h tt p : / / w w w . b j m i c r o b i o l . c o m . b r /
Biotechnology
and
Industrial
Microbiology
Growth
kinetic
models
of
five
species
of
Lactobacilli
and
lactose
consumption
in
batch
submerged
culture
Fazlollah
Rezvani
a,
Fatemeh
Ardestani
b,∗,
Ghasem
Najafpour
c aIslamicAzadUniversity,ShahroodBranch,DepartmentofChemicalEngineering,Shahrood,Iran bIslamicAzadUniversity,QaemshahrBranch,DepartmentofChemicalEngineering,Qaemshahr,IrancBabolNooshirvaniUniversityofTechnology,FacultyofChemicalEngineering,BiotechnologyResearchLab.,Babol,Iran
a
r
t
i
c
l
e
i
n
f
o
Articlehistory: Received7June2015 Accepted20September2016 Availableonline3January2017 AssociateEditor:MaricêNogueira deOliveira
Keywords: Bacterialgrowth
Exponentialkineticmodel Contoismodel
Lactobacilli
a
b
s
t
r
a
c
t
KineticbehaviorsoffiveLactobacillusstrainswereinvestigatedwithContoisandExponential models.Awarenessofkineticbehaviorofmicroorganismsisessentialfortheirindustrial processdesignandscaleup.Theconsistencyofexperimentaldatawasevaluatedusing Excelsoftware.L.bulgaricuswasintroducedasthemostefficientstrainwiththehighest biomassandlacticacidyieldof0.119and0.602gg−1consumedlactose,respectively.The biomassandcarbohydrateyieldofL.fermentumandL.lactiswereslightlylessandclosetoL. bulgaricus.Biomassandlacticacidproductionyieldof0.117and0.358forL.fermentumand 0.114and0.437gg−1forL.actobacilluslactiswereobtained.L.caseiandL.delbrueckiihadthe lessbiomassyield,nearly11.8and22.7%lessthanL.bulgaricus,respectively.L.bulgaricus (R2=0.9500and0.9156)andL.casei(R2=0.9552and0.8401)showedacceptableconsistency withbothmodels.Theinvestigationrevealedthattheabovementionedmodelsarenot suitabletodescribethekineticbehaviorofL.fermentum(R2=0.9367and0.6991),L.delbrueckii (R2=0.9493and0.7724)andL.lactis(R2=0.8730and0.6451).Contoisrateequationisasuitable modeltodescribethekineticofLactobacilli.SpecificcellgrowthrateforL.bulgaricus,L.casei, L.fermentum,L.delbrueckiiandL.lactiswithContoismodelinorder3.2,3.9,67.6,10.4and 9.8-foldofExponentialmodel.
©2017SociedadeBrasileiradeMicrobiologia.PublishedbyElsevierEditoraLtda.Thisis anopenaccessarticleundertheCCBY-NC-NDlicense(http://creativecommons.org/
licenses/by-nc-nd/4.0/).
Introduction
Kinetic models are useful tools in design and control of biotechnological processes to obtain improved knowl-edgeabout microbial growth behavior using mathematical
∗ Correspondingauthor.
E-mails:f.ardestani@qaemiau.ac.ir,Ardestanifatemeh@yahoo.com(F.Ardestani).
models along with specifically accurate and repeatable detailedexperiments.Cellgrowthtime-coursesareinvolved individual growth phases: lag phase, exponential growth phase,stationaryphaseandthephasewithexponentialdecay. Nonlinear mathematical models used to identify growth parameters.1
http://dx.doi.org/10.1016/j.bjm.2016.12.007
1517-8382/©2017SociedadeBrasileiradeMicrobiologia.PublishedbyElsevierEditoraLtda.ThisisanopenaccessarticleundertheCC BY-NC-NDlicense(http://creativecommons.org/licenses/by-nc-nd/4.0/).
