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Industrial
Microbiology
Production
of
mycelial
biomass
by
the
Amazonian
edible
mushroom
Pleurotus
albidus
Larissa
de
Souza
Kirsch,
Ana
Júlia
Porto
de
Macedo,
Maria
Francisca
Simas
Teixeira
∗CultureCollectionDPUA(ParasitologyDepartmentofAmazonasUniversity)/FederalUniversityofAmazonas,Manaus,Amazonas, Brazil
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r
t
i
c
l
e
i
n
f
o
Articlehistory:Received10April2015 Accepted9November2015 Availableonline21April2016 AssociateEditor:GiseleMonteirode Souza Keywords: Pleurotusalbidus Submergedfermentation Mycelialbiomass Factorialdesign
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b
s
t
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Ediblemushroomspeciesareconsideredasanadequatesourceoffoodinahealthydiet duetohighcontentofprotein,fiber,vitamins,andavarietyofminerals.The representa-tivesofPleurotusgenusarecharacterizedbydistinctgastronomic,nutritional,andmedicinal propertiesamongtheediblemushroomscommercializedworldwide.Inthepresentstudy, thegrowthofmycelialbiomassofPleurotusalbiduscultivatedinsubmergedfermentation wasevaluated.Saccharose,fructose,andmaltosewerethethreemaincarbonsourcesfor mycelialbiomassformationwithcorrespondingyieldsof7.28gL−1,7.07gL−1,and6.99gL−1. Inorganicnitrogensourcesdidnotstimulategrowthandtheoptimalyieldwassignificantly higherwithyeastextract(7.98gL−1).Thefactorialdesignusedtoevaluatetheinfluenceof saccharoseandyeastextractconcentration,agitationspeed,andinitialpHindicatedthatall variablessignificantlyinfluencedtheproductionofbiomass,especiallytheconcentration ofsaccharose.Thegreateramountofsaccharoseresultedintheproductionofsignificantly morebiomass.Thehighestmycelialbiomassproduction(9.81gL−1)wasreachedinthe mediumformulatedwith30.0gL−1saccharose,2.5gL−1yeastextract,pH7.0,andaspeed ofagitationat180rpm.Furthermore,P.albidusmanifesteddifferentaspectsof morphol-ogyandphysiologyunderthegrowthconditionsemployed.Mediacompositionaffected mycelialbiomassproductionindicatingthatthediversificationofcarbonsourcespromoted itsimprovementandcanbeusedasfoodorsupplement.
©2016SociedadeBrasileiradeMicrobiologia.PublishedbyElsevierEditoraLtda.Thisis anopenaccessarticleundertheCCBY-NC-NDlicense(http://creativecommons.org/
licenses/by-nc-nd/4.0/).
Introduction
Pleurotus albidus (Berk.) is a speciesthat occurs in Mexico, Argentina, and Brazil. It is glabrous, white to cream col-oredandpresentsinfundibuliformandcircularpileus,deeply
∗ Correspondingauthor.
E-mail:mteixeira@ufam.edu.br(M.F.S.Teixeira).
decurrentlamella,stipeflutedupwardthroughlamellarbases, taperingdownward,usuallycurved-ascendant,dullwhiteand occasionallywithhairsatthebase.1–3ThePleurotusspecies,
commonlyknownasoystermushrooms,havegastronomic, nutritional, and medicinal propertiesand are growninthe temperateandtropicalrainforests.Nowadays,seventyspecies
http://dx.doi.org/10.1016/j.bjm.2016.04.007
1517-8382/©2016SociedadeBrasileiradeMicrobiologia.PublishedbyElsevierEditoraLtda.ThisisanopenaccessarticleundertheCC BY-NC-NDlicense(http://creativecommons.org/licenses/by-nc-nd/4.0/).
