafiltration membrane bioreactor

Studies on simultaneous hydrolysis of starch and synthesis of cyclodextrins by Thermo-aerobacter cyclodextrin glucosyltransferase were conducted in an ultrafiltration membrane bioreactor, allowing enzyme recovery and reduction of product inhibition. The influence of various reaction parameters like starch concentration, enzyme dosage and residence time on cyclodextrin composition was tested. A comparison of batch and continuous cyclodextrin production indicates that employing an ultrafiltration membrane bioreactor increases process efficiency.     

Enzyme hydrolysis of plasma proteins in a CSTR ultrafiltration reactor: Performances and modeling

By investigating the effects of four operating variables-volume (V), Ultrafiltration flux (J), enzyme concentration (E), and substrate concentration (S)-on capacity (K) and conversion rate (epsilon) of a hollow fiber CSTR, the performances of the CSTR and the kinetic constants of the reaction were determined. A model which takes into account the course of fractional conversion (X) according to the modified space-time parameter, tau (integrated form of V, J, S, and E), was devised by employing the relationship to integrate the equation for the reaction rate of the CSTR and the expression of the modified space time. Correlation of this model and the experimentally obtained results demonstrates that the characteristics for an ultrafiltration membrane reactor for enzymatic hydrolysis by alcalase of plasma proteins are close to those of an ideal CSTR. Optimal scaling up, however, remains dependent on the compromise which may be obtained between capacity and the conversion rate.     

Enzymatic hydrolysis of rapeseed oil by Thermomyces lanuginosus lipase: variation of continuous and dispersed phase in a slug flow reactor

Applied Microbiology and Biotechnology - This paper takes a look on the effects of mass transport limitation occurring in hydrolysis of rape seed oil by means of an interfacial activated lipase...     

Biodiesel production using a membrane reactor

The immiscibility of canola oil in methanol provides a mass-transfer challenge in the early stages of the transesterification of canola oil in the production of fatty acid methyl esters (FAME or biodiesel). To overcome or rather, exploit this situation, a two-phase membrane reactor was developed to produce FAME from canola oil and methanol. The transesterification of canola oil was performed via both acid- or base-catalysis. Runs were performed in the membrane reactor in semi-batch mode at 60, 65 and 70 degrees C and at different catalyst concentrations and feed flow rates. Increases in temperature, catalyst concentration and feedstock (methanol/oil) flow rate significantly increased the conversion of oil to biodiesel. The novel reactor enabled the separation of reaction products (FAME/glycerol in methanol) from the original canola oil feed. The two-phase membrane reactor was particularly useful in removing unreacted canola oil from the FAME product yielding high purity biodiesel and shifting the reaction equilibrium to the product side.     

Enzymatic resolution of (S)-(+)-naproxen in a continuous reactor

An enzymatic method for the continuous production of (S)-(+)-2-(6-methoxy-2-naphthyl) propionic acid (Naproxen) has been developed. The process consists of a stereoselective hydrolysis of the racemic Naproxen ethoxyethyl ester catalyzed by Candida cylindracea lipase. The reaction has been carried out in a continuous-flow closed-loop column bioreactor packed with Amberlite XAD-7, a slightly polor resin on which the lipase has been immobilized by adsorption. Various immobilization conditions as well as the properties of the immobilized lipase have been studied. The performance and the productivity of the bioreactor were evaluated as a function of the critical reaction parameters such as temperature, substrate concentration, and product inhibition. By using a 500-mL column bioreactor, 1.8 kg of optically pure (S)-(+)-Naproxen were produced after 1200 h of continuous operation with a slight loss of the enzymatic activity.     

The hydrolysis of triglycerides by immobilized lipase in a hydrophilic membrane reactor

In the present article a method is described to immobilize lipase from Candida rugosa on a hollow fiber membrane, and the use of such a system for the hydrolysis of lipids is reported. The membranes were ENKA hydro philic Cuprophan((R))-type hollow fibers, having a large specific surface area. The immobilized lipase exhibited a high stability: the half-life time was 43 days at a temperature of 30 degrees C. Furthermore, it is proved that kinetic studies can be carried out with this system, operated in a batch or continuous mode. The relation between conversion rate and degree of hydrolysis was determined. On this basis, a dynamic model of the process was developed that describes the relation between reaction conditions and the conversion rate.     

Enzymatic synthesis of a series of alkyl esters using novozyme 435 in a packed-bed,miniaturized, continuous flow reactor

Using lipase catalysed, enzymatic esterification as a model reaction, we successfully demonstrate the use of miniaturized technology for biocatalytic reactions. Benchmarked against batch reactions, nine alkyl esters have been synthesized effectively, using Novozyme 435 in a pressure driven, packed-bed, miniaturized, continuous flow reactor. In some cases close to 100% ester conversions were obtained. The paper also demonstrates the ability to screen the enzyme for substrate specificity.