Lactobacillusisagenusofgram-positivefacultative anaer-obic bacteria also known as one of the main groups of probioticorganismsinvolvedinfunctionalfoods.2–5 A com-mon featureof these microorganisms istheir antagonistic activity against some pathogens such as salmonella spp., Escherichia coli, Listeria monocytogenes, Clostridium perfringens and Helicobacterhepaticus.6–11 Thecapability ofL.plantarum and L.reuteriin phyticacid hydrolysisis valuableinbread processingtechnology.12Inoculatinghetero-fermentative lac-tic acid bacteria to alfalfa silages cause to increase the production of lactic and acetic acids, hence decrease pH, reducethe number ofyeastsand molds,and inhibit Enter-obacteriumandKlebsiellapneumoniae.13Lactobacilliarewidely appliedinindustrialenzymeproductionprocesses,for exam-pleglucose-formingamylase14andlactase.15Differentstrains ofLactobacilli are the main fermentative lactic acid and ␥-aminobutyricacidproducersusedincommercialprocesses aswellasstartersindairyproducts.16–18
KineticbehaviorofLactobacilliwasstudiedbysome pre-viousresearchers. Ghalyetal.,19 reportedthat highlactose concentrationshadaninhibitoryeffectonL.helveticusgrowth rate. They also emphasized that adding yeast extract to culturemediumand using micro aerationcould caused to increase the specificgrowth rateand lactose consumption ofLactobacilli.19Vasudha andHari20investigatedGompertz andLogistickineticmodelsforL.plantarumNCDC414.The viablecellcountsincreasedfrom4×105to7×1010CFUmL−1 at24h.20CockandStouvenel21studiedlacticacidproduction byL.lactissubslactis and showedthat upto35gL−1 lactic acidwasobtainedinfermentationwithusing60gL−1ofinitial glucose.21Amrane22evaluatedthegrowthkineticofL. helveti-cusonwheypermeate.Hecharacterizedanddescribed five separatephasesduringL.helveticusgrowth.22L.rhamnosuscell dryweightwasobtained;whichwasequalto23gL−1after18h incubationatappointedbioreactorconditions.23Guptaetal.,24 foundthatL.plantarumcellgrowthratewasimprovedwith anincreaseinagitationspeed.24Itwasalsofoundthatmalic acidascarbonsourceenhancedthespecificgrowthrateofL. plantarumfrom0.2to0.34h−1.25Thestudyofcellgrowthand substrateutilizationkineticofL.caseiandL.rhamnosusshowed asstrongexponentiallydependentonproductinhibitionat lowlactic acid concentrations.26 In ourbest ofknowledge, thereisnotanydocumentedreportonLactobacillikineticswith ContoisandExponentialkineticmodels.
Inthisarticle,kineticbehavior,cellgrowthandsubstrate consumptiontrendsoffivedifferentstrainsofLactobacilliwere investigated.BasedonContoisandExponentialkinetic mod-elsinabatchsubmergedcheesewheyasthemainnutrientsof themediumwasused.Ineachcase,influentialkinetic param-etersweredetermined.
Materials
and
methods
Microorganismsandinoculumpreparation
Lactobacillus species: L. casei subsp. casei PTCC1608, L. delbrueckiisubsp. delbrueckiiPTCC1333, L.delbrueckiisubsp. bulgaricusPTCC1737,L.fermentumPTCC1744andL.delbrueckii subsp.lactisPTCC1743werepreparedfromIranianResearch OrganizationforScienceandTechnology.
Thestockcultureofeachstrainwasseparatelyprepared onMRSmedium.Inoculatedcultureswereincubatedat37◦C for48handthenstoredinarefrigeratorat4◦C.Batch sub-merged fermentation process was performed in separate laboratory shake flasks contained of deproteinized sterile wheyasthemainsubstrate.Theculturemediawasenriched byaddingsomegrowthfactorsincluding(gL−1):lactose,50; yeastextract, 10;sodium acetate,5;KH2PO4, 2;MgSO4,0.2; MnSO4,0.05;FeSO4,0.03;peptone,10.
Culturepreparation
100mLofdeproteinizedandenrichedsterilewheywasadded toa250mLshakeflask.Beforeautoclaving,pHwasadjustedto 6.5bya2MNaOHsolutionofor2NHCl.Topreventundesired reactions, deproteinized whey and the enrichment media wereseparatelyautoclavedat121◦Cfor15minandthenwere mixedtogetherinsterileconditionstoobtained100mLfinal culturemediumineachshakeflask.
Batchsubmergedfermentation
Inoculationwasperformedbyadding2.5mLofLactobacillus stockculturetoeachshakeflask.Then,theflaskswere incu-batedat37◦Cmixedwithagitationspeedof50rpmfor50h.At thisperiod,sampleswereremovedatproper5hintervalsto assaylacticacid,lactoseandcelldryweightconcentrations.
Assessments
Lacticacidandlactoseconcentrationswereanalyzedbyhigh performanceliquidchromatography(HPLC,PerkinElmer200, Shimadzu,Japan)withAminexHEX-87Hcolumn.Themobile phaseconsistedof5mMsulfuricacidsolutionat40◦C and flowrateof0.6mLmin−1wasused.27
Cell dry weightwas assayed usinga spectrophotometer (Shimadzu,1601,Japan)atawavelengthof480nm.Standard dilutesolutionsofbacterialcellwerepreparedfromstationary phaseofcellgrowth.Todeterminecelldryweightcalibration curve,15mLofeachstandardsamplewaspassedthrougha celluloseacetatefilterwith0.45micronporesize.Filtersthen washedwithdistilledwateranddriedat100◦Cfor24h.Cell dryweightwascalculatedbasedondifferencesbetweenthe initialandthefinalfilterweights.ForeachLactobacillusspecies, aseparatestandardcurveofcelldryweightversusabsorption valuewasrecorded;whichwasappliedtodeterminecelldry weightinactualexperimentalsamples.
Kineticmodels
Contois(Eq.(1))isanun-structuredkineticmodelbasedon substrateandbiomassconcentrationandExponential(Eq.(2)) kineticmodelsisanotherun-structuredkineticmodelbased ononlysubstrateconcentration.