ofthis genusare reported, but onlyfew ofthemare com-mercialized,includingP.ostreatus,P.florida,P.sajor-caju,and
P.eryngii.4
Ithaslongbeenknownthatmushroomsdevelopbiomass throughdegradingcelluloseandligninbytheactionofspecific enzymes under optimal conditions.5,6 They can be
culti-vated at large scale using techniques of solid state and submergedcultures.Bothmethodsuseagroindustrialwaste, althoughinsubmergedfermentation,theconditionsare mon-itoredwithgreater precisionwhencomparedtosolid state fermentation.7,8
Submerged fermentation isa viable alternative for effi-cientPleurotusbiomassproduction.Thisprocesshasanumber ofadvantages,suchasa bettercontrolofphysicochemical parameters,aswellasthepotentialforhighbiomass produc-tioninacompactspace,shortergrowthtime,andindependent ofseasonality.9,10
InsubmergedfermentationofPleurotus,nofruitingbody production occurs, and the mycelial biomass develops in two forms: filamentous and pellet. Pellets are character-ized by mycelia development into spherical aggregates, which are a branched and partially intertwined network of hyphae.11,12 The filamentous form consists of hyphae
homogenouslyspreadintheculturemediumwhichismore viscousthanthat ofthe pelletform.Themycelialbiomass produced by submerged fermentation can be used as an inoculum source for mushroom production in semi-solid fermentations,1infoodadditives,andforextractionof antimi-crobialcompounds,flavorings,polysaccharides,antioxidants, etc.10
Aimedatthe improvementofPleurotuscultivation tech-nology, the present study investigated the influence of physicochemicalparametersofsyntheticmediaonmycelial biomassproductionbyP.albidusinsubmergedfermentation.
Material
and
methods
Fungus
P.albidusDPUA1692wasobtainedfromFederalUniversityof AmazonasDPUACultureCollection,Brazil.Allstockcultures were maintained on a potato dextrose agar (PDA) supple-mentedwith0.5%(w/v)yeastextract(YE)(HiMedia,Mumbai, India)slant,subculturedandincubatedat25◦Cforeightdays inthedarkandthenstoredat4◦C.13
Effectofinoculumvolumeonmycelialbiomassproduction
An aqueous homogenate of mycelium, previously sub-cultured on PDA+YE, was prepared using 50mL of sterilized distilled water (per dish) in a blender. Dif-ferent volumes (0.5, 1.0, 2.0, 4.0, and 6.0mL) of the mycelial homogenate were added into Erlenmeyer flasks (125mL) containing 50mL of standard medium (SM): KH2PO4 (1.0gL−1), MgSO4·7H2O (0.5gL−1), peptone
(10.0gL−1), and glucose (20.0gL−1) at pH 6.0. The flasks were incubated for five days at 25◦C, under aerobic conditions at 150rpm, and tests were carried out in triplicate.14
Effectofcarbonandnitrogensourcesonmycelialbiomass
production
Following nutrients were analyzed: glucose,fructose, malt-ose,saccharose,andlactose,ascarbonsources;andpeptone, yeastextract,tryptone,sodiumnitrate andammonium sul-fate,asnitrogensources.TheglucoseandpeptoneintheSM werereplacedseparatelyaccordingtothecarbonandnitrogen sourcesmentioned.Theaqueoushomogenateofmycelium (6.0mL)wasaddedtotheflasks,andsubmergedfermentation wasperformedasmentionedabove.
Determinationofdrycellmass
Attheendoffermentation,biomasswascollectedbyvacuum filtration,washedthreetimeswithdistilledwater,anddried at70◦Cfordry-weightquantification.15
Determinationoftotalcarbohydrates
Thetotalcarbohydrateconcentrationwasdetermined colori-metricallybythephenol-sulfuricacidmethodaccordingtothe protocoldescribedbyDuboisetal.16
Conversionfactorofsubstratetobiomass,yieldand
productivity
Theconversionfactorofsubstratetobiomassandtheyield and productivity were calculated according to Confortin etal.17
The conversion factor of substrate to biomass was expressedingramsofmycelialbiomassproducedpergram ofsubstrateconsumed(gg−1):
Y(X/S)=XSf−Xi
i−Sf
(1) whereXfandXiarefinalandinitialbiomassconcentration,
respectively,andSiandSfareinitialandfinalsugar
concen-tration,respectively.
Theyieldwasexpressedingramsofmycelialbiomass pro-ducedpergram ofsubstrate initiallypresentintheculture medium(gg−1):
Y(r/S)=XfS−Xi i
(2) Theproductivity in biomasswas expressedin gramsof mycelialbiomassproducedpertime(gL−1h−1)17:
PX= Xf−t Xi (3)
wheretistheincubationtime.
Factorialdesignandstatisticalanalysis
A24 factorialdesignwasusedtoevaluatesaccharose
con-centration,yeastextractconcentration,agitationspeed,and initialpH(independentvariables)onmycelialbiomass pro-duction (dependent variable).18 In previous experiments,
saccharoseand yeastextractwere selectedasthebest car-bon and nitrogen sources, respectively. SM was used with saccharoseandyeastextractatdifferentexperimental con-centrations. Submerged fermentation was conducted, and thebiomassquantifiedasdescribedpreviously.Allstatistical analyseswereperformedviaStatistic8.0software.
