HAL Id: hal-02921485
https://hal.inrae.fr/hal-02921485
Submitted on 26 Aug 2020
HAL is a multi-disciplinary open access archive for the deposit and dissemination of sci- entific research documents, whether they are pub- lished or not. The documents may come from teaching and research institutions in France or abroad, or from public or private research centers.
L’archive ouverte pluridisciplinaire HAL, est destinée au dépôt et à la diffusion de documents scientifiques de niveau recherche, publiés ou non, émanant des établissements d’enseignement et de recherche français ou étrangers, des laboratoires publics ou privés.
Distributed under a Creative Commons Attribution| 4.0 International License
Standardized protocol for determination of biohydrogen potential
Julian Carrillo-Reyes, German Buitron, Iván Moreno-Andrade, Aida Cecilia Tapia-Rodríguez, Rodolfo Palomo-Briones, Elías Razo-Flores, Oscar Aguilar-Juárez, Jorge Arreola-Vargas, Nicolas Bernet, Adriana Ferreira Maluf
Braga, et al.
To cite this version:
Julian Carrillo-Reyes, German Buitron, Iván Moreno-Andrade, Aida Cecilia Tapia-Rodríguez, Rodolfo
Palomo-Briones, et al.. Standardized protocol for determination of biohydrogen potential. MethodsX,
Elsevier, 2020, 7, pp.100754. �10.1016/j.mex.2019.11.027�. �hal-02921485�
Protocol Article
Standardized protocol for determination of biohydrogen potential
Julián Carrillo-Reyes
a,*, Germán Buitrón
a,
Iván Moreno-Andrade
a, Aida Cecilia Tapia-Rodríguez
b, Rodolfo Palomo-Briones
b, Elías Razo-Flores
b,
Oscar Aguilar-Juárez
c, Jorge Arreola-Vargas
d, Nicolas Bernet
e, Adriana Ferreira Maluf Braga
f, Lucia Braga
g, Elena Castelló
g, Lucile Chatellard
e, Claudia Etchebehere
h, Laura Fuentes
h, Elizabeth León-Becerril
c, Hugo Oscar Méndez-Acosta
i, Gonzalo Ruiz-Filippi
j, Estela Tapia-Venegas
j, Eric Trably
e, Jorge Wenzel
h, Marcelo Zaiat
faLaboratoryforResearchonAdvancedProcessesforWaterTreatment,InstitutodeIngeniería,Unidad AcadémicaJuriquilla,UniversidadNacionalAutónomadeMéxico,Blvd.Juriquilla3001,Queretaro,76230, Mexico
bDivisióndeCienciasAmbientales,InstitutoPotosinodeInvestigaciónCientíficayTecnológicaA.C.,Caminoa laPresaSanJoséNo.2055,Col.Lomas4aSección,C.P.78216,SanLuisPotosí,SLP,Mexico
cDepartmentofEnvironmentalTechnology,CentrodeInvestigaciónyAsistenciaenTecnologíayDiseñodel EstadodeJalisco,A.C.,Av.Normalistas800,Col.ColinasdelaNormal,C.P.44270,Guadalajara,Jalisco,Mexico
dDivisióndeProcesosIndustriales,UniversidadTecnológicadeJalisco,LuisJ.JiménezNo.577,1odeMayo,C.
P.44979,Guadalajara,Jalisco,Mexico
eINRAE,Univ.Montpellier,LBE,Narbonne,France
fBiologicalProcessLaboratory,SãoCarlosSchoolofEngineering,UniversityofSãoPaulo(LPB/EESC/USP),Av.
JoãoDagnone1100,SãoCarlos,SãoPaulo,13563-120,Brazil
gLaboratorioBioProA,FacultaddeIngeniería,UniversidaddelaRepúblicadeUruguay,Av.JulioHerreray Reissig565,Montevideo,Uruguay
hLaboratoriodeEcologíaMicrobiana,DepartamentodeBioquímicayGenómicaMicrobiana,Institutode InvestigacionesBiológicasClementeEstable,Av.Italia3318,Montevideo,Uruguay
iDepartamentodeIngenieríaQuímica,CUCEI-UniversidaddeGuadalajara,Blvd.M.GarcíaBarragan1451,C.P.
44430,Guadalajara,Jalisco,Mexico
jEscueladeIngenieríaBioquímica,FacultaddeIngeniería,PontificiaUniversidadCatólicadeValparaíso,Av.
Brasil2085,Valparaíso,Chile
DOIoforiginalarticle:http://dx.doi.org/10.1016/j.ijhydene.2019.08.124
*Correspondingauthor.