=max S ksx+S
(1)
60 50 40 30 20 10 0 6 5 4 3 2 1 0 0 10 20 30 Time (h)
Lactose con. Lactic acid con. Cell dry weight
Cell dr
y wight (g.L
–1
)
Lactose and lactic acid concentr
ation (g.L
–1
)
40 50 60
Fig.1–Celldryweightandlacticacidproductionaswellas
lactoseconsumptionprofileforLactobacillusdelbrueckii
subsp.bulgaricusPTCC1737inasubmergedbatchcultureof
deproteinizedwheyat37◦Cwith50rpmagitationspeedfor
52h.
whereandmaxisthespecificgrowthrateandthe maxi-mumspecificgrowth rateofbacterialstrainintermofh−1, respectively.Ks,S,S0,S1,XandXmisthesemi-saturated coef-ficient,thelimitingsubstrate (lactose)concentration,initial lactoseconcentration,requiredlactoseforinitialcellbiomass forming,celldryweightandthemaximumcelldryweightin termgL−1,respectively.
Results
CellgrowthFivedifferentLactobacillispecieswerestudiedforcellgrowth evaluationforincubationperiodof50h.Deproteinizedwhey ascarbon sourceswasused inasubmerged batchculture. Almost for all studied strains, a 6h lag phase period and 25–45h(dependonthestrain)exponentialgrowthphasewas observed.Table 1presentsbiomassproductionand lactose consumptiontrendsforfivedifferentstrainsofLactobacilli.
Fig.1presentscelldryweightandlacticacidproduction aswellaslactoseconsumptionprofileforL.delbrueckiisubsp. bulgaricusPTCC1737.Afterincubationperiodof(therealend oftheexponentialgrowthphase)maximumcelldryweight (5.1gL−1)wasobtained.Therateofbiomassproductivitywas calculated as 0.17gL−1h−1 for this strain. Maximum pro-ducedlacticacidbyL.delbrueckiisubsp.bulgaricusPTCC1737 wasdefinedto be26.6gL−1. For thisstrain, maximum lac-ticacidyieldandproductivitywasdeterminedof0.602gg−1 consumedlactose(after52hincubation)and 0.804gL−1h−1 (after24hincubation),respectively.Resultsshowedthatcell dryweightwasincreasedfrom0.9to5.1gL−1(morethan466% increase incell density) ata period of18h inexponential growthphase.
Similar behavior, of course with lower efficiency was observedforL.caseisubsp. casei PTCC1608(Fig.2).For this strain, producedcell biomasshasreachedto 3.4gL−1 after 36hincubation.BiomassproductivityofL.caseisubsp.casei PTCC1608wascalculated0.119gL−1h−1.Maximumlacticacid concentrationof24.2gL−1wasobtained.Forthisstrain, max-imum lactic acid yield and productivity was determined as0.586gg−1 consumed lactose(48hafterincubation) and 0.696gL−1h−1(after 24hincubation),respectively. However,
60 50 40 30 20 10 0 5 4 3 2 1 0 0 10 20 30 Time (h)
Lactose con. Lactic acid con. Cell dry weight
Cell dr
y wight (g.L
–1)
Lactose and lactic acid concentr
ation (g.L
–1)
40 50 60
Fig.2–Celldryweightandlacticacidproductionaswellas
lactoseconsumptionprofileforLactobacilluscaseisubsp.
caseiPTCC1608inasubmergedbatchcultureof
deproteinizedwheyat37◦Cwith50rpmagitationspeedfor
52h.
celldryweightwasincreasedfrom0.8to4.3gL−1(morethan 437%increaseincelldensity)ataperiodof24hinexponential growthphase.
L.delbrueckiisubsp.lactisPTCC1743reachedtoitsendof exponentialgrowthphaseafter24hincubation.Atthistime, celldryweightwas3.1gL−1andthen,remainedconstantfora periodof18h.Butattheendofthestationaryphase(after48h incubation)suddenlyincreasedto3.9gL−1andthendecreased againto3.1gL−1after52hincubation(Fig.3).Biomass pro-ductivityofL.delbrueckiisubsp.lactisPTCC1743wasevaluated equalto0.081gL−1h−1after48h.Inexponentialgrowthphase, celldryweightwasincreasedfrom0.6to3.1gL−1(morethan 416%increaseincelldensity)ataperiodof12h.Maximum lac-ticacidconcentrationwasobtainedas14.7gL−1atafter42h incubation.Maximumlacticacidyieldandproductivitywas obtained0.437gg−1consumedlactose(after42hincubation) and0.47gL−1h−1(after30hincubation),respectively.
L.delbrueckiisubsp.delbrueckiiPTCC1333hadanextended exponentialgrowthphaseuntil42hafterincubation.Atthis time, cell dry weight reached to 3.2gL−1 (Fig. 4). Biomass productivityofL.delbrueckiisubsp.delbrueckiiPTCC1333was obtainedas0.076gL−1h−1 after52hincubation.Lactic acid production wasobserved both atexponentialand the sta-tionary growth phases. Maximumlactic acid concentration (13.2gL−1)wasobtainedafter52hincubation(endofthe sta-tionary phase).Maximumlactic acidyieldandproductivity wasobtained0.351gg−1consumedlactose(after52h incuba-tion)and0.317gL−1h−1(after36hincubation),respectively.
