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Process Biochemistry Vol. 33, No. I, 21-28, 1998 pp. 0 1998 Elsevier Science Ltd All rights resewed. Printed in Great Britain 0032.9592/98 $19.00+0.00 PII: SOO32-9592(97)00046-O Industrial applications of pectic enzymes: a review Itziar Alkorta,” Carlos Garb& Maria J. Llama and Juan L. Serra Departamento de Bioquimica y Biologia Molecular, Facultad de Ciencias, Universidad de1 Pais Vasco, Apdo. 644, 48080 Bilbao, Spain (Received 9 April 1997; accepted 19 April 1997) Abstract Although pectic enzymes have long been used to increase the yield and clarity of fruit juices, it is only recently that technological innovations, such as the use of immobilization supports and continuous-flow systems, have been considered to optimize these fruit processing procedures. To our knowledge, this is the first review to focus on the benefits brought to the field by these new technologies and their potential for commercial applications. 0 1998 Elsevier Science Ltd Keywords: pectic enzymes, immobilization, membrane reactors. Introduction Pectic suhstunces Pectic substances are glycosidic macromolecules of high molecular weight that are widespread in the plant kingdom. They form the major components of the middle lamella, a thin layer of adhesive extracellular material found between the primary walls of adjacent young plant cells. In addition, they constitute an important part of the primary plant cell wall. The American Chemical Society classified pectic substances into four main types: protopectins, pectinic acids, pectins and pectic acids [l]. Whereas protopec- tins are water-insoluble, the other three are either totally or partially soluble in water [2]. Chemically, pectic substances are essentially branched heteropolysaccharides containing between a few hundred and about one thousand building blocks per molecule, with a backbone consisting of galac- turonic acid residues part of which are methyl- esteritied. The pectin molecule (Fig. 1) is generally agreed to consist of a chain structure of axial-axial E-( 1,4)-linked D-galacturonic acid units, containing blocks of I.-rhamnosc rich regions, with mainly arabi- nose, galactose and xylose as side chains. The carboxyl *TO whom correspondence should be addressed groups of the galacturonic acid are partly esterified by methyl groups, and partly or completely neutralized by sodium, potassium or ammonium ions. Some of the hydroxyl groups on CZ and C, may be acetylated [3]. Although, owing to their great importance in many fields, pectic substances have been intensively studied for more than six decades a better knowledge of the chemical structure of industrial pectins is still required if we are to understand and improve their techno- logical applications. Curiously, and most likely due to their great complexity, despite many reports on the applications of pectic substances, mainly as food addi- tives, relatively little work dealing with the chemical composition and structure of industrial pectins has been published [4]. Here, it must be clearly stated that there is no such thing as a uniform pectic substance since they present numerous variations in molecular mass; in degree of esterification and acetylation; in content and type of binding of neutral sugars: and in the distribution of substituents and non-uronide com- ponents [5]. Apart from their function as ‘lubricating’ or ‘cementing’ agents in the cell walls of higher plants. pectic substances are also involved in the interactions between plant hosts and their pathogens [6] and in the texture of fruits and vegetables during growing, ripening and storage [7]. Traditionally, pectic sub- stances have found application in the food industry 22 Itziar Alkorta et al. Fig. 1. Structure of the pectin molecule. Only one chain of the major component of pectins - galacturonic acid partially methvlesterified - is renresented here. Side chains of galactose, arabinose and xylose residues are not included in the figure. Taken from Serra et al. [2j most often as gelling components [8], while nowadays they are also used as nutritional fibre [5]. Although research in the field of ‘pectic substances’ has been carried out for many decades by scientists and technologists from variety of disciplines, at present, interest in these substances is still continuing worldwide. the glycosidic bonds of either pectate (endo- and exo- polygalacturonate lyase) or pectin (endopoly- methylgalacturonate lyase). Polymethylgalacturonate lyases (all of which are endo-acting enzymes) are the only pectinases proven to hydrolyze pectin [5]. Pectic enzymes Pectic substances are naturally degraded by ‘pectic enzymes’. The classification of pectic enzymes is based on their attack on the galacturonan backbone of the pectic substance molecule. Basically three types of pectic enzymes exist: de-esterifying enzymes (pectines- terases), depolymerizing