Applied Microbiology and Biotechnology Volume 52 Issue 5 1999 [Doi 10.1007%2Fs002530051570] E....

11
MINI-REVIEW E. Parente Æ A. Ricciardi Production, recovery and purification of bacteriocins from lactic acid bacteria Received: 29 December 1998 / Received revision: 23 April 1999 / Accepted: 23 April 1999 Abstract Bacteriocins produced by lactic acid bacteria are a heterogeneous group of peptide inhibitors which include lantibiotics (class I, e.g. nisin), small heat-stable peptides (class II, e.g. pediocin AcH/PA1) and large heat-labile proteins (class III, e.g. helveticin J). Many bacteriocins belonging to the first two groups can be successfully used to inhibit undesirable microorganisms in foods, but only nisin is produced industrially and is licensed for use as a food preservative in a partially purified form. This review focuses on the production and purification of class I and class II bacteriocins from lactic acid bacteria. Bacteriocin production is growth associated but the yield of bacteriocin per unit biomass is aected by several factors, including the producing strain, media (carbohydrate and nitrogen sources, cat- ions, etc.) and fermentation conditions (pH, tempera- ture, agitation, aeration and dilution rate in continuous fermentations). Continuous fermentation processes with cell recycle or immobilized cells can result in a dramatic improvement in productivity over batch fermentations. Several simple recovery processes, based on adsorbing bacteriocin on resins or silica compounds, have been developed and can be used to build integrated produc- tion processes. Introduction Mankind has (consciously or unconsciously) exploited lactic acid bacteria (LAB) for thousands of years in the production of fermented foods because of their ability to produce desirable changes in the taste, flavour and tex- ture and to inhibit pathogenic and spoilage microor- ganisms. The inhibitory activity of LAB is due to pH decrease, competition for substrates and to a variety of antimicrobial compounds, including bacteriocins. Bac- teriocins have been defined as ‘‘extracellularly released primary or modified products of bacterial ribosomal synthesis, which can have a relatively narrow spectrum of bactericidal activity, characterized by inclusion of at least some strains of the same species as the producer bacterium and against which the producer strain has some mechanism(s) of specific protection’’ (Jack et al. 1995). The discovery of nisin, the first bacteriocin used on a commercial scale as a food preservative, dates back to the first half of this century (Rogers 1928; De Vuyst and Vandamme 1994) but research on bacteriocins of LAB has expanded in the last 15 years, prompted by their potential application as natural food preservatives and/or as food grade markers for the development of cloning vectors (Klaenhammer 1988). Bacteriocins have recently been grouped into three classes (class I: lanti- biotics; class II: small heat-stable non-lantibiotics; class III: large heat-labile proteins) on the basis of the se- quence of the mature peptides and prepeptides (Nes et al. 1996; Table 1). Nisin (class I) is licensed for use in foods in more than 40 countries and has been produced industrially since 1953 (De Vuyst and Vandamme 1994). The largest producer is Aplin & Barrett Ltd (Dorset, England, a subsidiary of Cultor Food Science, Ardsley, N.Y., USA), which markets a standardized (1 · 10 6 IU g )1 ) preparation of nisin (Nisaplin). The market price for Nisaplin is 810 DM kg )1 . In the current industrial pro- cess, pasteurized milk plus added yeast extract is treated with a protease and used as a substrate in batch fer- mentation at controlled pH and temperature. An ex- traction process, including a spray-drying step, follows and the resulting powder is standardized with NaCl to 1 · 10 6 IU g )1 . Further purification is costly and not commercially viable for food use (Trigg, Aplin and Barrett, personal communication). A standardized (minimum 0.9 · 10 6 IU g )1 ) nisin preparation (Chrisin) is also marketed by Chr Hansen (Hørsholm, Denmark). Appl Microbiol Biotechnol (1999) 52: 628–638 Ó Springer-Verlag 1999 E. Parente (&) Æ A. Ricciardi Dipartimento di Biologia, Difesa e Biotecnologie Agro-Forestali, Universita` della Basilicata, Via Anzio, 10, I-85100 Potenza, Italy e-mail: [email protected] Tel.: +39-0971-202432 Fax: +39-0971-46400

description

Applied Microbiology and Biotechnology Volume 52 Issue 5 1999 [Doi 10.1007%2Fs002530051570] E. Parente; A. Ricciardi -- Production, Recovery and Purification of Bacteriocins From Lactic Acid Bacteria

Transcript of Applied Microbiology and Biotechnology Volume 52 Issue 5 1999 [Doi 10.1007%2Fs002530051570] E....

  • MINI-REVIEW

    E. Parente A. Ricciardi

    Production, recovery and purication of bacteriocinsfrom lactic acid bacteria

    Received: 29 December 1998 / Received revision: 23 April 1999 /Accepted: 23 April 1999

    Abstract Bacteriocins produced by lactic acid bacteriaare a heterogeneous group of peptide inhibitors whichinclude lantibiotics (class I, e.g. nisin), small heat-stablepeptides (class II, e.g. pediocin AcH/PA1) and largeheat-labile proteins (class III, e.g. helveticin J). Manybacteriocins belonging to the first two groups can besuccessfully used to inhibit undesirable microorganismsin foods, but only nisin is produced industrially and islicensed for use as a food preservative in a partiallypurified form. This review focuses on the production andpurification of class I and class II bacteriocins fromlactic acid bacteria. Bacteriocin production is growthassociated but the yield of bacteriocin per unit biomassis aected by several factors, including the producingstrain, media (carbohydrate and nitrogen sources, cat-ions, etc.) and fermentation conditions (pH, tempera-ture, agitation, aeration and dilution rate in continuousfermentations). Continuous fermentation processes withcell recycle or immobilized cells can result in a dramaticimprovement in productivity over batch fermentations.Several simple recovery processes, based on adsorbingbacteriocin on resins or silica compounds, have beendeveloped and can be used to build integrated produc-tion processes.