60 50 40 30 20 10 0 5 4 3 2 1 0 0 10 20 30 Time (h)
Lactose con. Lactic acid con. Cell dry weight
Cell dr
y wight (g.L
–1
)
Lactose and lactic acid concentr
ation (g.L
–1)
40 50 60
Fig.3–Celldryweightandlacticacidproductionaswellas
lactoseconsumptionprofileforLactobacillusdelbrueckii
subsp.lactisPTCC1743inasubmergedbatchcultureof
deproteinizedwheyat37◦Cwith50rpmagitationspeedfor
Table1–BiomassandlactoseconcentrationsandspecificgrowthrateforfivestudiedLactobacilliinasubmergedbatch culturemediumoflactosefortifiedwheyat37◦Cwith50rpmagitationspeedfor52h.
Time(h) 0 6 12 18 24 30 36 42 48 52 L.bulgaricus X(gL−1) 0 0.2 0.9 2.5 4.2 5.1 5.1 5 5.1 5.2 S(gL−1) 50 47.9 40.1 26.6 13.5 7.3 7 6.7 6.1 5.8 (h−1) – 0 0.250 0.210 0.169 0.135 0.108 0.089 0.077 0.071 L.casei X(gL−1) 0 0.2 0.8 2.6 3.9 4.2 4.3 4.3 4.2 3.8 S(gL−1) 50 48.2 42.1 31.9 17.8 10.5 9.2 9.1 8.7 8 (h−1) – 0 0.231 0.214 0.165 0.127 0.102 0.085 0.072 0.064 L.lactis X(gL−1) 0 0.2 0.6 1.9 3.1 3.2 3.1 3.4 3.9 3.1 S(gL−1) 50 49.2 38.8 27.3 21.4 19.6 18.2 16.4 15.8 13.2 (h−1) – 0 0.183 0.188 0.152 0.115 0.091 0.079 0.071 0.059 L.delbrueckii X(gL−1) 0 0.2 0.6 1.7 2.4 2.6 2.9 3.2 3.1 3 S(gL−1) 50 48.1 36.4 25.3 22.1 18.2 16.4 15.1 13.6 12.4 (h−1) – 0 0.183 0.178 0.138 0.107 0.089 0.077 0.065 0.058 L.fermentum X(gL−1) 0 0.1 0.7 2.1 2.5 2.7 2.7 2.9 3.3 3.5 S(gL−1) 50 49.3 44.2 35.6 29.1 26.8 25.3 23.2 22.6 20.1 (h−1) – 0 0.324 0.254 0.179 0.137 0.110 0.093 0.083 0.077 60 50 40 30 20 10 0 5 4 3 2 1 0 0 10 20 30 Time (h)
Lactose con. Lactic acid con. Cell dry weight
Cell dr
y wight (g.L
–1
)
Lactose and lactic acid concentr
ation (g.L
–1)
40 50 60
Fig.4–Celldryweightandlacticacidproductionaswellas lactoseconsumptionprofileforLactobacillusdelbrueckii
subsp.delbrueckiiPTCC1333inasubmergedbatchculture ofdeproteinizedwheyat37◦Cwith50rpmagitationspeed for52h.
L.fermentumPTCC1744hadthelongestexponentialgrowth phase;after52hincubationperiod,maximumcelldryweight of 3.5gL−1 was obtained (Fig. 5). In addition, its biomass productivity was0.067gL−1h−1.Lactic acid productionwas observed at both exponential and the stationary growth phases. Maximumlactic acid concentration(10.7gL−1)was obtainedattheendofthestationaryphase.Maximumlactic
60 50 40 30 20 10 0 5 4 3 2 1 0 0 10 20 30 Time (h)
Lactose con. Lactic acid con. Cell dry weight
Cell dr
y wight (g.L
–1
)
Lactose and lactic acid concentr
ation (g.L
–1)
40 50 60
Fig.5–Celldryweightandlacticacidproductionaswellas
lactoseconsumptionprofileforLactobacillusfermentum
PTCC1744inasubmergedbatchcultureofdeproteinized
wheyat37◦Cwith50rpmagitationspeedfor52h.
acid yield and productivity was defined as0.358gg−1 con-sumedlactose(after52hincubation)and0.29gL−1h−1(after 30hincubation),respectively.
Contoiskinetic
Inordertoevaluatetheconsistencyoffivestudiedstrainswith Contoiskineticmodel,experimentaldataoflactose consump-tion and cell dry weightproduction inexponential growth phasewereused(Table1).Fig.6representsthelinearfitted experimentaldatausingContoiskineticmodelforfive inves-tigatedLactobacillistrains.
Malthuslawexplainstheexponentialgrowthphaseof Lac-tobacillusspeciesinabatchculture(Eq.(3)).IntegrationofEq.