enzymes (pectinases: hydro- lases and lyases) and protopectinases. Finally, protopectinases, protopectin-solubilizing enzymes, which liberate water-soluble and highly poly- merized pectin from protopectin, are classified into two types: one type reacts with the polygalacturonic acid region of protopectin (A-type), the other with the poly- saccharide chains that may connect the polygalac- turonic acid chain and cell wall constituents (B-type) Fl. Table 1 and Fig. 2 summarize the classification of pectic enzymes and the enzymic mode of action of the most frequent depolymerases on the pectin molecule, respectively. The first ones catalyze the de-esterification of the methoxyl group of pectin forming pectic acid, and are produced by fungi, bacteria, yeast and higher plants [5]. These pectinesterases are present in practically all commercial pectolytic enzyme preparations and may be involved in changes in the pectic substances of fruits and vegetables during ripening, storing and processing [71. The depolymerases split the a-(1,4)-glycosidic bonds between galacturonic monomers in pectic substances either by hydrolysis (hydrolases) or by J-elimination (lyases). The hydrolases have been divided into four groups [9]: those preferring pectate were called polyg- alacturonases, while those preferentially degrading pectin were called polymethylgalacturonases. The pre- fixes endo- and exo- used in connection with either these names denoting a random- or terminal-action pattern, respectively. Most commercial preparations of pectic enzymes are obtained from fungal sources [lo]. In fact, although for obvious economical reasons it is very difficult to find reliable information about the commercial production of pectic enzymes, probably all producer strains are Aspergillus species [5]. Nevertheless, in our laboratory, after studying the growth and extracellular production of pectin lyase by a group of 16 fungi obtained from the Spanish Type Collection Culture (Table 2) we con- cluded that Penicillium italicum and Penicillium expansum were the best producers [l 1,121. Pectic enzymes and fruit juice industry Endopolygalacturonases are produced by a wide variety of organisms such as numerous fungi and bacteria, a few yeasts, higher plants and some plant- parasitic nematodes. Exopolygalacturonases, however, have been shown to occur in different fruits and veget- ables as well as fungi and some bacteria [5]. Pectic substances are responsible for the consistency, turbidity and appearance of fruit juices [13]. In fact, the presence of pectic substances in fruit juices causes a considerable increase in their viscosity, thereby impeding the processes of filtration and subsequent concentration [2]. In relation to polymethylgalacturonases, although there are some articles describingtheir catalytic activity [9], the existence of these enzymes appears to be ques- tionable since it is possible that polygalacturonase preparations, contaminated with pectinesterases, have been mistaken for polymethylgalacturonase-containing preparations. Pectic enzymes have long been used to increase juice yield and to clarify juices [14]. Actually, most pectic enzyme preparations are used in the fruit pro- cessing industry. Considering that pectic enzymes alone account for about one-quarter of the worlds food enzyme production [15], one can safely conclude that we are ‘dealing with a huge market that could benefit immensely from the application of technological inno- vations designed to reduce economical costs and increase the productivity of the system. Lyases, which are also called trans-eliminases, split Fruit juice clarification, a process required to facili- Industrial applications of pectic enzymes: a review 23 Table 1. Classification of pectic enzymes acting on pectins or pectic acids EC suggested name Common name De-esterifying enzymes EC number Substrate Action pattern Polymethylgalacturonate esterase (PMGE) Depolymerizing enzymes Pectinesterase 3.1.1.11 Pectin Random Hydrolases Endopolygalacturonase (Endo-PC) Exopolygalacturonase 1 (Exo-PGl) Exopolygalacturonase 2 (Exo-PG2) Endopolymethylgalacturonase (Endo-PMG) Exopolymethylgalacturonase (Exo-PMG) Lyases Endopolygalacturonate lyase (Endo-PGL) Exopolygalacturonate lyase (Exo-PGL) Endopolymethylgalacturonate lyase (Endo-PMGL) Exopolymethylgalacturonate lyase (Exo-PMGL) Polygalacturonase Polygalacturonase Polygalacturonase Pectin hydrolase Pectin hydrolase Pectate lyase Pectate lyase Pectin lyase Pectin lyase 3.2.1.15 3.2.1.67 3.2.1.82 4.2.2.2 4.2.2.9 4.2.2.10 Pectate Random Pectate Terminal Pectate Penultimate bonds Pectin Random Pectin Terminal Pectate Random Pectate Penultimate bonds Pectin Random Pectin Terminal Pectic enzymes acting on ohgogalacturonates have not been included in this table because they are not very abundant and of little interest for industrial pectin degradation. Enzymes have been classified and