E-mailaddress:JCarrilloR@ii.unam.mx(J.Carrillo-Reyes).
http://dx.doi.org/10.1016/j.mex.2019.11.027
2215-0161/©2019TheAuthors.PublishedbyElsevierB.V.ThisisanopenaccessarticleundertheCCBYlicense(http://
creativecommons.org/licenses/by/4.0/).
ContentslistsavailableatScienceDirect
MethodsX
journal homepage:www.elsevier.com/locate/mex
ABSTRACT
Biohydrogenproductionpotential(BHP)dependsonseveralfactorslikeinoculumsource,substrate,pH,among manyothers.Batchassaysarethemostcommonstrategytoevaluatesuchparameters,wherethecomparisonisa challengingtaskduetothedifferentproceduresused.Thepresentmethodintroducesthefirstinternationally validatedprotocol,evaluatedby8independentlaboratoriesfrom5differentcountries,toassessthebiohydrogen potential.Asqualitycriteria,acoefficientofvariationofthecumulativehydrogenproduction(Hmax)wasdefined
tobe<15%.TwooptionstorunBHPbatchtestswereproposed;amanualprotocolwithperiodicmeasurementsof
biogasproduction,needingconventionallaboratorymaterialsandanalyticalequipmentforbiogascharacteriza- tion;andanautomaticprotocol,whichisruninadevicedevelopedforonlinemeasurementsoflowbiogas production.Thedetailedproceduresforbothprotocoloptionsarepresented,aswellasdatavalidatingthem.The validation showed acceptable repeatability and reproducibility, measured as intra- and inter-laboratory coefficientofvariation,whichcanbereducedupto9%.
©2019TheAuthors.PublishedbyElsevierB.V.ThisisanopenaccessarticleundertheCCBYlicense(http://
creativecommons.org/licenses/by/4.0/).
ARTICLE INFO
Protocolname:Biohydrogenpotentialprotocol
Keywords:Automaticprotocol,Darkfermentation,Heat-treatedinoculum,Manualprotocol Articlehistory:Received25October2019;Accepted29November2019;Availableonline4December2019
SpecificationTable
SubjectArea: EnvironmentalScience Morespecificsubject
area:
Biofuelsproduction
Protocolname: Biohydrogenpotentialprotocol Reagents/tools: Requiredreagents
NH4Cl
MES(2-(N-Morpholino)ethanesulfonicacid,4-Morpholineethanesulfonicacid) MgCl26H2O
FeSO47H2O CoCl26H2O MnCl24H2O KI NiCl26H2O ZnCl2
Anhydrousglucose HCl(37%) NaOH
Thymolphthalein(onlyfortheautomaticversion) Distilledwater
Requiredmaterialsandequipment
10-mLgraduatedpipettesoranairdisplacementpipette(110mL)withtips Spatula
pHmeter Pasteurpipettes
Digitalanalyticalbalance(readabilitydownto0.1mg)
Industrialblender,electriccoffeegrinderorporcelainmortarandpestle Standardmesh#20(sievesize850mm)
Laboratoryovenat1051C
Gaschromatographtoanalyzebiogascomposition(H2andCO2) Specificmaterialsforthemanualprotocol
120-mLserumbottles(Fig.1a)
Rubberstoppersforserumbottles(foranaerobiccultures)(Fig.1b)(Note:Becarefultonotuse thinstoppersthatcanleadtoleakageofthegasafterthefirstpunctureoftheneedle)
Aluminumrings(Fig.1b)
18-Gx11/2-inhypodermicneedlesandtubing(Fig.1c) Medicaldisposablethree-waystopcockvalve(Fig.1d) 50-mLplasticsyringe
100-mLgraduatedcylinder 500-mLglassbeaker
Crimpertosealaluminumrings Incubatorwithorbitalagitation Glassthermometer
Specificmaterialsfortheautomaticprotocol
AutomaticMethanePotentialTestSystem(AMPTSII,BioprocessControlAB;LundSweden) (Fig.2)
500-mLSchottglassbottles(Fig.2d) 50-mLgraduatedcylinder
500-mLgraduatedcylinder 50-mLglassbeakers
Experimentaldesign: TheproposedmethodpresentstwooptionstorunBHPbatchtests;amanualprotocolwithperiodic measurementsofbiogasproduction;andanautomaticprotocol,whichisruninadevicedevelopedfor onlinemeasurementsoflowbiogasproduction.
Trialregistration: n/a
Ethics: n/a
ValueoftheProtocol
Thismethodstandsforthefirststandardizedprotocolvalidatedinternationallytoestimatethehydrogenpotential.
Twoversionsoftheprotocolareincluded,amanualonewithlowequipment’srequirementsandanautomaticone.
Theaverageintra-laboratorycoefficientofvariationcanbereducedupto9%.