(3)usingsuitableinitialcondition(X=X0att=t0)resultedin Eq.(4)thatdemonstratesspecificcellgrowthrate().The val-uesforinitialbiomassconcentrationandlagphasetimedelay (X0andt0)wereconsidered0.2gL−1and6h,respectively.
dX dt =X (3) =ln
X X0 t−t0 (4)Specific cell growth rate valueswere calculated accord-ing tothecelldryweightasbiomassconcentration(X)and averagelactoseconcentrationaslimiting substrate concen-tration(Save)fortheexponentialgrowthphaseusingEq.(4). Kineticconstantcoefficients(max,Ks)werecalculatedusing thecurvefittingmethod.
Exponentialmodel
Theconsistencyofthepracticaldataforthecellgrowthand lactoseconsumptionoffivestudiedLactobacillusspecieswith
8 7 6 5 4 3 2 1 0 0 0.2 0.4 (X/S)ave
Lactobacillis bulgaricus Lactobacillus casei
Lactobacillus delbrueckii Lactobacillus fermentum Lactobacillus lactis 1/ µ (h) 0.6 0.8 16 14 12 10 8 6 4 2 0 0 0.1 0.2 (X/S)ave 1/ µ (h) 0.3 0.4 12 10 8 6 4 2 0 0 0.1 0.2 (X/S)ave 1/ µ (h) 0.4 0.3 0.5 12 14 10 8 6 4 2 0 0 0.05 0.1 (X/S)ave 1/ µ (h) 0.2 0.15 0.25 12 14 10 8 6 4 2 0 0 0.05 0.1 (X/S)ave y=72 687x+0.3859 R2=0.9367 y=42.17x+3.2158 R2=0.9493 y=38.21x+2.9994 R2=0.873 y=5.0736x+3.7738 R2=0.95 y=11.965x+3.3463 R2=0.9552 1/ µ (h) 0.2 0.15
Fig.6–ThelinearplottofittingtheexperimentaldataonsubstrateutilizationandcellgrowthtoContoiskineticmodelfor
fivestudiedLactobacilliinasubmergedbatchculturemediumoflactosefortifiedwhey.
Exponential kinetic model is presented in Fig. 7. F(S) was definedasEq.(5). F(S)=
S0+S1−S S1 (5) Specificcellgrowthratewascalculatedforeachofstudied Lactobacilliinexponentialandthestationarygrowthphases arepresentedinTable1.Discussion
Theanalysisofobtainedresults(presentedinTable1)showed that L. delbrueckii subsp. bulgaricus PTCC1737, L. fermentum PTCC1744 and L.delbrueckii subsp. lactis PTCC1743had the highestbiomassyieldof0.119,0.117and0.114gg−1of con-sumed lactose, respectively. L. casei subsp. casei PTCC1608
30 25 20 15 10 5 0 0 10 20 Time (h) f (S) 30 40 25 20 15 10 5 0 0 10 20 Time (h) f (S) 30 40 50 60 70 50 40 30 20 10 0 0 20 40 Time (h) f (S) 60 60 70 50 40 30 20 10 0 0 10 20 Time (h) Lactobacillus fermentum
Lactobacillus lactis Lactobacillus delbrueckii
Lactobacillus casei Lactobacillis bulgaricus f (S) 30 40 50 60 35 30 40 25 20 15 10 5 0 0 10 20 Time (h) f (S) 30 40 y=2.3216e0.0824x R2=0.9156 y=11 788e0.0339x R2=0.6451 y=6.6256e0.03x R2=0.7724 y=8.2789e0.0383x R2=0.6991 y=2284e0.0757x R2=0.8401
Fig.7–TheexponentialplottofittingtheexperimentaldataonsubstrateutilizationandcellgrowthtoExponentialkinetic
modelforfivestudiedLactobacilliinasubmergedbatchculturemediumoflactosefortifiedwhey.
and L.delbrueckiisubsp. delbrueckiiPTCC1333showed lower biomassproductionyield,relatively11.8and22.7%lessthan L.delbrueckiisubsp.bulgaricus PTCC1737, respectively.Fig. 1
represents that lactic acid production rate in exponential growthphasewashigherthanthestationaryphase.Biomass productivityofL.caseisubsp.caseiPTCC1608wascalculated 30%lessthanL.delbrueckiisubsp.bulgaricusPTCC1737. Max-imumlacticacidconcentrationwas9%lessthanL.delbrueckii subsp.bulgaricusPTCC1737.Forthisstrain,maximumlactic acidyieldandproductivity wasinorder2.65 and8.7%less thanL.delbrueckiisubsp.bulgaricusPTCC1737. Biomass pro-ductivityofL.delbrueckiisubsp. lactisPTCC1743was 52.35% lessthanL.delbrueckiisubsp.bulgaricusPTCC1737.Maximum
lactic acid concentration was approximate 45% less than L. delbrueckii subsp. bulgaricus PTCC1737. Maximum lactic acid yieldand productivity was inorder of27.4 and 41.5% lessthanL.delbrueckiisubsp.bulgaricusPTCC1737.Cockand Stouvenel21found35gL−1lacticacidproductionsbyL.lactis subs lactis.In the presentwork, maximumlactic acid con-centrationwasobtainedas26.6gL−1byL.delbrueckiisubsp. bulgaricus PTCC1737. Biomass productivity of L. delbrueckii subsp.delbrueckiiPTCC1333was55.3%lessthanL.delbrueckii subsp. bulgaricus PTCC1737 and approximately near to L. delbrueckiisubsp.lactisPTCC1743.Lacticacidproductionwas observed atexponential andthe stationarygrowth phases. Maximum lacticacidconcentrationwasobtainedafter52h
Table2–AcomparisonofContoisandExponentialkineticconstantsforfivedifferentspeciesofLactobacilli.