named according to the Enzyme Commission (EC) (IUPAC-IUB recommendations). tate filtration and remove turbidity, is the oldest use of viscosity as well as the flocculation of the micelles pectic enzymes [15]. The presence of pectic substances present [16], allows these particles to be separated by that suspend toward insoluble (pulp) particles leads to sedimentation or filtration. problems in the clarification of fruit juices. The addi- Another important application of pectic enzymes in tion of pectic enzymes, which results in a rapid drop in fruit processing is their role in fruit juice extraction. COO-CH 1 ’ OH ‘“\, PMGL , OH coo- I OH YOO~ i1 PMGE OH Fig. 2. Enzymatic mode of action of the most frequent depolymerases on the pectin molecule. PMGL: polymethylgalacturonate lyase (pectin lyase); PMG: polymethylgalacturonase (pectin hydrolase); PMGE: polymethylgalacturonate csterase (pectines- tcrase); PGL: polygalacturonate lyase (pectate lyase); PC: polygalacturonase (pectate hydrolase). Taken from Serra et al. 121 24 Itziar Alkorta et al. Table 2. Production of pectin lyase by several fungi after 63 h of growth” soluble enzymes are used for the clarification of fruit juices. Strain Final pH Dry wt of cultures (ms/ml) Pectin lyase Wmg protein) Aspergillus carbonatius (CECT 2086) 2.6 3.3 0,9 A. niger (CECT 2088) 3.9 7,6 0.9 Penicillium enpansum (CECT 2275) 3.5 2.1 4.7 Most studies dealing with immobilized pectic enzymes can be classified into two groups [22]: (a) those concerning the immobilization of the whole complex of pectic enzymes, and (b) those showing the immobilization of separate purified pectic enzymes which were further studied for the effect of immobili- zation on their properties and mode of degradation of polymeric substrates. l? italicum (CECT 2294) 3.7 3.1 12.0 “Liquid Czapek Dox (modified) medium containing 05% (wt/vol) citrus pectin was inoculated with 5 x 10“ spores per ml in all cases. After 63 h of growth, aliquots were sampled and pH, biomass, and pectin lyase activity were determined. During this time, no pectin lyase activity was detected in culture filtrates of Saccharomyces fibuligera (CECT 1238), A. niger (CECT 277.5, 2090 and 2091), A. oryzae (CECT 2094 and 2095) Rhizopus arrhizus (CECT 2339 and 2340), R. nigri- cans (CECT 2344) R. rhizopodiformis (CECT 2763), R. stob- nifer (CECT 2672), and R. thailandensis (CECT 2774). Again, degradation of pectin by these enzymes facili- tates pressing and ensures high yields. After crushing soft fruits such as blackcurrants, raspberries and black cherries, these crude juices are often very viscous and the remaining solids very difficult to separate from the juice [5]. The activity of pectic enzymes causes a drop in viscosity making it possible to extract juice by pressing. Pectic enzymes are also applied in the maceration and solubilization of fruit tissues to retain integrity of the cell wall in a process called liquefaction of tissues. Another relatively recent use of pectic enzymes is the selective treatment of citrus concentrates with endopolygalacturonase to give limited hydrolysis of the pectins so as to reduce viscosity (citrus juices tend to gel when concentrated) [14]. Different endopolygalacturonases have already been succesfully immobilized on various supports: endopoly- galacturonase of Aspergillus sp. was immobilized by adsorption onto porous powdered poly(ethylenetere- phthalate) and covalently bound via amino groups on poly(2,6-dimethyl-p-phenyleneoxide) and poly(6-capro- lactame) [23-261. Rexova-Benkova and Mrackova- Dobrotova [27] also studied the immobilization of an endo-o-galacturonase by covalent binding to (hydrox- yalkyl) methacrylate gel. Similarly, other materials such a y-alumina and various types of macromolecular sup- ports have been utilized to immobilize endopoly- galacturonase and pectinesterase for the treatment of fruit juices [19,28-311. In fact, these two enzymes have been covalently co-immobilized into a glycophase- coated controlled pore-glass to compare their behaviour to that shown by the enzymes immobilized separately [13,32]. These same authors [l&33] immobilized a commercial preparation of pectolytic enzymes onto a nylon-polyethyleneimine copolymer and studied their potential application for the claritica- tion of apricot juice. Porous glass particles were also utilized by Weibel et al. [34] to covalently immobilize pectinesterase. Finally, in our laboratory, pectin lyase purified from Penicillium itulicum was immobilized by covalent binding to nylon in order to evaluate its pos- sible application in fruit juice processing [ 16,351. Immobilized pectic enzymes and fruit juice clarification Traditionally, the industrial utilization of pectic enzymes in fruit juice processing has been conducted in conventional batch reactors using soluble enzymes [17]. Unfortunately, after each cycle of operation the enzymes can not be recovered