Descriptionofprotocol
Background
Hydrogenproductionbydarkfermentationisanemergingtechnologyofincreasinginterestdueto itsrenewablefeature.TheassessmentoftheBHPisacommonproceduretoevaluatenewpotential substrates, and other parameters [1–3]. This method stands for the first standardized protocol validated internationally to estimate the BHP using batch tests. A complete discussion of the developmentofthisprotocolhasbeenpublished[4].
Fig.1.Serumbottles,rubberstoppers,andaluminumrings.
Stocksolutions
SolutionA:nutrientsandbuffersolution,modifiedfrom[5]
Dissolveinavolumetricflasktomake1Lsolutionwithdistilledwater:41.6gNH4Cl,19.52gMES, 2gMgCl2
6H2O,1.6gFeSO47H2O,40mgCoCl26H2O,40mgMnCl24H2O,40mgKI,8mgNiCl26H2O,8mgZnCl2.
SolutionB:substrate,50gL1glucose
Dry28gofanhydrousglucose(105C,2h)andallowtocoolinadesiccator.Weigh25gofdry glucoseanddissolvewithdistilledwatertomakea500-mLsolutioninavolumetricflask.Thesource ofcarbohydratescanvaryaccordingtotheaimofeachdetermination,e.g.,usinganagroindustrial effluent. The recommendation to get the maximum hydrogen potential is to keep the initial carbohydrateconcentrationat5gL1duringtheassay.
SolutionC:pHadjustment,5NHCl
Add25mLofdistilledwatertoa50-mLvolumetricflask.Add20mLofHCl(37%)anddilutetothe graduationmarkingwithdistilledwater.
SolutionD:pHadjustment,5NNaOH
Add10gofNaOHto30mLofdistilledwater,dissolvewithmagneticstirringandallowtocool.
Dilutethesolutionwithdistilledwatertocomplete50mLinavolumetricflask.
SolutionE:pHindicator,0.4%(w/v)thymolphthalein
Dissolve40mgofthymolphthaleinin9mLofethanol(99.5%);dilutethesolutionwithdistilled watertocomplete10mLinavolumetricflask.
SolutionF:CO2absorptionsolution,3NNaOH
Add144g ofNaOHto1Lofdistilledwater,dissolve withagitation;diluteitto1.2L.Add6mLofsolutionE.
Note:SolutionsEandFareonlyrequiredfortheautomaticprotocol.
Inoculumpreparation
Use sludge froman anaerobic wastewater treatmentreactoras inoculum. Perform a thermal pretreatment drying the sludge at 105C during 24h, for the selection of hydrogen-producing microorganisms[6]. Letthesludge coolandhomogenizeit bygrinding(with theblender,coffee grinderorthemortar)andselecttheparticlesizelesserthan850
m
mbysieving.Determinevolatilesolids(VS)contentaccordingtostandardmethods[7].
Manualprotocol Preparation
1 Labelallbottles;triplicatesofeachevaluatedconditionmustbeincluded,aswellasendogenous control(withoutsubstrate)intriplicate.
Fig.2. Sample incubation unit (a), CO2absorption unit (b), gas volume measuring device (c), and Schott bottles with agitation system (d).
2CalculatethenecessaryamountofinoculumtoaddtoeachserumbottletomaintainanS/Xratio (substrate/inoculum,gsubstrategVS1)of2.7,consideringaworkingvolumeof80mLandan initialcarbohydrateconcentrationof5gL1.Weightheexactamountofinoculumdirectlyinthe serumbottleusingtheanalyticalbalance.
3Add5mLofsolutionAineachbottleusingagraduatedpipette(oranairdisplacementpipette).
4Add4mLofsolutionB(withtheexceptionoftheendogenouscontrol)usingagraduatedpipette(or anairdisplacementpipette);theinitialglucoseconcentrationwillbe5gL1.
5Addtheneededamountofdistilledwaterusingagraduatedcylinder,71mLor75mL,forbottles withcarbohydrates(withsolutionB)orendogenouscontrols,respectively;tocomplete80mLof workingvolumeintheserumbottles.Theheadspacewillbeof40mL.
6AdjusttheinitialpHto7.5bydrippingsolutionCorDasnecessaryusingaPasteurpipette.
7Closethebottleswiththerubberstopperandsealthemwiththealuminumrings(usethecrimper).
8Fortheheadspaceexchange,insertaneedleconnectedtoahosetoflushwithN2for30sinthe serumbottlesandwiththehelpofanotherneedletoletthegasout(Fig.3).After30s,getoutthe needlessimultaneously.
IncubationandmonitoringofH2production
1Consideringpreviousexperimentalexperiencestovalidatethisprotocol,starttheincubationclose tonoon(12:00h).
2Incubatethebottlesat37Cwithanorbitalshakingof150rpm.Afterthisstep,preparethewater- filledinvertedgraduatedcylinderaccordingtothefollowingsection.
