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IntroductiontoLowCarbonGasTechnologies
Contents
OVERVIEWPage3
Part1:DECARBONISATIONPage6
BiomethaneproductionthroughanaerobicdigestionPage6
PyrogasificationPage8
HydrothermalgasificationPage9
E-methanePage10
SolarphotocatalyticprocessesPage11
Part2:DIVERSIFICATIONPage12
MethanereformationPage13
-MethanereformingprocessforpureH2productionPage13
WaterelectrolysisPage14
ThermalgasificationPage14
MethanepyrolysisPage15
SolarphotocatalyticprocessesPage15
BiologicalproductionPage16
GeologicalextractionPage17
Part3:INNOVATION
Page18
ACKNOWLEDGEMENTS
Page19
Frontcoverimage:iS/artisteer
02IntroductiontoLowCarbonGasTechnologies
Overview
Attheendof2023,morethan140countrieshadamid-century
carbon-neutralitypledge.Meetingthesecommitmentswillrequirea
dramaticandrapidchangeintheentireglobalenergysystem,onewhichtheflexibilityandinnovationofthegasindustryiswellplacedtodeliver.
Reducingemissionsinlinewiththe2015ParisAgreementonClimateChangewillrequire,asaminimum,therampingupofthreekeyareas:
1
Decarbonisation:improvingenergyefficiency,andreducingemissionsandmethaneleaks.
2
Diversification:usingnaturalgaswithlow-carbonandrenewablealternatives,suchasbiomethane,e-methaneandhydrogen.
3
Innovation:supportingtheindustry,bothfromalegislative,regulatoryandinvestmentperspectivetocontinuouslyinnovateitsproductsandservicesrenderedtomarkets,consumersandusers.
Organicgrowth:
Amodernbiofuelgasplant.
Photo:iS/VadymTerelyuk
IntroductiontoLowCarbonGasTechnologies03
Overview
AlignedtoIGU’ssupportoftheParisAgreement’sNationallyDeterminedContributionstoreduceGHG
emissionsanditscommitmenttosignificantlydecarbonisetheglobalenergysystem,this“IntroductiontoLowCarbonGasTechnologies”providesabriefguideonkeylow-carbonandrenewablegastechnologiesthatarecurrentlyavailablefordeploymenttorampupthegasindustry’seffortstowardsdeepdecarbonisation.
Naturalgasanditsevolvingtechnologiessupporttherenewableenergysupplybyovercomingintermittencyandinstability.Existingnaturalgasinfrastructurewillalsoenablecost-effectiveandmorerapiddeploymentoflow-carbonandrenewablegases-criticalfordeepdecarbonisationoftheglobaleconomy.Together,theycanenablenet-zeropathways,energysecurityandaccessissues.
Futureenergymix:
Therearearangeof
optionsonthehorizon.
Image:iS/sharfsinn
04IntroductiontoLowCarbonGasTechnologies
Overview
I.
Thefirstsectionofthereportwillreviewthemainfivelow-CO2gastechnologiesaimingtodecarbonisethemethanemoleculesupplychain.Theseare:
1
Anaerobicdigestion:biomethanebasedonwetbiomass.
2
Pyrogasification:syntheticmethaneobtainedfromthermo-chemicalprocesswastesrichincarbon.
3
4
Hydrothermalgasification:syntheticmethanebasedonliquidbiomasstreatmentathightemperatures.
5
E-methane:syntheticmethaneusingcarbondioxideasfeedstock.Solarphotocatalyticprocesses.
Thesecondsectionofthereportwillprovideanoverviewofhydrogenproduction
technologiesasenergycarriers.Currently,thereisalimitednumberofsuchtechnologiesinwidespreadoperation,andthesemustberampedupbyordersofmagnitudetobe
consistentwiththeworld’scurrentclimatetargets.Onlythencanweensurethattheprioritiesofenergysecurityandenergytransitiondonotundermineeachother.