    Introduction

    Mankind has (consciously or unconsciously) exploitedlactic acid bacteria (LAB) for thousands of years in theproduction of fermented foods because of their ability toproduce desirable changes in the taste, flavour and tex-ture and to inhibit pathogenic and spoilage microor-

    ganisms. The inhibitory activity of LAB is due to pHdecrease, competition for substrates and to a variety ofantimicrobial compounds, including bacteriocins. Bac-teriocins have been defined as extracellularly releasedprimary or modified products of bacterial ribosomalsynthesis, which can have a relatively narrow spectrumof bactericidal activity, characterized by inclusion of atleast some strains of the same species as the producerbacterium and against which the producer strain hassome mechanism(s) of specific protection (Jack et al.1995). The discovery of nisin, the first bacteriocin usedon a commercial scale as a food preservative, dates backto the first half of this century (Rogers 1928; De Vuystand Vandamme 1994) but research on bacteriocins ofLAB has expanded in the last 15 years, prompted bytheir potential application as natural food preservativesand/or as food grade markers for the development ofcloning vectors (Klaenhammer 1988). Bacteriocins haverecently been grouped into three classes (class I: lanti-biotics; class II: small heat-stable non-lantibiotics; classIII: large heat-labile proteins) on the basis of the se-quence of the mature peptides and prepeptides (Neset al. 1996; Table 1).

    Nisin (class I) is licensed for use in foods in more than40 countries and has been produced industrially since1953 (De Vuyst and Vandamme 1994). The largestproducer is Aplin & Barrett Ltd (Dorset, England, asubsidiary of Cultor Food Science, Ardsley, N.Y.,USA), which markets a standardized (1 106 IU g)1)preparation of nisin (Nisaplin). The market price forNisaplin is 810 DM kg)1. In the current industrial pro-cess, pasteurized milk plus added yeast extract is treatedwith a protease and used as a substrate in batch fer-mentation at controlled pH and temperature. An ex-traction process, including a spray-drying step, followsand the resulting powder is standardized with NaCl to1 106 IU g)1. Further purification is costly and notcommercially viable for food use (Trigg, Aplin andBarrett, personal communication). A standardized(minimum 0.9 106 IU g)1) nisin preparation (Chrisin)is also marketed by Chr Hansen (Hrsholm, Denmark).

    Appl Microbiol Biotechnol (1999) 52: 628638 Springer-Verlag 1999

    E. Parente (&) A. RicciardiDipartimento di Biologia, Difesa e Biotecnologie Agro-Forestali,Universita` della Basilicata, Via Anzio, 10, I-85100 Potenza, Italye-mail: [email protected].: +39-0971-202432Fax: +39-0971-46400

  • Although several class II bacteriocins have beenshown to be eective in the biopreservation of foods(Stiles 1996), none is licensed or marketed as a food ad-ditive in a partially purified form. Some undefined anti-microbial products (ALTA 2341, Quest BioTechnologyInc., Sarasota, Fla., USA; Microgard, Rhone-Poulenc,Courbevoie, France) are licensed for food use but nodetails are available on their composition and produc-tion, although it has been reported that ALTA 2341 maycontain a class II bacteriocin (Szabo and Cahill 1998).

    In this paper the factors aecting the production ofclass I and II bacteriocins from LAB and the techniquesfor their recovery and purification are reviewed. Sincenisin production was recently reviewed by De Vuyst andVandamme (1994), only some aspects of nisin produc-tion and purification will be addressed.

    Biosynthesis of bacteriocins from LAB

    Bacteriocins are synthesized as pre-propeptides, whichare processed and externalized by dedicated transportmachinery or by the sec-dependent mechanism (Neset al. 1996). Table 1 shows the amino acid sequence ofthe prepeptides of some class I and class II bacteriocins.Cleavage of leader peptides is carried out by specificpeptidases or by a proteolytic domain of the dedicatedABC transporter (Nes et al. 1996), which recognizehighly conserved sequences in the leader peptide. Inaddition, the synthesis of lantibiotics, like nisin, requirespost-translational modification of selected amino acidresidues prior to secretion (De Vuyst and Vandamme1994). In addition to structural and secretion/modifica-tion machinery genes, bacteriocin operons always in-clude genes for specific immunity proteins (Jack et al.1995; Nes et al. 1996) which protect the producer cellsfrom their own bacteriocins. However, little is known ontheir mode of action. The genes nisI and nisFEG havebeen implicated in nisin immunity. nisI is a 32 kDaprotein which is postulated to be lipid modified andextracellularly anchored to the membrane (Kuipers et al.1993). nisF and nisE encode for an ABC transporterwhich shows homology with proteins implicated in re-sistance to subtilin and microcin B17, while the pre-dicted product of nisG is a hydrophobic protein whichmay interact directly with the pore-forming domain ofnisin in a way similar to the immunity proteins ofcolicins (Siegers and Entian 1995). Immunity proteins ofclass II bacteriocins are usually small (51150 aminoacids) and show a low degree of homology, even whenthe bacteriocins are closely related or identical. This maysuggest that they do not interact directly with the bac-teriocins (Nes et al. 1996). However, it has been pointedout that many immunity proteins may actually resembleeach other, at least in structure (Eijsink et al. 1998).Some immunity proteins may integrate in the membraneof the producer strain (Axelsson et al. 1993; Fremauxet al. 1993) but many others do not present transmem-brane helices (Eijsink et al. 1998).