Strain R2
max(h−1) Ks(gL−1)
Contois Exponential Contois Exponential Contois
L.delbrueckiisubsp.bulgaricusPTCC1737 0.9500 0.9156 0.265 0.0824 1.34
L.caseisubsp.caseiPTCC1608 0.9552 0.8401 0.299 0.0757 3.58
L.delbrueckiisubsp.lactisPTCC1743 0.8730 0.6451 0.333 0.0339 12.72
L.delbrueckiisubsp.delbrueckiiPTCC1333 0.9493 0.7724 0.311 0.03 13.11
L.fermentumPTCC1744 0.9367 0.6991 2.591 0.0383 188.33
incubation(endofthestationaryphase),halfofL.delbrueckii
subsp.bulgaricus PTCC1737.Maximum lacticacid yieldand productivitywasinorder41.7and60.6%lessthanL.delbrueckii
subsp.bulgaricusPTCC1737. L.fermentumPTCC1744hadthe longestexponentialgrowth phase.Itsbiomassproductivity was60.6%lessthanL.delbrueckiisubsp.bulgaricusPTCC1737. Thisstrainwasthesameaspreviousmentionedstrain,lactic acid productionwasobserved atbothexponentialand the stationarygrowth phases. Maximum lactic acid concentra-tionwasabout 60%lessthan L.delbrueckiisubsp.bulgaricus
PTCC1737.Maximumlactic acidyieldand productivitywas in order of 40.5 and 63.9% less than L. delbrueckii subsp.
bulgaricusPTCC1737.Polak-Bereckaetal.,23 reported23gL−1 of dry cell weight after 18h for L.rhamnosus, much more thanourstudiedstrains.Thisindicatethatstraintypeand culture composition have considerable impact on biomass production.23ReporteddatabyBerryetal.,28onL.rhamnosus ATCC10863growthcharacteristicsanditslacticacid produc-tioninbatchcultureofadefinedmediumshowedayieldof 0.84glacticacidg−1ofconsumedsubstrate.28Bustosetal.,29 studiedlacticacidproductionbyL.pentosusATCC8041from vine-trimmingwastes.They reporteda productionyieldof 0.77(glactic acidg−1 consumed substrate)that isrelatively lessthanourobtaineddata.29Itwasfoundthatthequalityof substrateandtypeoforganismspeciesarekeyparametersin productyield.Themainreasonmightbeduetoexistenceof highmineralconcentrationinthewhey.Kimetal.,30reported 13.7gL−1 lactic acid concentrations ina 48h fermentation usingL.lactisssp.lactisthatismuchlowerthanourobtained datausingglucoseasthemainsubstrate.30
Results showed that L. delbrueckii subsp. bulgaricus PTCC1737andL.caseisubsp.caseiPTCC1608hadgood accept-ableconsistencyusingContoiskineticmodel.R-square,max andKsforthefirststrainwereinorderof0.95,0.265h−1and 1.34gL−1 andforthesecondonewere0.9552,0.299h−1and 3.85gL−1,respectively(Table2).L.delbrueckiisubsp.delbrueckii PTCC1333 also showed an acceptable fitting with Contois kinetic model. For this strain R-square, max and Ks were 0.9493, 0.311h−1 and 13.11gL−1, respectively. L. fermentum PTCC1744wasfittedtoContoismodelwithagoodR-square (0.9367)andthegreatestamountsofspecificcellgrowthrate (2.591h−1).ButitsContoissemi-saturatedcoefficient(Ks)was the greatest obtained value of 188.33gL−1. Therefore, it is perceivedthatContoiskineticmodelmaynotbedesiredto describethecellgrowthandsubstrateconsumptionbehavior ofL.fermentumPTCC1744.Resultsindicatedthatthe consis-tency ofL. delbrueckiisubsp. lactis PTCC 1743 with Contois kineticmodelisthelessthan allotherinvestigatedstrains. Forthisstrain,R-squarewasdeterminedtobeaslowas0.873.