All results of the submerged fermentation experiments weresubjectedtovarianceanalysis(one-wayANOVA),andthe valueswerecomparedbyTukey’stestatp≤0.05.
Morphologyofthemycelialbiomass
Themorphologyofthemycelialbiomassproducedunderthe factorialdesignwas evaluated usingthe software Analysis FIVEOlympusand astereomicroscope(OlympusSZ61,Ltd., Tokyo,Japan).Thesampleswerefixedwithasolution com-posedof13mLof40%(v/v)formaldehyde,5mLofaceticacid, and200mLof50%(v/v)ethanol.19
Results
and
discussion
Effectofinoculumsize
Mycelialbiomassproductionvariedsignificantlydepending ontheinoculumsize(Fig.1).Thevolumeof6.0mLinduced higherbiomassproduction(5.00gL−1).Therefore,thisvolume wasusedforfurtherexperiments.
IninvestigationsonP.tuber-regium14andGrifolafrondosa,20
theinoculumsizewithacellsuspensionvolumerangingfrom 0.5to12.0mL,or2to6%,hadahigherpositiveinfluenceon mycelialgrowthincomparisontothemediumvolumein sub-mergedfermentation.
Effectofcarbonandnitrogensources
AllcarbonsourcestestedpromotedP.albidusgrowth(Table1). However, saccharose (7.28gL−1), fructose (7.07gL−1), and maltose(6.99gL−1)were thecarbon sourcesthatpromoted the most considerable growth. Although the mushroom manifestedthe highestmycelialbiomassproductioninthe
e d c b a 0 1 2 3 4 5 6 7 8 6.0 4.0 2.0 1.0 0.5 M y celial biom ass (g .L –1 ) Inoculum volume (mL)
Fig.1–EffectofdifferentinoculumsizeonP.albidus
mycelialbiomassproduction.Meansfollowedbythesame letter(s)arenotsignificantlydifferent,asestablishedby Tukey’stest(p≤0.05).
treatmentwithsaccharose,theconsumptionofthissugar dur-ing the fermentationprocess wastwicelower than thatof fructose.Thisresultmighthavebeencausedbythenatureof thecarbonsource,becausesaccharoseisadisaccharidewhich isnecessaryforinvertaseexcretion,andafterdecomposition intoglucoseandfructose,itcanbeabsorbedbythefungus.27
Monosaccharides, suchasfructoseand glucose,are car-bon sources that stimulate Pleurotus growth in submerged fermentation.21,22 However, the preference for saccharose
as a carbon source has also been reported for Antro-dia cinnamomea,23 Cordyceps militaris,24 C. sinensis,15 and C.
jiangxiensis.25Consideringcostsandeaseofproduction,
sac-charosecanbeconsideredamoresuitablesubstratecompared toothersyntheticsourcesavailableonthemarket.
In our study, saccharose was more efficiently con-verted into biomass (1.15gg−1) with a higher productivity (0.061gL−1h−1), whereas biomass and productivity were 0.86gg−1and0.059gL−1h−1,respectively,forfructose.These
Table1–Mycelialbiomass,conversionfactorofsubstratetobiomass(YX/S),yield(Yr/S)andproductivity(PX)ofP.albidus
underdifferentcarbonandnitrogensources.
Sources Mycelialbiomass(gL−1) YX/S(gg−1) Yr/S(gg−1) PX(gL−1h−1) FinalpH
Carbon Saccharose 7.28a 1.15a 0.36a 0.061a 5.19a Fructose 7.07a 0.86b 0.35a 0.059a 5.05b Lactose 6.23c 0.65d 0.31c 0.052c 5.21a Maltose 6.99a 0.79c 0.35a 0.058a 5.00b Glucose(basal) 6.56b 0.43e 0.33b 0.055b 5.06b Nitrogen Yeastextract 7.98a 0.42a 0.40a 0.066a 5.45a Tryptone 7.19b 0.39b 0.36b 0.060b 4.70c Ammoniumsulfate 1.39d 0.24c 0.07d 0.012d 3.33d Sodiumnitrate 0.79e 0.11d 0.04e 0.007e 4.62c Peptone(basal) 6.56c 0.43a 0.33c 0.055c 5.06b
valueswerehigherthanthosereportedforPleurotussajor-caju
(0.82gg−1and0.085gL−1h−1)inaliquidmediumcontaining aninitialconcentrationof10gL−1glucoseand0.59gg−1and 0.041gL−1h−1for10gL−1saccharose.17
Theaddition of sodium nitrate and ammonium sulfate in the culture media did not favor mycelial biomass pro-duction. Themaximum values of biomassformation were 0.79and1.39gL−1,respectively(Table1).Thesefindingsare inaccordance withthose obtained forC. militaris24 and G.