Thecurrentenergy-carryinghydrogenproductiontechnologiesare:
Methanereformation:extractinghydrogenfrommethanemoleculesandremovingCO2.
Waterelectrolysis:usingrenewableelectricitytoproducehydrogenfromwater.
Thermalgasification:extractinghydrogenfromsolidmaterialwithhighheat.
Methanepyrolysis:extractinghydrogenfrommethaneusingaprocessthatdoesnotproduceCO2.
Solarphotocatalytic:usingdedicatedsolarenergyinstallationstoproducerenewablehydrogen.
Biologicalproductionofhydrogen:throughfermentationandphotolysisofbiomass.
Geologicalextractionofnaturalhydrogen.
2.
4
6
3
7
2
5
1
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Decarbonisation
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I.Decarbonisation
1Biomethaneproductionthroughanaerobicdigestion
Feedstocksproduction,storageandphysicalpretreatment
Production
Digestate
valorisation
Biogas/Biomethanevalorisation
Anaerobicdigestion
Biogas
Combinedheat
andpowerplant
(CHP)
Digestate
Collect
feedstocks
Digestatestorage
Fertilizer
Storage
Biogasupgrading
Biofuel
Spreading
Naturalgasgridinjection
Agriculturalwastes
Other
biowastes
Electricity
Biomethane
Manure
Heat
Anaerobicdigestionisaprocessthroughwhichbacteriabreakdownorganicmatterintheabsenceofoxygen.
Thisprocessreleasesenergy-richbiogas,whichisrelativelyhighinmethane(CH4)contentandcanbe
capturedandusedasfuel.Itcanbeenhancedeitherbyinjectinghydrogen(H2)inthereactororbyusingalightelectricalcurrenttoimprovetheCH4/CO2-ratio.
Thereisawiderangeofpotentialorganicmatterinputsthatcanbeusedasfeedstock,suchasfoodandfeedindustrywastes,manureandslurry,greenwastes,intermediatecropsandsewagesludge.
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Biomethaneisconsideredcarbon-neutral
Biomethaneproductioncapturesmethane,astrong
greenhousegas,fromitsbiorawmaterial,andturnsitinto
usefulfuel.Thisprocessstopsmethanefromescapingintotheatmosphere,whereitwouldcontributetoglobalwarming.
Biomethane,madefrombiogas,canbeusedjustlikenaturalgas.
Iteasilyusestheexistinggassystemswithoutneedinganychanges,makingitacost-effectiveandsimplewaytosupportdecarbonisation.
CO2fromtheatmosphereiscapturedbyorganicwasteusedtoproduce
biomethane.ItscombustionproducesbiogenicCO2emissions.
Compensationeffect:almostnoimpactongreenhousegasemissions.
0
CarbonNeutral
%
1.CollectionOrganicwasteiscollectedand
transportedtothemethanisationsite.
fermentation
processwhichproduces
digestateandbiogas.
Digestate
Isusedandanaturalfertiliser.
Biogas
Arenewablefuelto
generateheat(hotwaterandsteam)and
electricity(CHP)onsite.
Organicwaste
goesthroughananaerobic
2.Anaerobicdigestion
RGGO=1MWhgreengasinjected
4.EndusesBiogasispurifiedtobeinjectedinto3.Upgrade
thegasgridforindustrialanddomesticuses,suchasheatingandcooking.
Thesefeedstocksarecollectedandtransportedtothefacility(methanisationsite),wheretheyareturnedintobiogas.
Thebiogascanthenbedirectlyusedtoproduceelectricityandheat,oritcanbepurifiedintoBiomethane,whichisaone-for-onereplacementfornaturalgas.
Biomethanecanbeinjectedintotheexistinggasgridforindustrialanddomesticuses,suchasheatingorcooking,andformobilitypurposes.Itisimportanttorememberthattheefficiencyofbiomethaneproductionisheavilydependentonthesourcematerial.
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2Pyrogasification
Pyrogasificationisathermochemicalprocessthatconsistsofheatingwasteintheabsenceofoxygentoproducearenewablemethane.Ithastwomainsources:
IDrybiomass:woodwaste,residuesfromwastemanagement,andmostorganicwaste.