for further use, and are inevitably present in the final product altering organo- leptic properties. In this context, the immobilization of pectolytic enzymes has proven to be very advantageous for continuous industrial use [18]. From all these papers, and others not mentioned here, two things can be noted: (a) the most frequent methods for immobilization of pectic enzymes are covalent binding to insoluble supports and adsorption on a solid support; and (b) although pectin lyase and pectinesterase have also been immobilized, the most frequentimmobilized enzyme has been endopolygalac- turonase. Both facts can also be concluded from the survey of the main data on immobilized pectolytic enzymes carried out by Lozano et ul. [33]. However, relatively little research has been carried out on the immobilization of pectic enzymes [19]. Several authors [20,21] have already reported the dif- ferent advantages that the immobilization of pectic enzymes offers in comparison with processes where In spite of this amount of research on immobilized pectic enzymes, the procedures proposed still show low immobilization yields, high support costs and methods too elaborate to be easily applied on an industrial scale. In fact, Alkorta et al. [16] in their studies on nylon immobilized pectin lyase from P italicurn found a relatively low percentage of activity, probably due to the existence of diffusional constraints that impeded both substrate access to the enzyme and the release of the product into the bulk phase where it was actually being monitored. In addition, immobilization itself Industrial applications of pectic enqmes: a review 2s could partly hinder the conformational changes for the activity of the enzyme. These results were not surprising since although over the last decade there has been increased interest in the preparation of immobilized pectic enzymes for the clarification and depectinization of fruit juices using a wide variety of carriers and methods, satisfac- tory results without any limitations have rarely been achieved. The coupling of the enzyme usually results in a decrease in enzyme activity and, in some cases, some other characteristics of the enzyme action mode are also altered [ 16,361. Nonetheless, there are in the literature some posi- tive results suggesting the vast potential of immobilized pectic enzymes for the clarification of fruit juices and other similar applications. For instance, Alkorta et al. [16] reported that, in spite of the low yield values, the nylon-immobilized pectin lyase was capable of pro- ducing a 36% reduction in viscosity in a pectin solution (compared to a 46Y o viscosity reduction found with the free soluble enzyme), a value considered acceptable for the commercial application of this immobilized system in fruit juice processing. Omelkova et al. [26] also found a slower decrease in viscosity when using an immobilized endopolygalacturonase as compared to the soluble enzyme. Lozano et al. [33] point out that the viscosity-reducing activity is clearly affected by immobilization because the steric constraints produced by the support mean that only the more external bonds of the pectin molecule are accesible to the immobilized pectolytic enzymes. Alkorta et al. [16] also examined the effect of immobilized pectin lyase on the viscosity of melon, apricot and other fruit juices. In all cases, a reduction in viscosity of at least 25% was observed after just 60 min of incubation. Moreover, in the case of peach juice, the decrease in viscosity was similar to that obtained when the soluble enzyme was used. This may be due to the fact that the immobilized enzyme had a lower optimum pH of activity (closer to the pH of fruit juices) than its soluble counterpart. This shift to lower pH values is commonly found when immobilizing enzymes on supports actually possessing a positive net charge due to alteration of the proton distribution between the bulk phase and the surroundings of the immobilized enzyme [31,37,38]. Since many fruit juices show acidic pH values, this shift toward lower pH is an important benefit when considering the possible appli- cation of immobilized systems for the treatment of fruit juices. Alkorta rt al. [16] showed that the immobilization of pectin lyase on nylon caused a marked increase in the temperature stability of the enzyme. This higher thermal stability could be due to a restriction on its degrees of freedom caused by the immobilization itself, consequently hindering heat denaturation. Although it is well-known that an enzyme, when immobilized, sometimes turns out to bc more resistant to heat and chemicals than the soluble enzyme [39], the current state-of-the-art does not provide any direct answer to the question of what the stability of a given enzyme would be after immobilization [40]. In this respect, Ginalska et al. [41] found that endopolygalacturonase purified from A. niger was less