3Afteronehourofincubation,dischargetheexcesspressureofeachserumbottlesintheinverted graduatedcylinder.
4Performgasproductionmeasurementseverythreeorfourhours.Recordthevolumeproduced,as wellasthetemperatureoftheacidwaterinthewater-filledinvertedgraduatedcylinder.
5Totakeagassample,purgethehosebeforetakingthesample.Analyzethecompositionofthe biogas(H2andCO2)atleastonceadaybygaschromatography.
6Todeterminetheendofthetest,applythestoptimecriterion(ST),whichisobtainedwhentheH2
productioncurve becomesasymptotic(FT) (Fig.4)[8].Additionally,you canusethecoefficient ofvariation betweenthelastthreerecordsofcumulativehydrogenasstopcriterionwhenitislowerthan5%.
Fig.3. Headspaceexchangeontheserumbottles.
7 Tostopthetest,removetheserumbottlesfromtheincubator.Seethesamplingandanalysissection forfurtherinstructions.
NOTE. Todetermine theendof thetestproperly, youwillhavetoplotimmediatelyeveryH2
productionreading.
Water-filled-invertedgraduatedcylindertomeasurebiogas
1 Acidify500mLofdistilledwaterwith10mLofsolutionC(pH<2)topreventCO2dissolutioninthe liquid.
2 Placea100mLinvertedcylinderasshowninFig.5usingahosetothebottomofthecylinder,a syringe,andathree-waystopcocktofillthecylinderwiththeacidwater(Fig.5c).
3 Tomeasurethebiogasproduction,connectaneedletoonesideofthethree-waystopcockandkeep itclosed,theninserttheneedlethroughtherubberstopperoftheserumbottlesandopenthe stopcocktoallowthebiogasdisplacetheliquidinthecylinder,registerthevolume(Fig.5d).
Fig.4.Kineticovertime.LT:latencytime;FT:finaltime;SP:timetostopthekinetic.
Fig.5.Requiredmaterialforthebiogasmeasuring(a),fillingtheinvertedcylinderwithasyringe(b),water-filled-inverted graduatedcylinder(c),andbiogasproductionmeasuring(d).
4The biogas samples can be taken from the displaced volume in the cylinder, or using a chromatographysyringedirectlyfromtheserumbottle.
Automaticprotocol
Fortheautomaticdeterminationofthebiohydrogenpotential,theprotocolwasadaptedtothe manufacturer recommendations of the Automatic Methane Potential Test System II (Bioprocess ControlAB;Lund,Sweden),intheoperationandmaintenancemanual[https://www.bioprocesscon- trol.com/media/1511/bioprocess-control-manual-ampts-ii-ampts-ii-light.pdf].
Preparation
1For theCO2 absorption unit preparation, add 80mLof F solution to each bottle of the CO2
absorptionunit(Fig.3b),placeaplasticstopperwiththetwotubingports.
2ConnectthebiogashosesofeachbottleoftheCO2absorptionunittothecorrespondentbottlein theincubationunit(Fig.3a)accordingtotheAMPTSIIinstructions.
3Label all Schott bottles;triplicates of each evaluatedcondition must beincluded, as wellas endogenouscontrol(orblank)intriplicate.
4CalculatethenecessaryamountofinoculumtoaddtoeachSchottbottletomaintainanS/Xratio (substrate/inoculum,gsubstrategVS1)of2.7,consideringaworkingvolumeof360mLandan initialcarbohydrateconcentrationof5gL1.Weightheexactamountofinoculumforeachbottle inglassbeakersusingtheanalyticalbalance.
5Add22.6mLofsolutionAineachglassbottleusingagraduatedpipette(oranair-displacement pipette).
6Add36mLofsolutionBineachbottle(excepttoendogenouscontrol)usingagraduatedpipette(or anairdisplacementpipette);theinitialglucoseconcentrationwillbe5gL1.
7Addtheweighedinoculumtoeachglassbottle,suspendtheremainingsludgethatstaysintheglass beakerusingthewaterpointedoutinthefollowingstep,andaddedtothecorrespondingbottle.
8Tocomplete360mLofworkingvolumeintheserumbottles,addtheneededamountofdistilled waterusingagraduatedcylinderandpipette,301.4and337.4mL,tothebottleswithcarbohydrates (withsolutionB)orforendogenouscontrols,respectively.Theheadspacewillbeof240mL.A workingvolume/headspaceratioof1.5willbemaintainedaccordingtotherecommendationsof theAMPTSIImanual.
9AdjusttheinitialpHto7.5bydrippingsolutionCorDasnecessaryusingaPasteurpipette.
10Putathinlayerofstopcockgreaseinthebottlethreadandtheoutsidepartofthebottleopening,to avoidgasleaks.