Vasudha and Hari 20 studiedthe Gompertzand Logistic kineticmodelsforL.plantarumNCDC414.Theyfoundthatthe viablecellcountsincreasedfrom4×105to7×1010CFUmL−1, lacticacidconcentrationincreasedbyabout4.5foldsand44% w/vofsubstrateconsumptionwasoccurredatanincubation periodof24h.20 Inthiswork,significantlacticacid produc-tion observedfortheexponentialandstationaryphases.In addition,thecell dryweightincreasedbyabout10–15folds (depend on thestrain) in24h. Alvarezet al.,26 studied the kineticsofcellgrowth,lactic acidproductionandsubstrate utilization ofL.caseivar.rhamnosus.Theyreportedastrong exponentiallydependentproductinhibitionatlowlacticacid concentrations.Theirresultsindicatedthatlacticacid produc-tionratewaspartiallyassociatedwithbiomassgrowthasthis workdemonstrated.26
Based onthe calculated kineticparameters (Table 2),L. delbrueckii subsp. bulgaricus PTCC1737 and L. casei subsp. caseiPTCC1608hadgoodacceptableconsistencywithContois kineticmodeltoo.R-squareandmaxforthefirststrainwere inorder0.9156and0.0824h−1andforthesecondstrainwere 0.8401and0.0757h−1,respectively(Table2).
Itwas foundthatother studiedstrains didnothavean acceptableconsistencywithExponentialkineticmodel.Thus, Exponential kinetic model is not a well desired model to describethecellgrowth andsubstrateconsumption behav-iorofthesethreestrains. Theobtainedspecificgrowthrate forL.delbrueckiisubsp.bulgaricusPTCC1737withExponential kineticwasabout70%lessthantheobtainedvaluewith Con-toiskineticmodel.Also,forL.caseisubsp.caseiPTCC1608,75% declinewasdocumentedinthiswork.
Conclusion
Thisisthefirstreportonthecellgrowthandsubstrate utiliza-tionkineticoffivedifferentstrainsofLactobacilliwithrespect toContoisandExponentialkineticmodels.L.delbrueckiisubsp. bulgaricus PTCC1737 was introduced as the desired strain infields ofbiomassand lacticacid productionyield.L. del-brueckii subsp. bulgaricusPTCC1737and L.casei subsp. casei PTCC1608showedacceptableconsistencywithbothContois andExponentialkineticmodels.Wefound,Contoisisbetter thanExponentialmodeltodescribecellgrowth andlactose consumptionbehaviorofL.strains.
Conflicts
of
interest
Acknowledgments
TheauthorswishtothanktheOfficesofViceChancellorsin ResearchatIslamicAzadUniversity,QaemshahrBranchfor theirsupportofvaluedexperimentalandanalyticalwork con-ductedduringthecourseofpresentresearch.
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s
1. VazquezJA,MuradoMA.Unstructuredmathematicalmodel
forbiomass,lacticacidandbacteriocinproductionbylactic
acidbacteriainbatchfermentation.JChemTechBiotechnol.
2008;83:91–96.
2. PancheniakEFR,MazieroMT,Rodriguez-LeonJA,ParadaJL,
SpierMR,SoccolCR.Molecularcharacterizationandbiomass
andmetaboliteproductionofLactobacillusreuteriLPBP01-001:
apotentialprobiotic.BrazJMicrobiol.2012;43:135–147.
3. SuleJ,KorosiT,HuckerA,VargaL.Evaluationofculture
mediaforselectiveenumerationofbifidobacteriaandlactic
acidbacteria.BrazJMicrobiol.2014;45:1023–1030.
4. TurchiB,ManciniS,FratiniF,etal.Preliminaryevaluationof
probioticpotentialofLactobacillusplantarumstrainsisolated
fromItalianfoodproducts.WorldJMicrobiolBiotechnol.
2013;29:1913–1922.
5. YuZ,ZhangX,LiS,LiC,LiD,YangZ.Evaluationofprobiotic
propertiesofLactobacillusplantarumstrainsisolatedfrom
Chinesesauerkraut.WorldJMicrobiolBiotechnol.
2013;29:489–498.
6. RiazS,NawazSK,HasnainS.BacteriocinsproducedbyL.
fermentumandL.acidophiluscaninhibitcephalosporin
resistantE.coli.BrazJMicrobiol.2010;41:643–648.
7. ScapinD,GrandoWF,RossiEM,PerezKJ,MalheirosPS,Tondo
EC.AntagonisticactivityofLactobacillusacidophilusLA10
againstSalmonellaentericaserovarEnteritidisSE86inmice.
BrazJMicrobiol.2013;44:57–61.
8. AppukuttanS,KadirveluJ.Optimizationofnutritionaland
non-nutritionalfactorsinvolvedforproductionof
antimicrobialcompoundsfromLactobacilluspentosusSJ65
usingresponsesurfacemethodology.BrazJMicrobiol.
2014;45:81–88.
9. BianL,MolanAL,MaddoxL,ShuQ.Antimicrobialactivityof
LactobacillusreuteriDPC16supernatantsagainstselectedfood
bornepathogens.WorldJMicrobiolBiotechnol.2011;27:
991–998.
10.ZhangM,ZhangH,LiY,QiW,WangZ,WangJ.Inhibitory
effectofLactobacillusacidophilusonHelicobacterhepaticusin
vitro.WorldJMicrobiolBiotechnol.2013;29:499–504.
