食品专业英文论文.docx
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食品专业英文论文.docx
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食品专业英文论文
ExtractionofanthocyaninsfromredcabbageusinghighpressureCO2
ZhenzhenXua,b,c,JihongWua,b,c,YanZhanga,b,c,XiaosongHua,b,c,XiaojunLiao
a,b,c,
andZhengfuWanga,b,c
aCollegeofFoodScienceandNutritionalEngineering,ChinaAgriculturalUniversity,Beijing100083,China
bKeyLaboratoryofFruitandVegetableProcessing,MinistryofAgriculture,Beijing100083,China
cResearchCenterforFruitandVegetableProcessingEngineering,MinistryofEducation,Beijing100083,China
Received24November2009;
revised30March2010;
accepted2April2010.
Availableonline24April2010.
Abstract
TheextractionkineticsofanthocyaninsfromredcabbageusinghighpressureCO2(HPCD)againstconventionalacidifiedwater(CAW)wasinvestigated.TheHPCDtime,temperature,pressureandvolumeratioofsolid–liquidmixturevs.pressurizedCO2(R(S+L)/G)exhibitedimportantrolesontheextractionkineticsofanthocyanins.Theextractionkineticsshowedtwophases,theyieldincreasedwithincreasingthetimeinthefirstphase,theyielddefinedassteady-stateyield(y*)wasconstantinthesecondphase.They*ofanthocyaninsusingHPCDincreasedwithhighertemperature,higherpressureandlowerR(S+L)/G.Thegeneralmasstransfermodelwithhigherregressioncoefficients(R2>0.97)fittedthekineticdatabetterthantheFick’ssecondlawdiffusionmodel.AscomparedwithCAW,thetime(t*)toreachthey*ofanthocyaninsusingHPCDwasreducedbyhalfwhileitscorrespondingoverallvolumetricmasstransfercoefficientskL×afromthegeneralmasstransfermodelincreasedbytwofolds.
Keywords:
Redcabbage;Anthocyanins;HighpressureCO2;Thegeneralmasstransfermodel;TheFick’ssecondlawdiffusionmodel
Nomenclature
CAW
conventionalacidifiedwater
HPCD
highpressureCO2
FW
freshweight
A519
absorbanceat519nm
A519(pH1.0)
A519inpH1.0buffer
A519(pH4.5)
A519inpH4.5buffer
A
A519(pH1.0)−A519(pH4.5)
Mw
molecularweightofanthocyanin(=433.2g/mol)
DF
dilutionfactor(=10)
Ε
extinctioncoefficient(=31,600Lcm−1mol−1)
L
pathlength(=1cm)
V
finalvolumeofanthocyaninsliquidextracts(L)
M
weightofredcabbage(g)
V(S+L)
volumeofsolid–liquidmixture(mL)
VG
volumeofpressurizedCO2(mL)
VL
volumeofacidifiedwater(mL)
R(S+L)/G
volumeratioofsolid–liquidmixturevs.pressurizedCO2
T
time(minors)
Y
yieldofanthocyaninsinbulkliquidatgiventime(mg/100gFW)
y*
steady-stateyield(mg/100gFW)
t*
extractiontimetoreachy*(min)
kL×a
overallvolumetricmasstransfercoefficient(s−1)
S/L
ratioofsolidtoliquid(g/mL)
C
concentrationofsolute(mg/g)
D
diffusioncoefficientordiffusivity(m2s−1)
X
distanceofdiffusion(m)
Cs
concentrationofanthocyaninsinsolidphaseatgiventime(mg/g)
Cs,0
initialconcentrationofanthocyaninsatt=0(mg/g)
Cs,i
concentrationofanthocyaninsatgiventimet(mg/g)
steady-stateconcentrationofanthocyaninsatt
t*(mg/g)
Deff
effectivediffusivity(m2s−1)
λ
functionofradius(m−2)
v/v
volumetovolume
v/v/v
volumetovolumetovolume
RM
massratioofpressurizedCO2vs.solid–liquidmixture
R2
regressioncoefficient
DCO2
CO2density(g/mL)
SCO2
CO2solubility(g/100g)
Dwater
waterdensity(g/mL)
ML
massofwater(g)
MG
massofpressurizedCO2
RM
massratioofpressurizedCO2tosolid–liquidmixture
ArticleOutline
Nomenclature
1.
Introduction
2.
Methods
2.1.Preparationofredcabbage
2.2.Quantificationofanthocyanins
2.3.Extractionexperiments
2.3.1.HPCDextraction
2.3.2.CAWextraction
3.
Kineticmodels
3.1.Thegeneralmasstransferkineticmodel
3.2.TheFick’ssecondlawdiffusionmodel
4.
Resultsanddiscussion
4.1.Effectoftheextractiontimeontheyieldofanthocyanins
4.2.Effectoftheextractiontemperatureonthesteady-stateyieldy*ofanthocyanins
4.3.Effectoftheextractionpressureonthesteady-stateyieldy*ofanthocyanins
4.4.EffectoftheextractionR(S+L)/Gonthesteady-stateyieldy*ofanthocyanins
4.5.Modelingtheextractionkineticsofanthocyaninsfromredcabbage
5.
Conclusions
Acknowledgements
References
1.Introduction
Redcabbage(BrassicaoleraceaL.var.capitataf.rubra)belongstothefamilyofBrassicaceae,whichisanativevegetableoftheMediterraneanregionandsouthwesternEurope(Arapitsasetal.,2008).Recently,ithasattractedmuchattentionbecauseofitsphysiologicalfunctionsandapplications.Anthocyaninsrichinredcabbageseemtoberesponsibleforthoseproperties(McDougalletal.,2007).