    Many bacteriocin operons are regulated by a quo-rum sensing system (for a review see Nes et al. 1996;Kleerezebem et al. 1997). The extracellular accumula-tion of an induction factor (IF) is sensed by a two-component signal transduction system consisting of amembrane- located histidine kinase (HK) which phos-phorylates a response regulator (RR), which in turninteracts with promoters of structural, biosynthetic andregulatory operons and induces gene expression. Thelantibiotic nisin autoregulates its own production(Kuipers et al. 1995; de Ruyter et al. 1996a; Quiaoet al. 1996). In Lactoccus lactis N8 (a nisin Z producer)both nisZBTCIPRK and nisFEG operons are inducedby nisin (Quiao et al. 1996). In nisin A producers, twoinducible promoters are located upstream of nisA andnisF; a third promoter is located upstream of nisR(Kuipers et al. 1995; de Ruyter et al. 1996a). In manyclass II bacteriocins, the IF, HK and RR are organizedin an autoinducible regulatory operon (Nes et al. 1996)and the IF is a bacteriocin-like peptide which mayhave no inhibitory activity. However, it has recentlybeen found that the IF of the plantaricin operons inLactobacillus plantarum C11, PlnA, has indeed bacte-riocin-like activity (Anderssen et al. 1998) and thatbacteriocin operons in Carnobacterium piscicola LV17Bcan be induced by carnobacteriocin CB2 and by abacteriocin-like IF (CnbS) whose gene is organized inan operon with cnbK (HK) and cnbR (RR) (Quadriet al. 1997).

    Induction is not the only factor aecting the expres-sion of bacteriocin operons: carbon source regulationand the level of cell-adhered nisin have been shown toaect nisin synthesis (De Vuyst and Vandamme 1992;Meghrous et al. 1992) and catabolite repression has beenclaimed to operate in the regulation of plantaricin Cproduction (Barcena et al. 1998). There are also a fewreports of induction of bacteriocin production caused bycells and extracts of sensitive strains (Barefoot et al.1994; Sip et al. 1998).

    Kinetics of bacteriocin production

    Bacteriocin production in LAB is growth-associated: itusually occurs throughout the growth phase; and ceasesat the end of the exponential phase (or sometimes beforethe end of growth: Parente et al. 1997; Lejeune et al.1998). A decrease of bacteriocin titre usually follows.This may be attributed to adsorption on producer cellsor to degradation by specific or non-specific proteases.To our knowledge, the latter has never been proven,while adsorption to cells occurs for most bacteriocins(see for example Meghrous et al. 1992; Yang et al. 1992;Parente et al. 1994; Parente and Ricciardi 1994a; DeVuyst et al. 1996; Lejeune et al. 1998; Chinachoti et al.1997d). Since adsorption of bacteriocins to cells ismaximal at pH 5.56.5 (Yang et al. 1992) and decreasesat low pH, it is not surprising that no reduction ofbacteriocin titre is sometimes observed in fermentations

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  • Table1

    Amino

    acid

    sequence

    ofprepeptides

    ofsomebacteriocinsproduced

    bylactic

    acid

    bacteria.(Lc.=

    Lactococcus;

    Lb.=

    Lactobacillus;

    Pc.=

    Pediococcus;

    Ec.

    =Enterococcus;

    Leuc.=

    Leuconostoc)

    Name

    Producerstrain

    Leader

    peptidesequence

    Propeptidesequence

    Ref.a

    ClassI(lantibiotics)

    Nisin

    ALc.lactissubsp.lactis

    (manystrains)

    MSTKDFNLDNVSVSKKDSGASPR

    ITSISLCTPGCKTGALMGCNMKTATCHCSIH

    VSK

    1

    Nisin

    ZLc.lactissubsp.lactis

    (manystrains)

    MSTKDFNLDNVSVSKKDSGASPR

    ITSISLCTPGCKTGALMGCNMKTATCNCSIH

    VSK

    2

    LactocinS

    Lb.sakei(L45,148)

    MEKTEKKVLDELSLHASAKMGARDVESSMNAD

    STPVLASVAVSMELLPTASVLYSDVAGCFKYSAKHHC

    3

    ClassIIa(pediocin-likebacteriocinswith

    strongantilisterialeect)

    PediocinAcH

    /PA-1

    Pc.acidilactici(PA1,H),

    Lb.plantarum(W

    HE92)

    MKKIEKLTEKEMANIG

    GKYYGNGVTCGKHSCSVDWGKATTCIINNGAMAWATGGHQGNHKC

    4

    SakacinA

    Lb.sakei(706),

    Lb.curvatus(LTH1174)