11.BendjeddouK,FonsM,StrockerP,SadounD.
Characterizationandpurificationofabacteriocinfrom
Lactobacillusparacaseisubsp.paracaseiBMK2005,an
intestinalisolateactiveagainstmultidrug-resistant
pathogens.WorldJMicrobiolBiotechnol.2012;28:
1543–1552.
12.DidarZ,HaddadKhodaparastMH.Effectofdifferentlactic
acidbacteriaonphyticacidcontentandqualityofwhole
wheattoastbread.JFoodBiosciTechnol.2011;1:
1–10.
13.ZhangT,LiL,WangXF,ZengZH,HuYG,CuiZJ.Effectsof
LactobacillusbuchneriandLactobacillusplantarumon
fermentation,aerobicstability,bacteriadiversityand
ruminaldegradabilityofalfalfasilage.WorldJMicrobiol
Biotechnol.2009;25:965–971.
14.lloriMO,AmundOO,OmidijiO.Shortcommunication:
purificationandpropertiesofaglucose-formingamylaseof
Lactobacillusbrevis.WorldJMicrobiolBiotechnol.
1995;11:595–596.
15.AkolkarSK,SajgureA,LeleSS.Lactaseproductionfrom
Lactobacillusacidophilus.WorldJMicrobiolBiotechnol.
2005;21:1119–1122.
16.NancibA,NancibN,BoudrantJ.Productionoflacticacid
fromdatejuiceextractwithfreecellsofsingleandmixed
culturesofLactobacilluscaseiandLactococcuslactis.WorldJ
MicrobiolBiotechnol.2009;25:1423–1429.
17.GivryS,PrevotV,DuchironF.Lacticacidproductionfrom
hemicellulosichydrolyzatebycellsofLactobacillus
bifermentansimmobilizedinCa-alginateusingresponse
surfacemethodology.WorldJMicrobiolBiotechnol.
2008;24:745–752.
18.QianL.SubmergedfermentationofLactobacillusrhamnosus
YS9for␥-aminobutyricacid(GABA)production.BrazJ
Microbiol.2013;44:183–187.
19.GhalyAE,TangoMSA,MahmoudNS,AveryAC.Batch
propagationofLactobacillushelveticusforproductionoflactic
acidfromlactoseconcentratedcheesewheywith
microaerationandnutrientsupplementation.WorldJ
MicrobiolBiotechnol.2004;20:65–75.
20.VasudhaSh,HariNM.Un-structuredkineticmodelingof
growthandlacticacidproductionbyLactobacillusplantarum
NCDC414duringfermentationofvegetablejuices.LWT–
FoodSciTechnol.2014;59:1123–1128.
21.CockLS,deStouvenelAR.Lacticacidproductionbyastrain
ofLactococcuslactissubslactisisolatedfromsugarcane
plants.ElectJBiotechnol.2006;9:41–45.
22.AmraneA.Analysisofthekineticsofgrowthandlacticacid
productionforLactobacillushelveticusgrowingon
supplementedwheypermeate.JChemTechnolBiotechnol.
2005;80:345–352.
23.Polak-BereckaM,WaskoM,Kordowska-WiaterM,Targonski
Z,Kubik-KomarA.Applicationofresponsesurface
methodologytoenhancementofbiomassproductionby
LactobacillusrhamnosusE/N.BrazJMicrobiol.
2011;42:1485–1494.
24.GuptaS,Abu-GhannamN,ScannellAGM.Growthand
kineticsofLactobacillusplantaruminthefermentationof
edibleIrishbrownseaweeds.FoodBioprodProcess.
2011;89:346–355.
25.PassosFV,FlemingHP,HassanHM,McFeetersRF.Effectof
malicacidonthegrowthkineticsofLactobacillusplantarum.
ApplMicrobiolBiotechnol.2003;63:207–211.
26.AlvarezMM,Aguirre-EzkauriatzaEJ,Ramirez-MedranoA,
Rodriguez-SanchezA.Kineticanalysisandmathematical
modelingofgrowthandlacticacidproductionof
Lactobacilluscaseivar.rhamnosusinmilkwhey.JDairySci.
2010;98:5552–5560.
27.KoizumiK.Chapter3:HPLCofcarbohydratesongraphitized
carboncolumns.JChrom.2002;66:103–119.
28.BerryAR,FrancoCMM,ZhangW,MiddelbergAPJ.Growth
andlacticacidproductioninbatchcultureofLactobacillus
rhamnosusinadefinedmedium.BiotechnolLett.
1999;21:163–167.
29.BustosG,MoldesAB,CruzJM,DominguezJM.Productionof
fermentablemediafromvine-trimmingwastesand
bioconversionintolacticacidbyLactobacilluspentosus.JSci
FoodAgr.2004;84:2105–2112.
30.KimWoojinS,RenJ,DunnNoelW.Differentiationof
Lactococcuslactissubspecieslactisandsubspeciescremoris
strainsbytheiradaptiveresponsetostresses.FEMSMicrobiol