Fig.6. HeadspaceexchangeonAMPTSIIbottlesusingagassamplingbagwithN2.
11 Place thebottlestopperswithtwo tubingportsandrotatingshaft for mixingintheopening ofthe bottles.
12AttachthemultifunctionbrushlessDCmotor.
13PuttheTygon1hoseintheportsfromthestopper.Connectoneofthehosestothecorresponding bottleintheCO2absorptionunitandsealtheotherhosewithapipeplug.
Headspaceexchange
1 Fortheheadspaceexchange,temporallydisconnecttheTygon1hosefromtheCO2absorptionunit andintroducethehoseinabeakerwithwatertodischargetheexcesspressure.Removethepipe plugandconnectittoaN2flow,flushtheheadspaceduring30s(Fig.6).
2 ClosetheTygon1hosesagainwiththepipeplugandreconnecttheotherhosetothecorresponding bottleintheCO2absorptionunit.
AMPTSIIsystemincubationandmonitoring
1 Filltheincubationunitwithdistilledwaterandsettoatemperatureof37C.
2 Connecttheagitationsystemsofeachbottleseriallywiththemotorcables,andthefirstmotorto theMotorController.
3 Connectthe12VpoweradaptertotheGasVolumeMeasuringDevice,andtoa100240V50/
60Hzstandardpowersocket.Afterthis,connectthe24VpoweradaptertotheMotorController andtoa100240V50/60Hzstandardpowersocket.
4 SettheSystemswitchontheMotorControllertoON,andsettheON/OFFswitchesoneachmotor unittoON.
5 Emptyeachflowcellinthegasvolumemeasuringdevice.
6 Adjustthemotorspeedto60%(approx.120rpm),withintermittentmixingat60sONand180s OFF.ActivatethemotorsettingthecontroltoONandapplythesettings.
7 StartthedataloggingprogramaccordingtotheAMPTSIIsoftwaremanual.
8 Analyzethegascompositiontodeterminethehydrogenfractioninthebiogassamples,foreach bottleatleastonceduringthekinetics.DisconnecttheTygon1hosefromtheabsorberunitand sealitwithapipeplugandtakethebiogassamplewithasyringefromtheotherhose.
9 Checkdailythatthehardtubingpiecesthatconnectthebentstirrodtothemotorareundamaged andthemixingworksproperly.Otherwise,changethetubingpieces.
10Checkdailythatthewaterlevelinthethermostaticwaterbathreachestheplasticlidandfillitwith additionaldistilled water ifnecessary. Makesurethat theTygon1 hoseisnot bentabruptly, interferingwiththegasflowandnotbeingdamagedbytherotatingpartsoftheagitator/motor.
11 Verifythatthewaterlevelinthegasvolumemeasurementdeviceiswithintherecommended range.Fillwithadditionaldeionizedordistilledwatertotherecommendedwaterlevelwhen necessary.
12ThethymolphthaleinpHindicatorinsolutionFwillchangefrombluetocolorlesswhentheCO2
absorption capacity of the NaOH solution drops below the optimum. At this point, it is recommendedtoreplacethebottlewithnewsolutionFtopreventtheCO2gasfrompassingtothe gasvolumemeasuringdevice.Approximately2.9LofCO2canbecaptured(at22C)ineachbottle beforeitneedstobechanged.
13TochangethesolutionF,placepipeplugsonthehosesoftheincubationunitandgasmeasuring device.Replacetheoldsolutionwithanewone,reconnectthehosesandremovethepipeplugs.
NOTE.BeforeusingtheAMPTSIIsystem,readtheoperationandmaintenancemanualcarefully, detailsofsettinguptheequipment,connection,andsoftwaremanagementareincluded.
Endofthetest
1TheAMPTSIIsoftwareautomaticallyupgradesthecumulativehydrogenproductioncurve;review thecurvedailytodeterminetheendoftheessayfollowingthestopcriteria.Thestoptimecriterion (ST) is obtained when theH2 production curvebecomes asymptotic (FT) (Fig. 4) [8]. Asan
additionalstopcriterion,youcanusethecoefficientofvariationbetweenthelastthreerecordsof cumulativehydrogenwhenitbecomeslowerthan5%.
2 IntheAMPTSIIsoftware,generateareportintheDownloadreportmenu.Downloadthereportand openittomakesurethatthereporthasbeengeneratedcorrectlyandthatnoerrorshaveoccurred duringthedownloadofthefile.
3 Stoptheregistrationbypressingthepausebuttonandthenthestopbutton.Note:Bypressingthe stopbutton,theexperimentassociatedwiththatparticularcellcannolongercontinue.