IISolidrecoveredfuels(SRF)areproducedfromhouseholdrecyclingwasteandgeneralindustrialandcommercialwaste.
Oncecollected,thewasteisheatedtoveryhightemperatures(800to1,500degreesCelsius)inthepresenceofasmallamountofoxygen,convertingthewasteintosyntheticgas(syngas).Syngasisrichincarbonmonoxide,hydrogen,carbondioxideandmethaneandmustbepurified.
SyngasfromSRFcontainsmorepollutantsthansyngasfromcleanbiomass,suchasfromplants.Further
challengesarefoundinconventionalinorganicgasremovalprocesses,whichmustbeadaptedbeforebeinguseable.
Developmentisalsonecessarytopurifythesyngasaccordingtoitsfutureusage,includinginmakingammonia,methanolorotherindustrialchemicalsandfuels.
Pyro-gasificationprocess
Stepaimingtoincreasethecarbon
conversion
intomethane
Stepaiming
atconvertingbiomassintoasyntheticgas(<<syngas>>)richinCO,H2,CO2andCH4
Stepdesignedtoremove
undesirablecompoundssuchastarsorinorganicsulfur
StepdesignedtoadjustthebioSNGqualityaccordingto
itsusage
CO+3H2>>CH4+H2OCO2+4H2>>CH4+2H2O
Hightemperatureheatapplied
Renewable
carbon
feedstock
Catalytic
methanation
Syngas
purification
Gas
upgrading
Removingimpurities
BioSNG
Fieldwork:Biogasfromcorn.Photo:iS/Jan-Otto
08IntroductiontoLowCarbonGasTechnologies
Decarbonisation
3Hydrothermalgasification
Hydrothermalgasificationrequiresthepresenceofwatertoconvertwetorliquidorganicwasteintosyngas,throughaprocesswhichsubjectsthewastetohighpressureandtemperatures.
Theproducedsyngasisarenewablegas,composedofmethane,hydrogenandcarbondioxide.However,thecompositionofthissyngasvaries,accordingtothecharacteristicsoftheinputs.
Theprocesscreatesgreengasesusingliquidorganicwaste,whichisotherwisedifficulttodisposeof,suchasdigestatesfromanaerobicdigestion,sewagesludgefromindustrialormunicipalwastewatertreatmentplants,macroandmicro-algae,liquidandsolidfarmingwaste,foodindustryresiduesandby-products.
Thehydrothermalgasificationconsistsofthefollowing:
-Liquidorganicwasteispumpedathighpressure(260-300bars).
-Thematterthenpassesthroughaheatexchanger,whichseparatesphosphorus,potassium,calciumandmetalswhichareextractedandrecovered.
Hydrothermalgasificationisgasificationinhotcompressedwaterwhichuseswaterinasupercriticalstate
HydrothermalreactorSyngasabovethe
watersupercritical
point(221bar,374oC)
Non-catalytic600-700oC
S
Syngas
Separation
Catalytic380-420oC
CH4
Liquidorganicwaste
Productionofsyngas,CH4,H2,orchemicals
●Rawsyngascanbevalorisedeitherdirectlyforheatand/orelectricityproduction,orpurifiedtocleanCH4orH2,orconvertedintochemicals.
CH4contentreaches50-60%incatalyticconversion,andupto90%whenH2isco-injectedinthegasifier.H2concentrationcanachieve50-75%insyngas.
Source:2020.LeCadreE.MertensJ.EmergingSustainableTechnologies
P,K,Ca
metalsrecovery
Heat
exchanger
Waterand
NH4+
260-300bar
Purification
Pump
CO2
H2
Theprocessispossibleatbothhigherandlowertemperatures(aslongasacatalystisused).Therearepositivesandnegativesforboth,ashighertemperaturesrequiremoreenergy,andtheuseofapreciousmetalcatalystatlowertemperaturesiscostlyandhasafinitelifespan.