    MANVKELSNTELQTITGG

    ARSYGNGVYCNNKKCWVRNGEATQSIIGGMISGWASGLAGM

    5

    EnterocinA/1146

    Ec.faecium(CTC492,DPC1146)

    MKHLKILSIK

    ETQLIY

    GG

    TTHSGKYYGNGVYCTKNKCTVDWAKATTCIA

    GMSIG

    GFGGAIPGKC

    6LeucocinA

    Leuc.gelidum(U

    AL187)

    MMNMKPTESYEQLDNSALEQVVGG

    KYYGNGVHCTKSGCSVNWGEAFSAGVHRLANGGNGFW

    7

    ClassIIb(two-peptidebacteriocins)

    LafX

    (lactacinF)

    Lb.johnsoniiVPI11088

    NRWGDTVLSAASGAGTGIK

    ACKSGGP

    WGMAICGVGGAAIG

    GYFGYTHNACA

    8LafA

    (lactacinF)

    Lb.johnsoniiVPI11088

    RNNWQTNVGGAVGSAMIG

    ATVGGTICGP

    VAGAHYLPILWTGVTAATGGFGKIR

    K8

    ClassIIc(sec-dependentsecreted

    bacteriocins)

    EnterocinP

    Ec.faeciumP13

    MRKKLFSALIG

    IFGLVVTNFGTKVDA

    ATRSYGNGVYCNNSKCWVNWGEAKENIA

    GIVISGWASGLAGMGH

    9

    aReferences

    1Buchmanetal.(1988)

    4Motlaghetal.(1992)

    7Hastingsetal.(1991)

    2deVosetal.(1993)

    5Axelssonetal.(1993)

    8Allisonetal.(1994)

    3Skaugen

    (1994)

    6Aymerichetal.(1996)

    9Cintasetal.(1997)

    630

  • without pH control (De Vuyst and Vandamme 1992;Yang and Ray 1994).

    There have been only a few attempts to model bac-teriocin production. Parente and Ricciardi (1994a) andParente et al. (1994) modelled separately the productionand the adsorption/degradation of enterocin 1146 andlactococcin 140 using the following equations:

    dBdt YB=X dX

    dtif t < t0 1

    dBdt kD B X if t > t0 2

    where X is biomass concentration; B is bacteriocin titre;YB/X is the yield of bacteriocin per unit biomass pro-duced; t is the time at which bacteriocin production ismaximum; and kD the specific bacteriocin degradationrate. To model enterocin 1146 in batch and continuousfermentations (Parente et al. 1997), Eqs. (1) and (2) werecombined and bacteriocin degradation was assumed tobe a function of cell concentration only:

    dBdt YB=X dX

    dt kD X 3

    Lejeune et al. (1998) modelled bacteriocin production byLactobacillus amylovorus DCE471 in batch culturesusing a dierent approach:

    dBdt kB dX

    dtif X < X 0 4

    dBdt k0 B if X > X or S 0 5

    where S is substrate concentration; kB (=YB/X) is de-fined as the specific bacteriocin production rate; X is thecell dry mass level at which bacteriocin productionceases; k is the specific bacteriocin degradation rate. kwas found to be constant over a wide range of condi-tions while both X and kB varied significantly.

    The models described by Eqs. (1)(5) are empiricaland do not take induction into account, but this mayhave no consequence under practical conditions. In fact,even if the expression of nis operons is tightly regulatedand no transcription is obtained in the absence of nisin,the level needed for full induction in Lc. lactis is very low(0.50 lg l)1 = 0.02 IU ml)1; de Ruyter et al. 1996b). InCb. piscicola LV17, the use of very low inocula (

  • riocin production has been observed for nisin (Kim et al.1997) and amylovoryn L471 (De Vuyst et al. 1996; Le-jeune et al. 1998): In an elegant study, Kim et al. (1997)demonstrated that the ceiling for nisin production isaected by both nutrient availability and nisin inhibi-tion.

    Media

    Bacteriocin production is deeply aected by type andlevel of the carbon, nitrogen and phosphate sources,cations, surfactants and inhibitors.

    Bacteriocins can be produced from media containingdierent carbohydrate sources. Nisin Z can be producedfrom glucose, sucrose and xylose by Lc. lactis IO-1(Matsusaki et al. 1996; Chinachoti et al. 1997b, d) butbetter results were obtained with glucose (4000 IU ml)1)compared to xylose (3000 IU ml)1). Glucose, followedby sucrose, xylose and galactose were the best carbonsources for the production of pediocin AcH in an un-buered medium (Biswas et al. 1991). Sucrose wasfound to be a better carbon source than glucose forenterocin 1146 production; fructose or lactose result incomparable levels of biomass but low levels of bacte-riocin (Parente and Ricciardi 1994b). Catabolite re-pression has been used to explain the production ofplantaricin C at higher dilution rates (0.10.12 h)1) withsucrose and fructose compared to glucose (0.055 h)1) incontinuous cultures (Barcena et al. 1998).