4 Turnoffthethermostaticwaterbath.
5 Settheon/offswitchofeachmotorunittoOFF.
6 SetthesystemswitchonthemotorcontrollertoOFF.
7 Unplugthepoweradapters(forthemotorcontrollerandthegasvolumemeasuringdevice)from thepowersupply.
8 DisconnectthehosesbetweenthereactorsandtheNaOHbottles.
9 DisconnectthehosesbetweentheNaOHbottlesandthegasvolumemeasuringdevice.
10Emptythewaterbathusingthemanualwaterpumpincludedwiththeequipment.
Samplingandanalysis
1Oncethekineticshavebeencompletedaccordingtothepreviouslymentionedcriteria,openthe bottlesandrecordthepHvalueofitsliquidcontent.
2Keep the bottles in constant agitation with the help of a magnetic stirrer and grill. Take a homogeneoussampleofatleast20mLfromeachbottleanddeterminetheconcentrationoftotal andvolatilesuspendedsolidsbyduplicate(5mLpersample)accordingtostandardmethods[7].
3Take a sample of at least20mL fromeach bottle todeterminethechemical oxygen demand (COD),fermentationproducts,andresidualcarbohydrates.Acidifythesampleswithconcentrated H2SO4(pH<2).
4Centrifugethe20-mLsamples(3600rpmfor10min,oratahigherspeed)andfilterthesupernatant with0.45
m
mnitrocellulosefilters.Thesamplecanbekeptrefrigerated(4C)fornomorethan 7daysuntilanalysis.Ifsamplescontainmanysuspendedsolids,beforethenitrocellulosefilteritis advisabletousea1.5m
mglassfiberfilter.5FromthecentrifugedsampleanalyzetheCODaccordingtostandardmethods[7],thefermentation productsbygasorliquidchromatography,aswellastheresidualcarbohydratesbythephenol- sulfuricacidmethod[9].
Fig.7. Cumulativehydrogenproduction(Hmax)specifictotheworkingvolume(LH2L1),forthemanualandautomatic protocols,anditscorrespondingintra-andinter-laboratoryvariation.Forthemanualprotocolevaluationdifferentinoculum weretestedbydifferentlaboratories,meanwhilefortheautomaticprotocolthreedifferentsourceofinoculumwereevaluated indifferentlaboratories.Thedifferentinoculumsourceswereheat-treatedanaerobicsludgefromathermophilicdigester (HTT);heat-treatedanaerobicsludgefromamesophilicdigester(HTM);biomassfromanauto-fermentedeffluentrichin sucrose(AF);aerobicsludgepretreatedbycellwash-out(WO);compostfromkitchenwastes(C);andheat-treatedanaerobic sludgefromadigestertreatingsolidwastes(HTS).L1–L8standsforresultsfromdifferentlaboratories.
Validationofanalyticalmethods
It is highly recommended to validate the analytical methods to determine COD, sugars and fermentationproductsasindicatedbelow:
1 Weigh1gofanhydrousglucose(driedat105Cfor2handstoredinadesiccator)anddiluteina1L volumetricflaskwithdistilledwater.
2 Analyzethe CODand carbohydrates of thesolutionwith themethodologyof each laboratory.
ConsiderthatglucosehasatheoreticalCODof1.067gCODgglucose1.
3 IftheresultsofCODorcarbohydratesanalysisarenotasexpected,youshouldreviewyouranalysis procedureandcalibrationcurves.
4 Tovalidatethemethodsofmeasuringfermentationproductsitissuggestedtousecertifiedreference materials(e.g.VolatileFreeAcidMixCRM46975-Supelco,andLacticacidPHR1215-Supelco;Merck KGaA,Germany).
Calculations
H2cumulativevolume
FromthecumulativehydrogenvolumegraphadjustthecurvetothemodifiedGompertzmodel [10],recordthesoftwareusedandthecorrelationcoefficient,maketheadjustmentforeachreplicate:
HðtÞ¼Hmaxexp exp 2:71828Rmax
Hmax ð
l
tÞþ1WhereH(t)(mL)isthecumulativehydrogenproductionattimet(h);Hmax(mL)isthemaximumgas produced;Rmaxisthemaximumproductionrate(mLh1);and
l
isthelag-phasetimebeforetheexponentialhydrogenproduction(h).Forcumulativehydrogenproductionresultsusingthemanual version,adjusttherecordedvolumetostandardconditions(0Cand1atm).Theautomaticdevice AMPTSIIreportsthegasproductionatstandardconditions,accordingtointernaltemperatureand pressuresensors.