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Theresultingsyngasisthenpurifiedtoextractunwantedcarbondioxide,leavingmethaneandhydrogen.Thisrawsyngashasthepotentialtobeuseddirectlyforheatandelectricityproduction.Alternatively,the
hydrogencanbeusedtoconvertsomeofthecarbondioxideintoadditionalmethanethroughamethanationstep,afterwhichtheresultinggascanbetreatedsoitisreadytoinjectintothegastransmissionsystem.
Methanecontentreaches50-60%incatalyticconversionandevenupto90%whenadditionalhydrogenisalsoinjectedintothegasifier.Theprocessproducesmethaneorhydrogenefficiently.
4E-methane
Methanationcanalsobeusedtocombinecarbonmonoxide(CO)orcarbondioxide(CO2)withhydrogentoproducee-methane,inaprocessthatalsoproducesheat.Methanationisaprocessthroughwhich
hydrogenisconvertedintomethane,whichcanbeusedintheexistingnaturalgasinfrastructure.
Carbondioxidecanbeobtainedfrommanysources,suchasmethanisationplants(biogenicCO2)orfrom
industrialproductionandcapturefromtheatmosphere,supportingthedevelopmentofawiderangeofnewtechnologiesthatmayhavethepotentialtoreducegreenhousegasemissions.
CO2canbeusedasbuildingblocksforhighadded-valuefuelslikemethane
SOURCEofCO2
Atmosphere
Cleaning
Capture(iflowconcentration)
OR
Industry
SOURCEofHYDROGEN
elabityle}Electrolyser
Plants
Algae,Cynobacteria,
CO2
CO2
Minerals
Bacteria
CO2
C2}2
+
CO2
VALORISATION
PHOTOSYNTHESISBiological
ENHANCEDOILRECOVERY
CARBONATIONFOODINDUSTRY
POLYMERISATIONChemical
MINERALISATIONChemical
FERMENTATIONBiological
HYDROGENATIONChemical
Co-Electrolysis
MARKETS
Decarbonisedrenewable
electricity
requiredforallprocessestobe
sustainable
Thiscouldbesyntheticnaturalgas(=syntheticmethane)
10IntroductiontoLowCarbonGasTechnologies
Decarbonisation
5Solarphotocatalyticprocesses
Artificialphotosynthesis(AP),alsoknownassolarphotocatalyticprocess,hasthepotentialtoproducesyntheticmethane.ThisprocessdecreasesorremovestheneedforusingelectricalpowerandGHG
emissions,aswellasbiomass,intheproductionoflow-CO2methane.
Artificialphotosynthesisseekstoreplicatethenaturalphotosynthesisprocess.Itwidelyusessemi-conductorsasthephotocatalyst,anditoftensplitstheprocessintotwosteps:
IProductionofhydrogenbysplittingwaterthroughthemethodofphotocatalysis.
IICarbondioxideproduction,anditssubsequentreactionswithhydrogen,toformlightweighthydrocarbons,byusingdifferentapproaches.
OxygenEvolution
Reaction(OER)
h
O2
Greenhydrogenmarket
CO2
H2O
bH2b
(photo)-electrocatalysis
HydrogenEvolution
Reaction(HER)
Greensyntheticmolecules
(CH4,CH3OH,COOH,CxHy,...)
Conversion:PhotovoltaicpowersupplysystemsPhoto:iS
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2.Diversification
Hydrogenissettoplayagrowingroleintheenergysector,withseveralemergingtechnologiesaimingtoconvertvariousinputsintohydrogen,whichcanthenbeutilisedwithinthepowerandheatingindustries,andasfeedstockinthechemicalindustry.
Thegraphbelowillustrateshydrogenproductiontechnologiesandtheirpotentialenergysources:
Hydrogen
Inadditiontothesetechnologies,geologicalH2isemergingasapotentialsource.