Anthocyaninsareglycosidesofpolyhydroxyandpolymethoxyderivativesof2-phenylbenzopyryliumorflavyliumsalts(MazzaandMiniati,1993).Besidesgivingcolortoplants,anthocyaninsalsohaveanarrayofhealth-promotingbenefits,astheycanprotectagainstavarietyofoxidantsthroughavariousnumberofmechanisms(Kongetal.,2003).Healthbenefitsassociatedwithanthocyaninsincludeenhancementofsightacuteness,antioxidantcapacity,treatmentofvariousbloodcirculationdisordersresultingfromcapillaryfragility,vaso-protectiveandanti-inflammatoryproperties,inhibitionofplateletaggregation,maintenanceofnormalvascularpermeability,controllingdiabetes,anti-neoplasticandchemoprotectiveagents,radiation-protectiveagents,andpossiblyothersduetotheirdiverseactiononvariousenzymesandmetabolicprocesses(GiustiandWrolstad,2003).Twenty-fouranthocyaninshavebeenseparatedandidentifiedinredcabbage,allhavingcyanidinasaglycon,representedasmono-and/ordi-glycoside,andacylated,ornot,witharomaticandaliphaticacids(Arapitsasetal.,2008).
Anthocyaninsaresolubleinpolarsolvents,andtheyarenormallyextractedfromplantmaterialsbyusingmethanolthatcontainssmallamountofhydrochloricacidorformicacid(Kongetal.,2003).Theextractionwithmethanolis20%moreeffectivethanwithethanol,and73%moreeffectivethanonlywaterinanthocyaninsextractionsfromgrapepulp(Metivieretal.,1980).Acetonehasalsobeenusedtoextractanthocyaninsfromseveralplantsources,whichallowsanefficientandmorereproducibleextraction,avoidingproblemswithpectins,andpermitsamuchlowertemperatureforthesameconcentrationcomparedwithclassicalacidifiedaqueousormethanolicsolvents(Garcia-Vigueraetal.,1998).Nowadays,theresiduesoforganicsolventssuchasmethanolandacetoneinthesemethodsareassociatedwithfoodsafety,sotheorganicsolventsarelimitedinfoodindustry.However,theconventionalacidifiedwater(CAW)extractionofanthocyaninsistime-consumingandinefficient,andhigherextractiontemperaturescausethedegradationofanthocyanins.Moreover,smallamountofacids,suchashydrochloricacidorformicacid,mayalsocausepartialortotalhydrolysisoftheacylmoietiesofacylatedanthocyaninspresentinsomeplants(Kongetal.,2003).Therefore,itisakeyfocustodevelopnewextractionmethodswithfasterextractionratesandhigheryieldsinanthocyaninsextraction.Luque-Rodríguezetal.(2007)optimizedtheextractionconditionofanthocyaninsusingdynamicsuperheatedliquidextraction.ArapitsasandTurner(2008)proposedtheextractionofanthocyaninsfromredcabbageusingpressurizedsolventextraction.Corralesetal.(2009)studiedthehighhydrostaticpressureextractionofanthocyaninsfromgrapeskins.Thesestudies([Arapitsasetal.,2008],[Luque-Rodríguezetal.,2007]and[Corralesetal.,2009])indicatethatraisingextractionpressuremaybeanewmethodtoimproveextractionyieldandincreaseextractionrate.
CO2isanontoxicagentwithoutposinganyproblemsassociatedwithfoodsafety.TheexplosiveeffectofhighpressureCO2(HPCD)isfirstlydemonstratedtodisruptbacterialcellsbytherapidreleaseofgaspressurewiththeaimofcollectingcellcontents,numerousstudieshaveshowedtheefficacyofHPCDtoinactivatemicroorganismsandenzymesinbatch,semi-continuous,andcontinuoussystems([Balabanetal.,1991],[Yoshimuraetal.,2002]and[Kincaletal.,2006]).Withaneyeonthesimilarityindisruptingcellstructurebetweenmicrobialinactivationandsolid–liquidextraction,itisdeducedthatHPCDalsostrengthenedextractionprocessbyitssuperiorabilitiesincellmembranemodification,intracellularpHdecrease,disorderingoftheintracellularelectrolytebalance,removalofvitalconstituentsfromcellsandcellmembranes.However,thereisnostudyonHPCD-assistedextractionofanthocyaninstodate.LimitedstudiesinliteratureregardingtheeffectofHPCDonqualityofanthocyanin-containingfruitjuicesareavailable.DelPozo-Insfranetal.(2006)reportedthatnosignificantchangewasfoundinthetotalanthocyanincontent(TAcy)formuscadinegrapejuicespasteurizedbyHPCD.Tiwarietal.(2009)alsopointedoutthathighhydrostaticpressureandHPCDcausednodegradationofanthocyanins.
Kineticdataofextractionwerethemostimportantinformationinunderstandingtheextractionprocess.Thegeneralmasstransferkineticmodelandthediffusionmodelcanfitthenormalsolid–liquidextractionswell([CacaceandMazza,2003],[Seikovaetal.,2004],[Handayanietal.,2008]and[Heetal.,2008]).Inthisstudy,HPCDasanovelassisted-extractiontechniquewasusedtheextractionofanthocyaninsfromredcabbageforthefirsttime,theeffectsoftheimportantparameterssuchastheextractiontime,temperature,pressureandvolumeratioofsolid–liquidmixturevs.pressurizedCO2(R(S+L)/G)ontheextractionkineticswasdiscussed.TheextractionkineticswasfittedtothegeneralmasstransferkineticmodelandtheFick’ssecondlawdiffusionmodelforbetterunderstandingtheHPCDextractionprocess.
2.Met
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