frondosa.20Overall,itseemsthatinorganicnitrogendoesnot
promotegrowthofseveralfungispecies,incontrasttoorganic sources.24,26
Deacon27 describes that as a result of ammonia
metabolism,H+ionsarereleased,andthepHofthemedium
isreduced,inhibitingthegrowthofsomemushroomspecies. This was alsoobserved when, atthe end of fermentation process,thepHofculturemediainwhichammoniumsulfate andsodiumnitratewereutilizedwasbelow4.6(Table1).
OurresultsindicatedthatYE(7.98gL−1)wasthenitrogen sourcethatstimulatedmostpronouncedlymycelialbiomass production,whichwasduetopresenceofseveralother nutri-ents,includingcarbonsources,growthfactors,andvitamins presentinYE.ThebiomassofP.albiduswashigherinthe cul-turemediumcontainingYE,andthevaluesobtainedforyield andproductivity were 0.40gg−1 and0.066gL−1h−1, respec-tively,whichweresignificantlyhigherwhencomparedwith theothernitrogensourcesevaluated.However,nostatistical differences(p≤0.05)were observedbetween the valuesfor yeastextractandcontrolconcerningthevaluesofthe con-versionfactorofsubstratetobiomass.
Thepresenceoftryptone(7.19gL−1)andpeptone(6.56gL1)
inculturemediaalsofavoredbiomassproductionwith val-ues thatwere statisticallydifferent (p≤0.05) from those of theinorganic sourcesofnitrogen.Various organic nitrogen sourceshavebeenreportedassuitableformushroomsgrowth, includingmeatpeptone,polypeptone,yeastextract,and soy-beanconcentrates.20,23,28
Factorialdesign
Thevariablesandtheresultsobtainedfromtherunsofthe24
fullfactorialdesignarelistedinTable2.Themycelialbiomass productionrangedfrom3.92gL−1to9.81gL−1representedby runs3and12,respectively.
Thecontrastvalueswerecalculatedforeachofthe vari-ablesandtheirinteractionsfromtheexperimentsoffactorial design(Table3).Allvariableshadasubstantialinfluenceon mycelialbiomassproduction,and,intermsoftheirimpact, theycan be classified inthe following decreasing order of significance:saccharoseconcentration,agitationspeed,yeast extractconcentration,andpH.Forthefirstthreevariablesthe effectwaspositive,whichindicatedthattheincreaseofthis lowerleveltothehigherlevelfavoredbiomassproductionof
P.albidusinthefermentationprocess.ThepHwasalso signif-icantforthisresponse;however,thenegativeeffectshowed thatthereductionoftheinitialpHpromotedmorefavorable conditionsforproductionofmycelialbiomass.The interac-tionsofpHandagitationspeed,andsaccharoseconcentration andagitationspeedonthehigherlevel,alsofavoredP.albidus
growth.
Table2–Resultsofthefullfactorialdesign24for
mycelialbiomassproductionbyP.albidus.
Runs Sca YEcb pH Asc Mycelialbiomass(gL−1)
1 10.0 2.5 5.0 120 4.52 2 10.0 2.5 5.0 180 5.47 3 10.0 2.5 7.0 120 3.92 4 10.0 2.5 7.0 180 5.37 5 10.0 10.0 5.0 120 6.70 6 10.0 10.0 5.0 180 5.72 7 10.0 10.0 7.0 120 5.21 8 10.0 10.0 7.0 180 5.11 9 30.0 2.5 5.0 120 6.87 10 30.0 2.5 5.0 180 6.49 11 30.0 2.5 7.0 120 5.24 12 30.0 2.5 7.0 180 9.81 13 30.0 10.0 5.0 120 7.53 14 30.0 10.0 5.0 180 9.26 15 30.0 10.0 7.0 120 6.59 16 30.0 10.0 7.0 180 9.56 17d 20 5.0 6.0 150 7.47 18d 20 5.0 6.0 150 7.34 19d 20 5.0 6.0 150 7.41 a Sc,saccharoseconcentration(gL−1). b YEc,yeastextractconcentration(gL−1). c As,agitationspeed(rpm).
d Centralpoints.