Mostexistinghydrogenmarketsareveryspecific,consistingmainlyofindustrialuseandsupplyinginputsintoammoniaandmethanolproduction,actingalsoasareducingagentforthepetrochemical,chemical,steelandfoodindustries.
Presentusesofhydrogenasanenergycarrierremainlimited,andoftenexperimentalandpilot;however,
globalplanstoexpandthemaresignificant.Thereareseveraltechnologyadvancementprioritiestoaddressfortheseplanstomaterialise:
-Loweringcostsandgrowingtheircommercialtrackrecord.
-Storageandtransportationtechnologies,infrastructure,andstandards.
-Certificationdevelopment.
-End-userequipmentconversiontosupporthydrogenasfuel.
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1Methanereformation
I
Methane(CH4)canbeutilisedtocreatepurehydrogenusingthefollowingprocessofsteammethanereformation:
II
Byusingheat,steamandmethanereacttogetherwithacatalysttoformcarbonmonoxideandhydrogen;thisisanenergy-intensiveprocess.
Inthewater-gasshiftreaction,carbonmonoxideiscombinedwithmoresteam,
producinghydrogenandcarbondioxide.Thecarbondioxidecanthenbecapturedthroughcarboncapturetechnologies,asitisinacontrolledenvironment.
Ifcarboncaptureandsequestrationarenotutilisedduringthisprocess,therewillbecarbonemissions
associatedwithit.However,whencarboncaptureandsequestrationareaddedtotheprocess,thehydrogenproducedisconsideredlowcarbon,alsocalled“bluehydrogen”.
MethanereformingprocessforpureH2production
Thisprocessconsistsoffourstages:
IPretreatmentunittopre-formfeedstockandtoeliminatesulphurcompounds.
IIReformingsteptoproducesyngasusingeithersteammethanereforming,partial
oxidisationorautothermalreforming.Itispossibletocombinethesetechnologies.IIIShiftreactor(s)toconvertsyngasand(increaseH2contentanddecreaseCO).
IVThepurificationunitseparatesthehydrogenfromtheproductstream.CO2canbecapturedthroughcarboncapturetechnologies.
1
Pretreatment
2
SteamMethaneReforming
Partial
Oxidation
AutothermalReforming
Steam
Heat
3
Water-GasShiftConversion
4
CO2
NaturalGas,HeavyOil,Naphtha,LPG
O2
Steam
O2
CO2
Purification
Hydrogen
Catalysts:
-TherelativecatalyticactivityofmetalsintheSMRreaction:Ru>Rh>Ir>Ni>Pt>Pd
PartialOxidation
CH4+1/2O2>>CO+2H2H=36kJ/mol
-Conventionaliron-chromiumforhightemperatureWGSandcopperalloysforlowtemperatureWGS
AutothermalReforming
CH4+H2O>>CO+3H2CH4+1/2O2>>CO+2H2
Water-GasShift
CO+H2O>>H2+CO2H=41kJ/mol
SteamMethaneReforming
CH4+H2O>>CO+3H2H=206kJ/mol
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2Waterelectrolysis
Waterelectrolysisisawayofproducinghydrogenthatuseselectricitytosplitwaterintohydrogenand
oxygen.Whentheelectricityusedintheprocessisrenewableornuclear,therearenoGHGemissionsproducedintheprocess,andthiscanbereferredtoasrenewable,“green”and“pink”hydrogen,respectively.
Anelectricalcircuitiscreatedbycombininganelectrolyteandtwoelectrodestoformanelectrolyticcell.Thesechargedelectrodesthensplitthewater,withtheresultingnegativelychargedelectrodeattractingthepositivelychargedhydrogenionsand,conversely,thepositiveelectrodeattractingthenegativelychargedoxygenions
formingseparatebubblesofoxygenorhydrogenthatcanthenbecollected.