    Both YB/X and final bacteriocin concentration areaected by the initial carbohydrate concentration inbatch fermentations at controlled pH. Using Lc. lactissubsp. lactis NIZO22186 in sucrose media (De Vuystand Vandamme 1992), maximum nisin titres were ob-tained with 30 g l)1 sucrose. Even if more biomass wasproduced, YB/X decreased from 19.1 to 10.9 mg g

    )1 assucrose concentration increased from 10 to 40 g l)1.This was explained by carbon source regulation of thesynthesis or activity of prenisin-modifying enzymes.Substrate and product inhibition of growth resultedin reduced enterocin 1146 production rate at high S0(Parente et al. 1997). Maximum amylovorin L471activity did not increase when glucose was increasedfrom 20 to 60 g l)1, but bacteriocin degradation startedsooner.

    Since LAB are nutritionally fastidious microorgan-isms, growth and bacteriocin production are often lim-ited by organic nitrogen sources rather than by thecarbon substrate. Kim et al. (1997) found that maxi-mum nisin concentration increased with increasing or-ganic nitrogen content. However, at any given specificgrowth rate, the specific nisin production rate decreasedwith the increasing amount of nitrogen source. The typeof nitrogen source also aects bacteriocin production.De Vuyst and Vandamme (1993) compared the eect oforganic nitrogen sources (at 10 g l)1) on nisin produc-tion in a complex medium: best results (2500 IU ml)1,with YB/X 64 mg g

    )1) were obtained with cotton-seed

    meal but high nisin yields (>2000 IU ml)1) were alsoobtained with yeast extract and fish meal. Lc. lactissubsp. lactis ATCC11454 produced 1.5 times more nisinin a filtered stillage-based medium (a raw nitrogensource) compared to LTB broth (Vant Hul and Gib-bons 1996). The dierential eect of nitrogen sourceswas confirmed by factorial experiments for enterocin1146 (Parente and Hill 1992; Parente and Ricciardi1994b) and lactocin D (Parente and Hill 1992).

    Both anions (phosphate) and cations (Mg2+, Ca2+)aect bacteriocin production, but their eect may bestrain specific. Inorganic phosphate improved nisinproduction with Lc. lactis subsp. lactic NIZO22186 (DeVuyst and Vandamme 1993): best results (3500 IU ml)1)were obtained in batch fermentations at pH 6.8 with50 g l)1 K2HPO4. However, the stimulatory eect ofphosphate was not confirmed for strain IO-1 (Matsusakiet al. 1996). Mg2+ has been shown to increase pediocinAcH production (Biswas et al. 1991), to improve nisinproduction and significantly decrease cell adhered nisinin Lc. lactis subsp. lactis ATCC11454 (Meghrous et al.1992) but it did not improve nisin production with strainIO-1 (Matsusaki et al. 1996). Adding 0.1 mol l)1 CaCl2resulted in increased maximum nisin Z concentrationand specific production rate, but did not aect growth orlactate production from xylose and glucose in batchfermentations at controlled pH (Matsusaki et al. 1996;Chinachoti et al. 1997b). This was explained by Ca2+

    activation of increased immunity of the leader peptidase(NisP) (by protecting the integrity of the cytoplasmicmembrane) or by nisin Z displacement from the cellsurface.

    Tween 80 has been found to stimulate the productionof some bacteriocins (Parente and Hill 1992; Daba et al.1993; Matsusaki et al. 1996). However, Tween maysimply have the eect of preventing bacteriocin ad-sorption on polypropylene and glass surfaces (Joostenand Nunez 1995) thus increasing apparent bacteriocintitres. Adding ethanol (1% v/v) improved lactocin S(Mrtvedt-Abildgaard et al. 1995) and amylovorin L471(De Vuyst et al. 1996) production. The stimulatory eectwas attributed to influences on gene expression, pre-vention of bacteriocin aggregation and to increased YB/Xunder stress conditions.

    Eect of fermentation conditions

    Since pH control improves the growth of LAB, it alsoresults in improved bacteriocin production. However,the optimal pH for bacteriocin production is usually5.56.0 (Meghrous et al. 1992; Kaiser and Montville1993; Parente et al. 1994; Parente and Ricciardi 1994a;Matsusaki et al. 1996; Chinachoti et al. 1997b), oftenlower than the optimal pH for growth. For enterocin1146 (Parente and Ricciardi 1994a) the optimal pH is aresult of higher YB/X and lower kD. A few bacteriocinsare produced only at low pH (5.0) (Biswas et al. 1991;Yang and Ray 1994; Mrtvedt-Albilgaard et al. 1995;

    632

  • Tahara et al. 1996; Barcena et al. 1998). For pediocinAcH this was attributed to the low pH needed for post-translational processing of the bacteriocin. However,this eect may be strain or species-dependent sincepediocin AcH is produced at pH 6.0 by Lb. plantarumWHE2 (Ennahar et al. 1996). Optimal pH may also beaected by the culture medium: nisin Z production withstrain IO-1 was optimal at pH 6.0 in xylose media(Chinachoti et al. 1997b) and at pH 5.5 in glucose media(Matsusaki et al. 1996).

    Growth at optimal temperature usually results inoptimal bacteriocin production (Meghrous et al. 1992;Daba et al. 1993; Matsusaki et al. 1996; Chinachotiet al. 1997b; Lejeune et al. 1998) but temperature stressand growth at sub-optimal temperature may result in anincrease of YB/X (Lejeune et al. 1998).