CODbalanceoffermentationproducts
It is highlyrecommended toquantifythenon-identified(N.I.CODeq)products followinga COD balance[11]:
N:I:CODeq¼CODfGlucoseCODeqX
MetabolitesCODeq
WhereCODf(gCODL1)istheanalyticalsolubleCODconcentrationdeterminedattheendofthetest;
GlucoseCODeq (gCODeqL1)istheresidualglucoseconcentration;and P
MetabolitesCODeq isthetotal solubleproductsconcentration(gCODeqL1)determinedbychromatography.TheCODequivalenceof the different fermentation products and carbohydrates, can be calculated with the following equations,basedontheaverageoxidationreactionsoftheanalyzedcompoundsandthewater-oxygen aselectronacceptor.
aÞ mg CODace
L ¼ X mgace L
1 mmol 60 mgace
8 meq e 1 mmolace
8 mg OD 1 meq e
bÞ mg CODpro
L ¼ X mgpro L
1 mmol 74 mgpro
14 meq e 1 mmolpro
8 mg OD 1 meq e
cÞ mg CODbut
L ¼ X mgbut L
1 mmol 88 mgbut
20 meq e 1 mmolbut
8 mg OD 1 meq e
dÞ mg CODval
L ¼ X mgval
L
1 mmol 102 mgval
12 meq e 1 mmolval
8 mg OD 1 meq e
eÞ mg CODcap
L ¼ X mgcap L
1 mmol 116 mgcap
24 meq e 1 mmolcap
8 mg OD 1 meq e
fÞ mg CODeth
L ¼ X mgeth L
1 mmol 46 mgeth
12 meq e 1 mmoleth
8 mg OD 1 meq e
gÞ mg CODlac
L ¼ X mglac L
1 mmol 90 mglac
12 meq e 1 mmollac
8 mg OD 1 meq e
hÞ mg CODfor
L ¼ X mgfor L
1 mmol 46 mgfor
2 meq e 1 mmolfor
8 mg OD 1 meq e
iÞ mg CODsuc
L ¼ X mgsuc
L
1 mmol 118 mgsuc
14 meq e 1 mmolsuc
8 mg OD 1 meq e
jÞ mg CODglu
L ¼ X mgglu L
1 mmol 180 mgglu
24 meq e 1 mmolglu
8 mg OD 1 meq e
kÞ mg CODH2¼X mL H2; STP 1 mmol 22:4 mLH2
2 meq e 1 mmolH2
8 mg OD 1 meq e
WhereXmgcompoundL ¼producedmetabolitesconcentration mgL
;ace,aceticacid;pro,propionicacid;but, butyricandisobutyricacids;val,valericandisovalericacids;cap,caproicandisocaproicacids;eth, ethanol;lac,lacticacid;for,formicacid;suc,succinicacid;glu,glucose;H2,hydrogen;XmLH2,STP, hydrogen volume at standard temperature (0C) and pressure (1atm) conditions. The COD equivalenceisalsousefultodeterminethestoichiometryofthereactionsandmetabolicpathways followedbytheinoculumused.Anexampleofsuchcalculationisdetailedelsewhere[12].
Qualitycriteriafortheresults
Inordertovalidatethehydrogenproductiontests,thecoefficientofvariationofHmaxmustbe<15
%,evenafterapplyingastatisticalanalysistoeliminateoutliers[4].UsetheDixontesttoeliminatea uniqueoutlieroftriplicates,consideringapvalue=0.05.
Methodvalidation
The present method was validated in 8 independent laboratories from 5 different countries (Brazil, Chile, France,MexicoandUruguay);adetaileddiscussionaboutitsdevelopment,validationandconsiderationof workloadtimewerealreadypublished[4].Averagevaluesofcumulativehydrogenproduction(Hmax)and thecorrespondingstandarddeviationswereusedtocalculatetheintra-laboratoryandinter-laboratory coefficientofvariation(CV)asrepeatabilityandreproducibilityindicators,respectively.
Applyingthepresentprotocol,theaverageintra-laboratorycoefficientofvariationrangedfrom13
%to9%usingthemanualandtheautomaticprotocol,respectively.Butusingtheautomaticprotocol, theinterlaboratoryvariationcouldbereducedupto15%withtheHTTasinoculum;whichisan acceptableresultaccordingtostudiesanalyzingthebiochemicalmethanepotential(Fig.7)[13].
Conclusions
Thismethodfeaturesanewandvalidatedprotocolforbiohydrogenpotential,providingatoolfor inter-laboratory studies and reliable comparisons of results. Indeed, following the protocol, the variationofresultscanbereducedtoacceptablelevels,usingeitherthemanualorautomaticversion.
DeclarationofCompetingInterest
The authors declare that they have no known competing financial interests or personal relationshipsthatcouldhaveappearedtoinfluencetheworkreportedinthispaper.