Thehighestbiomassproductionwas9.81gL−1,as deter-minedinrunnumber12withtheculturemediumformulated withsaccharose(30.0gL−1), yeastextract(2.5gL−1), pH7.0, and an agitation speed of 180rpm. An R-square value of 0.9341wasobtainedforthebiomass,indicatingthatthemodel explainedapproximately93%ofthevariabilitydata.
Park et al.11 evaluated the influence of different
phys-icochemical parameters on the growth and production of polysaccharides by submerged fermentation in another mushroomspecies(C.militaris).Theirresultsindicatedthat
Table3–Contrastvaluescalculatedaccordingtofactorial designofP.albidusmycelialbiomassproduction.
Variables Contrasts
(1)Saccharoseconcentration 120.75±1.06+
(2)Yeastextractconcentration 49.90±1.06+
(3)pH −11.00±1.06+ (4)Agitationspeed 63.75±1.06+ Interaction1-2 6.64±1.06 Interaction1-3 24.03±1.06+ Interaction1-4 47.25±1.06+ Interaction2-3 −23.34±1.06+ Interaction2-4 −18.50±1.06+ Interaction3-4 47.26±1.06+ Interaction1-2-3 −5.90±1.06+ Interaction1-2-4 24.93±1.06+ Interaction1-3-4 30.14±1.06+ Interaction2-3-4 −20.93±1.06+
+ Statisticallysignificantvaluesata95%confidencelevel.
Thestandarderrorsareestimatedfromthereplicaterunsatthe centralpoint.Theerrorisdescriptivearoundofthecontrast esti-mate,aftersymbol±.
Fig.2–Pelletmorphologyunderdifferentcultureconditions.(A)Run11,(B)Run5,(C)Run8,(D)Run9,(E)Run12and(F) Run14ofthefactorialdesign.
amongthecarbonsourcestested,saccharosealsoexerteda favorableeffectonmycelialgrowth.Thegrowthwas propor-tionaltotheincreaseoftheinitialconcentrationofthiscarbon source,rangingfrom 10gL−1to60gL−1 andexpressingthe maximumgrowthinthemediumcontaining60gL−1of sac-charose.
AccordingtoTangetal.,5theagitatedculturemedium
pro-motedproperhomogenizationofcomponents,increasedthe oxygenation,andimprovedthemassandheattransfer.These conditionshad apositiveinfluenceon mushroommycelial growthbysubmergedfermentation.Nevertheless,extremely highagitationspeedsmay alsocause shearforcesthatcan damagethehyphae,causingchangesinthemycelium, vari-ationsingrowthrate,andinterferewithproductformation. Theagitationspeedof180rpminP.albiduscultureswasthat themostsuitableforthemycelialgrowthincomparisontothe othersspeedstested.Theseresultsdifferfromthoseobtained byKimetal.29whoevaluatedtheeffectofagitationspeedand
aerationonthemycelialgrowthofGanodermaresinarum.The authorsreportedthatwhenagitationspeedincreasedfrom50 to250rpm,biomassproductionwasreducedbyapproximately 30%(from12.7gL−1to8.9gL−1).
TheuseofYEasanitrogensourceintheculturemedium toevaluatebiomassproductionbyG.frondosawasreported.20
Theauthorsevidencedthatthebiomassincreasedasthe con-centrationofthenitrogensourcewaselevatedintheculture medium;andtheyeastextractconcentrationof6gL−1was optimalforbiomassproduction.Anumber ofstudies have indicatedthatmushrooms,whengrownundertheconditions ofsubmergedfermentation,havepreferencefororganic nitro-gensources,suchasyeastextractandpeptoneratherthan fortheinorganic ones.30,31 Gbolagade etal.32 reportedthat
thispreferencemaybeexplainedbythecomplex combina-tionofaminoacidsandcarbohydratespresentintheseorganic compounds,resultingintheenhancedfungalgrowth.
FermentationmediumpHisanextremelyimportant vari-ableinthegrowthoffungi,asitaffectsthefunctionofthe
cellmembrane,thestructure,andcellularmorphology,aswell astheprocessesofuptakeofvariousnutrientsandproduct biosynthesis.27,33Inthisresearch,theresultsindicatedthat,in
general,theuseoflowerinitialpHinculturemediumfavored
P.albidusgrowth.Attheendofthefermentationprocess,the pHremainedconstantintheculturemediawheretheinitial pHwas5.0.However,whenthefungusstarteditsgrowthat initialpH7.0,therewasareductiontopH5.0.Accordingto Papagianni,33culturemediumcompositionmayaffectthe
ini-tialculturemediumpHcausingfluctuationsinthepHrange duringfungalgrowth.