    Some LAB produce more than one bacteriocin. In-terestingly, the optimal pH and temperature for theproduction of the two bacteriocins of Leuconostoc me-senteroides subsp. mesenteroides FR52 (mesenterocin52 A and 52B; Krier et al. 1998) were dierent, thusallowing manipulation of the ratio of the two bacterio-cins by changing growth conditions.

    Agitation and aeration aect bacteriocin produc-tion. In fermentations at pH 5.5 using glucose mediawith Lc. lactis IO-1, maximum nisin Z concentration(3940 IU ml)1) and YB/X (68.5 mg g

    )1) were obtained at320 rpm (Chinachoti et al. 1997d) and only a small de-crease of nisin concentration and yield (3410 IU ml)1,YB/X 68.5 mg g

    )1) was obtained at 1000 rpm. On theother hand agitation at >540 rpm resulted in inhibitionof growth and nisin production in xylose media. Aera-tion (1040 ml min)1) significantly reduced nisin pro-duction, perhaps because of chemical degradation.Chemical degradation and eects on gene expressionwere also used to explain the suppression of lactocin Sproduction in aerobic conditions (Mrtvedt-Abildgaardet al. 1995). As observed for other stress factors, fer-mentation in the presence of oxygen resulted in an in-creased YB/X for amylovorin L471 (De Vuyst et al.1996), despite lower final bacteriocin titres.

    Since bacteriocin production is growth associated,bacteriocin production rates should improve in contin-uous fermentations where high growth rates can bemaintained. Batch and continuous processes for selectedbacteriocins are compared in Table 2. As predicted byEq. (4) a linear relationship is observed between dilutionrate (D) and specific enterocin 1146 production rate(Parente et al. 1997) with 0.10 < D < 0.60 h)1. A sim-ilar relationship can be calculated for bavaricin MN(Kaiser and Montville 1993) and for divercin (Bhugaloo-Vial et al. 1997). On the other hand, plantaricin C pro-duction in continuous culture is obtained only at lowdilution rates (Barcena et al. 1998). A more complexpattern was observed for nisin production in continuousculture with Lc. lactis subsp. lactis ATCC 11454 (Meg-hrous et al. 1992): in both lactose-limited and non-lim-ited cultures, maximum nisin concentration, yield andspecific production rate were obtained at D = 0.25 h)1

    and sharply decreased at higher and lower D (Table 2;Meghrous et al. 1992). Both the level of cell-adherednisin and the specific lactose uptake rate aected nisinproduction.

    Increase in D results in a decrease of biomass andbacteriocin concentration, a high substrate concentra-tion in the euent, and eventually wash-out of the cul-ture. Therefore, continuous fermentation with cellrecycle or with immobilized cells has been tested by someauthors (Table 2). Continuous fermentation coupledwith cell recycle with Lc. lactis subsp. lactis IFO12007led to an increase in nisin titre and volumetric nisinproductivity compared to batch fermentations (Tanigu-chi et al. 1994). Decrease in nisin productivity at highsubstrate concentration in the feed was attributed tohigh lactic acid concentrations which inhibited growthand nisin production. Continuous culture with cell re-cycle using a ceramic membrane can be used to producenisin Z at high dilution rates (Chinachoti et al. 1997c)with a slight improvement in productivity comparedto batch or continuous fermentation without cell recy-cle. Choice of the membrane type proved to be critical,since a hollow fibre polyolefin membrane completelyadsorbed nisin. Retention of bacteriocin with ceramicmembranes was also observed by Bhugaloo-Vial et al.(1997).

    Wan et al. (1995) compared nisin, brevicin 286 andpediocin PO2 production with free or Ca-alginate im-mobilized cells. In repeated batch fermentations, im-mobilized cells produced less bacteriocin than free cellsperhaps because of diusional limitations in alginategels. However, in continuous fermentation at high di-lution rate (3 h1) the titre of bacteriocin was higher(brevicin) or equal to (nisin and pediocin PO2) thoseobtained in batch fermentations, with significantly im-proved productivity. Using Ca-alginate immobilizedcells of Cb. divergens LV41 in a plug flow reactor op-erated at D = 2 h)1 resulted in a dramatic improvementof productivity compared to batch and continuous fer-mentations with free cells (Table 2; Bhugaloo-Vial et al.1997; Boyaval et al. 1998).

    Removal of phosphate and addition ofCaCl2 is neededtomaintainCa-alginate gel stability in repeated batch andcontinuous fermentations. Adsorption of cells on a re-generable photo-crosslinked gel (ENTG-3800) resulted innisin titres (up to 3000 IU ml)1) and yields (2.5 106

    IU g)1 CDW) higher than from free cells in repeatedbatch fermentations, with excellent support stability(Chinachoti et al. 1997a). In continuous fermentations,immobilization allowed the use of higher D compared tofree cell systems and, although nisin titre was lower thanwith free cells, nisin productivity increasedup to 3.89 105

    IU l)1 h)1 when D was increased to 0.3 h)1.