Acknowledgements
ThisworkwasperformedintheframeoftheBiohydrogenLatinAmericanetwork.Theauthors thanksthefundingofthefollowingprojects:FondodeSustentabilidadEnergéticaSENERCONACYT, ClústerBiocombustiblesGaseosos,247006andCONACYT240087;Fondecyt3160219;ProgramECOS- CONICYTprojectN C12E06, GRAIL613667 (FP7-KBBE-2013);ANII-FSE102488 (Uruguay); FAPESP (2015/06246-7)and CNPq processes 406751/2013-7,150641/2015-0,150475/2016-0 (Brazil); and programEUWaste2bioHyproject(FP7-MC-IEF-326974).ThecofundingofBioprocessControlAB (Lund,Sweden)fortheopenaccesspublicationofthismethodisalsoacknowledged.Theauthors thankthe technicalassistance of Carolina MejíaSaucedo, Gloria MorenoRodríguez,Jaime Pérez Trevilla,ÁngelA.HernándezHuerta,GuillermoVidriales-EscobarandRobertoE.BolañosRosales.
References
[1]X.M.Guo,E.Trably,E.Latrille,H.Carrere,J.P.Steyer,Predictiveandexplicativemodelsoffermentativehydrogenproduction fromsolidorganicwaste:roleofbutyrateandlactatepathways,Int.J.HydrogenEnergy9(2013)3–12,doi:http://dx.doi.
org/10.1016/j.ijhydene.2013.08.079.
[2]L.Chatellard,E.Trably,H.Carrère,Thetypeofcarbohydratesspecificallyselectsmicrobialcommunitystructuresand fermentationpatterns,Bioresour.Technol.221(2016)541–549,doi:http://dx.doi.org/10.1016/j.biortech.2016.09.084.
[3]H.Han,L.Wei,B.Liu,H.Yang,J.Shen,Optimizationofbiohydrogenproductionfromsoybeanstrawusinganaerobicmixed bacteria,Int.J.HydrogenEnergy37(2012)13200–13208,doi:http://dx.doi.org/10.1016/j.ijhydene.2012.03.073.
[4]J.Carrillo-Reyes,A.C.Tapia-Rodríguez,G.Buitrón,I.Moreno-Andrade,R.Palomo-Briones,E.Razo-Flores,O.AguilarJuárez, J.Arreola-Vargas,N.Bernete,AdrianaFerreiraMalufBragaf,L.Braga,E.Castelló,L.Chatellard,C.Etchebehere,L.Fuentes,E.
León-Becerril,H.O.Méndez-Acosta,G.Ruiz-Filippi,E.TapiaVenegas,E.Trably,J.Wenzel,M.A.Zaiat,Standardized biohydrogenpotentialprotocol:aninternationalroundrobintestapproach,Int.J.HydrogenEnergy44(2019)26237–
26247,doi:http://dx.doi.org/10.1016/j.ijhydene.2019.08.124.
[5]O.Mizuno,R.Dinsdale,F.R.Hawkes,D.L.Hawkes,T.Noike,Enhancementofhydrogenproductionfromglucosebynitrogen gassparging,Bioresour.Technol.73(2000)59–65,doi:http://dx.doi.org/10.1016/S0960-8524(99)00130-3.
[6]I.Moreno-Andrade,G.Moreno,G.Kumar,G.Buitrón,Biohydrogenproductionfromindustrialwastewaters,WaterSci.
Technol.71(2015)105–110,doi:http://dx.doi.org/10.2166/wst.2014.471.
[7]APHA/AWWA/WFE,StandardMethodsfortheExaminationofWaterandWastewater,21thedn,(2005)WashingtonDC,USA.
[8]I.Moreno-Andrade,G.Buitrón,Influenceoftheoriginoftheinoculumontheanaerobicbiodegradabilitytest,WaterSci.
Technol.49(1)(2004)53–59.
[9]M.Dubois,K.A.Gilles,J.K.Hamilton,P.A.Rebers,F.Smith,Colorimetricmethodfordeterminationofsugarsandrelated substances,Anal.Chem.28(1956)350–356.
[10]M.H.Zwietering,I.Jongenburger,F.M.Rombouts,K.van’tRiet,Modelingofthebacterialgrowthcurve,Appl.Environ.
Microbiol.56(1990)1875–1881.
[11]B.E.Rittmann,P.L.McCarty,EnvironmentalBiotechnology:PrinciplesandApplications,McGraw-Hill,Boston,Mass,2001.
[12]H.S.Lee,B.E.Rittmann,Evaluationofmetabolismusingstoichiometryinfermentativebiohydrogen,Biotechnol.Bioeng.
102(2009)749–758.
[13]C.Holliger,M.Alves,D.Andrade,I.Angelidaki,S.Astals,U.Baier,etal.,Towardsastandardizationofbiomethanepotential tests,WaterSci.Technol.(2016)1–9.