Morphologicalobservationsofmyceliuminsubmerged
fermentation
Znidarsic and Pavko34 and Kim et al.29 reported that the
characteristicsofthemyceliumproducedbysubmerged fer-mentationareinfluencedbycultureconditions,suchasthe compositionandinitialpHofthefermentationmedium,the ageandsizeofinoculum,aerationrate,andagitationspeed.
Theformationofpelletswithdifferentsizesand morphol-ogywereobservedinallfermentationconditions.Thesepellet characteristicsweremoreevidentaftervariationinthe agi-tationspeed,followingthealterationsintheinitialpHofthe culturemedium.Whentheprocesswasperformedat120rpm, thepelletswerelargeandfewinnumbers,whereasat180rpm, theybecamesmallerinsizeandlargerinquantity.The varia-tioninthesizeofpelletsunderdifferentagitationconditions wasalsoreportedbyotherauthors.29Theyobservedthe
pres-enceoflargepelletswhenGanodermaresinaceumwassubjected toanagitationspeedof50rpm,whereasundermore vigor-ousagitation(300rpm),pelletsbecamesmallattheendofthe fermentationprocess.
At120rpmandpH7.0,growthofelongatedandprotruding hyphae onthe surfaceofthepelletswasobserved(Fig.2a). Under fermentationconditionsofpH5.0,theextensionsof thesehyphaeexhibitedmorereducedlengthorwereabsent
(Fig.2bandd).InastudyperformedbyHwangetal.,35the
authorsverifiedthatPhellinusbaumiigrowninaliquidmedium producedpellets withastarfish-like appearanceata more acidic pH. However, when the pH of the culture medium rangedfromneutraltoalkaline,pelletsbecamemorecompact, andnofreemyceliumwasavailable.
Inculturesperformedatahigheragitationspeed(180rpm), exceptforrunno.6,pelletswerepresent,and,ingeneral, elon-gatedhyphaewereobservedonthesurface.AtpH7.0(Fig.2c ande),hyphaearoundthepelletsweremorenumerousthan atpH5.0(Fig.2f).
Similar resultswere alsoobtained byParket al.,11 who
reported that the pellets of C. militaris formed during the fermentationperiodincreasedinsizeindependentlyofthe agitation speed. Nonetheless, when the fermentation was conducted under low agitation speed (50rpm), the pellets becamelarge andfluffy, whereas atahighagitation speed (300rpm),theouterhairyregionsofthepelletswereremoved and,consequently,becamesmallerandchangedtoacircular shape.
Duringthe fermentationprocess,P. albidusbiomasswas observed to adhere strongly to the inside walls of the Erlenmeyer flasksin all growth conditions evaluated. This phenomenonwasalsoobservedinpreviousinvestigationson submergedfermentationofGanodermalucidum,inwhichthe authorsreportedbiomassadherenceduetothe polysaccha-ridesproduction.36
Whenestablishingarelationshipbetweentheproduction andbiomassmorphologyofP.albidus,highermycelialbiomass productionwasfoundwhenthepelletsweresmallinsizewith shorthyphae.
Conclusion
Theresultsobtainedinthisstudyelucidatedsomeimportant aspectsofthemorphologyandphysiologyofP.albidus.These findingscanbeconsideredpioneeringfortheproductionof mycelialbiomassofthismushroombysubmerged fermen-tation.Thecomponentsoftheculturemedia,includingthe concentrationandtypeofcarbonandnitrogensources,initial pH,inoculumvolume,andagitationspeedaremainfactors thatsignificantlyaffectbiomassproduction.The experimen-tal design was an effective tool for evaluating the culture factorsthatmostinfluencedthegrowthandmorphologyof themushroombiomass.Thisinformationmaybeusefulfor theproductionofP.albidusmycelialbiomassforhuman con-sumption.
Conflicts
of
interest
Theauthorsdeclarenoconflictsofinterest.
Acknowledgements
Theauthorsacknowledgethetechnicalandfinancialsupport grantedbytheCultureCollectionDPUAandCoordenac¸ãode Aperfeic¸oamentodePessoaldeNívelSuperior(Capes)/Brazil.
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