    Recovery and purication of bacteriocins

    The recovery and purification of bacteriocins on a lab-oratory scale has been recently reviewed (Carolissen-

    633

  • Table2Comparisonofbatchandcontinuousprocessesfortheproductionofselected

    bacteriocinsfromlacticacidbacteria.Bbacteriocintitre;YB/Xbacteriocinyieldperunitbiomass;

    r B=

    volumetricproductivity;Lb.=

    Lactobacillus;Ec.=

    Enterococcus;Cb.=

    Carnobacterium;Lc.=

    Lactococcus;Pc.=

    Pediococcus;n.a.notavailable;Ddilutionrateh

    )1;Ca-alg

    calcium

    alginateimmobilized

    cells;MFmicrofiltration;imm.immobilized

    cells(onENTG-3800)

    Bacteriocin

    Strain

    Process

    B (106AU

    orIU

    l)1)

    YB/X

    (106AU

    g)1)

    r B (106AU

    l)1h

    )1)

    Reference

    BavaricinMN

    Lb.bavaricusMN

    batch

    3.2

    n.a.

    0.12

    Kaiser

    andMontville(1993)

    cont.D=0.058

    6.4

    n.a.

    0.37

    cont.D=0.205

    6.4

    n.a.

    1.31

    Enterocin1146

    Ec.faeciumDPC1146

    batch

    2.8

    2.0

    0.28

    Parenteetal.(1997)

    cont.D=0.14

    3.2

    1.9

    0.45

    cont.D=0.56

    1.8

    1.9

    1.01

    Divercin

    Cb.divergensV41

    batch

    100.0

    n.a.

    2.2

    Bhugaloo-Vialetal.(1997)

    cont.D=0.03

    200.0

    78.1

    6.1

    cont.D=0.2

    210.0

    78.1

    40.0

    cont.+Ca-alg

    D=2

    5.0

    n.a.

    200.0

    cont.+MFD=0.4

    2.0

    n.a.

    0.8

    PlantaricinC

    Lb.plantarumLL441

    cont.D=0.055

    3.2

    2.1

    0.18

    Barcenaetal.(1998)

    cont.D=0.12

    0.4

    0.2

    0.05

    cont.D=0.25

    0.1

    0.06

    0.03

    Brevicin

    286

    Lb.brevisVB286

    batch

    24.8

    n.a.

    1.6

    Wanetal.(1995)

    cont.Ca-alg

    D=3

    38.4

    n.a.

    115.2

    Nisin

    Lc.lactisAFISC2011

    cont.Ca-alg

    D=3

    0.13

    n.a.

    0.38

    PediocinPO2

    Pc.acidilacticiPO2

    cont.Ca-alg

    D=3

    0.25

    n.a.

    0.75

    Nisin

    Lc.lactisATCC11454

    cont.D=0.1

    0.08

    0.043

    0.008

    Meghrousetal.(1992)

    cont.D=0.25

    0.18

    0.097

    0.044

    cont.D=0.4

    0.06

    0.033

    0.024

    Nisin

    Lc.lactisIFO12007

    batch

    0.12

    0.035

    0.019

    Taniguchietal.(1994)

    cont.+

    MFD=0.5

    0.15

    n.a.

    0.073

    cont.+

    MF+BD=0.5

    0.14

    n.a.

    0.071

    Nisin

    Lc.lactisIO

    -1batch

    3.15

    2.25

    0.263

    Matsusakietal.(1996)

    cont.D=0.1

    2.81

    2.14

    0.281

    Chinachotietal.(1997c)

    cont.+imm.D=0.1

    2.16

    n.a.

    0.216

    cont.+imm.D=0.3

    1.30

    n.a.

    0.389

    cont.+MFD=0.1

    2.75

    n.a.

    0.275

    cont.+MFD=0.3

    2.00

    n.a.

    0.60

    batch+MF+SepPakC8

    2.4(+

    1.4)

    2.50

    0.33

    634

  • Mackay et al. 1997). The cationic and hydrophobic na-ture of bacteriocins is used for their recovery fromcomplex fermentation broths which contain high levelsof peptides (1030 g l)1 compared to a bacteriocinconcentration of 10100 mg l)1). Laboratory purifica-tion protocols usually include an ammonium sulphateprecipitation step, followed by various combinations ofion-exchange and hydrophobic interaction chromatog-raphy, with a final RP-HPLC purification step. Chro-matography may be replaced by preparative isoelectricfocusing (Venema et al. 1997) and immunoanitychromatography has been reported to allow one-steppurification of nisin A (Suarez et al. 1997). Althoughthese procedures may provide excellent results in termsof yield and purification (Cintas et al. 1998), they areunsuitable for large scale bacteriocin recovery and pu-rification.

    Several protocols based on adsorption/desorption oron phase partitioning have been developed for largescale recovery and purification of bacteriocins.

    Bacteriocins can be recovered by adsorption onproducer cells at pH 6.06.5, followed by cell separationand desorption at pH 2.0 and 0.1 mol l)1 NaCl. Thismethod was very eective for pediocin AcH, nisin, sa-kacin A and leuconocin Lcm1 (Yang et al. 1992) butrecovery may be limited for other strain/bacteriocincombinations (Daba et al. 1994). Vortex flow filtrationsystems may replace centrifugation (Vant Hul andGibbons 1996) and may be more amenable to large scalerecovery of cells. However, when bacteriocin concen-tration is very high, the ability of cells to adsorb nisincan be exceeded, and recovery of bacteriocin with thecell fraction may only be partial.