sensitive to the action of metal ions after immobilization than was its soluble counterpart. Reactors for immobilized pectic enzymes The activity yields of immobilized systems using pectic enzymes appear to be negatively influenced by the col- loidal characteristics of pectin solutions and by the high molecular weight of pectic substances [42]. These diffu- sional limitations can be overcome, at least partly, thanks to the development of membrane reactors. Cross-flow membrane reactors have certain advantages when used to treat polymeric cloudy and viscous sub- strates [18]. For a review on membrane reactors and ultrafiltration, see Heath and Belfort 1431 and Zeman [44], respectively. Membrane reactors combine the advantages of con- ventional bioreactors and membrane technology by bringing together a continuous reaction and the simul- taneous separation of products from the reaction mixture. In addition to permitting the continuous removal of the resulting small-sized products from the reaction mixture containing the enzyme and the remaining large substrate, membrane reactors show, in principle, higher degrees of conversion than other types of bioreactors [45]. Recently. Lozano et al. [IX] reported the kinetics and operational behaviour of an immobilized pectolytic enzyme derivative in a membrane cross-flow reactor. Although ultrafiltration has been frequently used for fruit juice clarification [46,47], to our knowledge. only a few studies [ 17,18,48-501 that comhinc the USC of this technology and pectic enzymes have been reported. Alkorta et al. [17] designed and optimized a mem- branc reactor for the continuous /j-trans-elimination of citrus pectin using pectin lyasc from P italicurn. Figure 3 shows the membrane reactor system used in this work. All four variables studied (i.c. enzyme and sub- strate concentrations, filtrate flow-rate, and reaction volume) had an effect on pectin convcrsion. Although a gradual decay in reactor activity was obscrvcd over time. the system was capable of maintaining a viscosity decrease of 55% for approximately 50 h. After that time. the enzyme lost part of its activity probably due to sheer stress [ 171. Lozano ct ~1. [I81 also found that after reaching a maximum conversion value. the system became progressively less cfticicnt. Ncverthcless. it seems likely that the system stability may dcpcnd on the nature of the enzyme under study. Alkorta et 01. [SO] cxamincd the decrease in viscosity 26 Itziar Allvxta et al. Ultrafiltration I : - Valve /I \ Reactor Water bath u module I I - gauge Fig. 3. Scheme of the continuous-flow membrane system. Taken from Alkorta et al. [17] reactor of several fruit juices caused by pectin lyase in a batch and confined in a continuous-flow ultrafiltration mem- brane reactor. Although a similar viscosity reduction was achieved in both reactors (batch vs. continuous- flow membrane reactor) (Fig. 4), at this point, the intrinsic advantages of using continuous sytems should be taken into consideration. Conclusions on future applications of pectic enzymes Although pectic enzymes have long been used for fruit processing, it has only been recently that technological innovations such as the use of immobilization supports and continuous-flow systems have been considered in this context.Despite the fact that satisfactory results in the appli- cation of immobilized pectic enzymes without any limitations have rarely been achieved, the present data suggest that the immobilization of these enzymes appears to be of potential interest for the clarification of fruit juices. Once certain problems, such as diffu- sional constraints and the decrease in the enzyme activity usually found after immobilization, are over- (4 Batch reactor (b) Membrane reactor ._ > o Melon 20 - ??Purple grape I I 1 I I / I I 0 10 20 30 40 0 120 240 360 480 Operation time (min) Fig. 4. Decrease of viscosity of melon and purple grape juices catalyzed by I? italicurn pectin lyase in (A) a batch reactor and (B) a continuous-flow membrane reactor. The reaction mixture (20 ml in A and 100 ml in B) contained 0.2 U/ml pectin lyase and was incubated at 40°C and at the pH imposed by the juice. One hundred per cent viscosity values corresponded to 2.5 and 4.1 cSt for melon and grape juice, respectively. Modified from Alkorta et al. [SO] come the field will benefit greatly from the advantages intrinsic to immobilized systems. Similarly, although much research, mainly several on the optimization and design of a suitable reactor, is still required before considering a future commercial appli- cation, continuous-flow reactors and, in particular, membrane reactors show a great potential for their utilization in fruit juice processing. References 1. 2. 3. 4. 5. 6. 7. 8. 9. 10. 11. 12. 13. Kertesz, Z. I., The Pectic Substances. Interscience Publishing, New York, 1951. Serra, J. 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