    Bacteriocins can be adsorbed on HIC and cationexchange resins. The lantibiotics nisin and carnocinUI49 have been purified nearly to homogeneity with asimple two step protocol based on adsorption on HICand cation exchange resins (Stoels et al. 1993). Re-covery was higher than 100% (attributed to removal ofinterferences in the bioassay due to the purification) andpurification was 245 and 60fold for carnocin and nisin,respectively. Chinachoti et al. (1997c) found that Sep-Pak C8 cartridges were the best adsorbent for nisin Z.SepPak C8 were used in an integrated fermentationsystem with a batch fermentation coupled to microfil-tration; permeate was circulated on the cartridge andreturned to the fermenter: growth of the producer strainwas improved and a higher nisin productivity was ob-tained (Table 2).

    Ingestible porous silica compounds can also be usedto adsorb bacteriocins (nisin, pediocin PO2, brevicin 286and piscicolin 126) from fermentation broths (Wan et al.1996). Best results were obtained with Micro-Cel E.Adsorbed bacteriocins were still active on target or-ganisms (Wan et al. 1996) and could be desorbed with0.1% sodium dodecyl sulphate (Coventry et al. 1996),obtaining 110130 fold purification. Unfortunately, re-moval of SDS (by cold precipitation) was only partial(6070%).

    Boyaval et al. (1998) developed a simple, two-steppurification system based on detergent (Triton 114),phase partitioning and adsorption/desorption on a cat-ion exchange resin. Upon addition of 2% detergent tosupernatants, divercin V41 accumulated in the detergentphase and was recovered with a purity >95% afteradsorption on a cation exchange resin, washing andelution with NaCl 0.7 mol l)1. The method was claimedto be eective in the recovery of mesenterocin Y105 andnisin.

    Conclusions

    Although many bacteriocins produced by LAB havebeen shown to be very eective against pathogenic andspoilage microorganisms both in vitro and in vivo onlynisin is currently licensed for food use in a partiallypurified form. There might be several reasons for this.Although some class II bacteriocins may be more ef-fective than nisin against some food-borne pathogens(such as Staphylococcus aureus and Listeria monocyto-genes, Cintas et al. 1998; Eijsink et al. 1998), definitiveevidence on their eectiveness and stability in foods isstill scarce (Stiles 1996). In some cases it may be simplerand cheaper to use bacteriocin-containing food ingre-dients (Zottola et al. 1994) or to produce the bacteriocinin situ: protective cultures of Lb. plantarum WHE92(Ennahar et al. 1996, ALC 01 Visbyvac, from Wiesby,Niebull, Germany) and Lb. sakei BJ-33 (Andersen 1995,Bactoferm B-2, from Hansen, Hrsholm, Denmark) aremarketed for use in cheese and meat products, respec-tively. However, in several food products the growth ofLAB may be undesirable and direct addition of bacte-riocins may be a viable alternative. This would requireapproval by regulatory agencies (Fields 1996): althoughLAB are GRAS organisms and bacteriocins are likely tobe present in all natural, fermented foods (Stiles 1996).Although bacteriocin containing products (ALTA 2341)or bacteriocinogenic cultures (see above) are alreadybeing marketed, the cost of approval of bacteriocins fordirect use as food additives may not be justified by theassets.

    Low yields and high costs may be further bottleneckslimiting the commercial production of bacteriocins otherthan nisin. While there is no information on nisin yieldwith industrial strains, the maximum yield reported fornisin (1 mg=40,000 IU) is currently around 100 mg l)1

    (Chinachoti et al. 1997b). No figures are available forclass II bacteriocins, although in a recent paper (Cintaset al. 1998) yields of 0.10.25 mg l)1 were reported.Further improvement in bacteriocin yield and produc-tivity seem possible: by careful optimization the yield ofgallidermin has been raised from 10 to 720 mg l)1 (Jacket al. 1995). Although low cost substrates can be suc-cessfully used as carbon (for example whey permeate) ornitrogen (cotton seed meal, filtered stillage) sources, theneed for rich, complex media increases costs and com-plicates bacteriocin recovery; and the choice of ingredi-

    635

  • ents should be carefully optimized. The advantages ofintegrated production and recovery processes (batch orcontinuous fermentation with cell recycle and continu-ous adsorption of bacteriocins on resin) similar to thosedeveloped for the lantibiotic epidermin produced byStaphylococcus epidermidis (Horner et al. 1989) havebeen demonstrated for nisin (Chinachoti et al. 1997c).Appropriate exploitation of both cell biomass and bac-teriocin can result in further improvement of the prof-itability of the process: biomasses of the pediocin AcHproducer Lb. plantarum WHE92 are already used asprotective cultures in cheese.

    Genetic manipulations may improve the value ofexisting bacteriocins or allow their production in heter-ologous hosts. Improvement of nisin solubility and sta-bility can be obtained by protein engineering:replacement of Asn-27 or His-31 with lysine in nisin Zimproves solubility and stability without aecting anti-microbial activity (Rollema et al. 1995). Nisin was ex-pressed in the subtilin producer Bacillus subtilisATCC6633 (which has simpler nutritional requirementsthan LAB) but no data are available on the yields andproductivities (Rintala et al. 1993). Heterologous ex-pression of class II bacteriocins in other bacteriocin-producing strains has been demonstrated for lactacin F(Allison et al. 1995). Finally, increase in the expressionof immunity genes may raise the ceiling for bacterio-cin production (Kim et al. 1998).

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