Therearefivemaintechnologiesusedtoperformwaterelectrolysis,whichdifferintermsofthematerialsusedfortheelectrodesandplates:
I
II
III
Alkalineelectrolysis
PEM(Protonexchangemembrane)electrolysis
SOEC(Solidoxideelectrolysis)
IVPCEC(Photoelectrochemical)
VAEM(Anionexchangemembrane)
Eachofthesefivetechnologieshasbenefitsanddrawbacks,rangingfromcost,efficiency,anddurability.
Thisiswhyfurtherresearchtoimproveperformanceandviabilityofwaterelectrolysisiscurrentlyongoing.
3Thermalgasification
Thermalgasificationisaprocessthatuses
solidorganicmatter(suchascoal,biomass-basedfeedstocks,SRFsandfractionsofnon-recyclableplastics)andconvertsthemintosyngasusing
hightemperatures(rangingfrom700-1500°C).Thereactionoccursunderstoichiometric
conditions(meaningallreactantsarecontrolledandfullyused),turningsolidresiduesinto
syngas.
Thesyngasisthenpurifiedtoremoveorganic
pollutants(suchaslightandheavytars)and
inorganicpollutants(suchashydrogensulphide,ammonia,andhydrochloricacid).Thisisthen
followedbythegas-watershiftreaction,which
meansthatthecarbonmonoxideproducedcan
beconvertedintoadditionalhydrogenandcarbondioxide.
Thegasesproducedarecollected,andhydrogenisextractedfromtheothergasesproduced(mainlycarbondioxide,carbonmonoxideandmethane)togivethehydrogenapurityofover99.9%.
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4Methanepyrolysis
Methanepyrolysisusesmethaneasfeedstockand,byapplyingenergytobreakthechemicalbondbetweencarbonandhydrogen,itproduceshydrogengasandasolidcarbonproduct.
Theprocessrequireslessenergythanelectrolysis,anditsGHGfootprintislowduetotheabsenceofemissions.
Usingnaturalgasasfeedstockalsoprovidesthebenefitofaccesstotheexistinginfrastructure.Therearedifferentwaysofgeneratingtheheatformethanepyrolysis:
IPlasmapyrolysis:electriccurrentsareusedtocreateahotplasmawhichbreaksdownthemethaneintohydrogenandcarbon.
IIThermalpyrolysis:hotbathsofmoltensaltsormetalsareusedtobreakdownthemethaneintohydrogenandcarbon.
IIICatalyticpyrolysis:methaneispassedthroughafluidisedbedcontainingacatalystwhichbreaksdownthemethanewithincreasedefficiency.
IVMicrowaveassistedpyrolysis:microwavesareusedwithacatalysttobreakthemethanemoleculeintohydrogenandcarbon.
5Solarphotocatalyticprocesses
SolarphotocatalyticprocessesavoidanyGHGemissionsastheyrelyexclusivelyonsolarpower:
aphotocatalyticinstallationwhichcouldbefurtherenhancedbytheadditionofsolarPVpanels.Inthis
process,aphoto-absorber(typicallyasemi-conductor)absorbslight,leadingtotheseparationofpositiveandnegativecharges.Thereductioncreateshydrogen,andoxidationproducesoxygen,hydrogen,and
e-charges,makingthemavailableforredoxreactions(transferofelectrons)toproducehydrogenfromwater.Thisbasicconceptisutilisedinseveraltechnologies:
I
Photocatalysed(PC)watersplitting:thissystemisthesimplestoneand
consists,typically,ofaphotocatalystimmersedinasolution,atthesurfaceof
whichthereactionstakeplace.Oxygenandhydrogenmustbefurtherseparated.
II
Photo-ElectroChemical(PEC)watersplitting:thissystemisbasedontheprincipleofelectrolysiswheretheanodeand/orcathodeareimplementedwithphotocatalysts.Thedifference,comparedtophotocatalysedwater
splitting,isthatthissystemiselectro-assisted,allowingthecurrenttobeincreasedforhigheryields.
III
Photo-ElectroChemical(PV-EC)watersplitting:thislastsystemisoftenassociatedwithPCandPECprocessesandconsistsofanelectrolyser
equippedwithanintegratedhighlyefficientmultijunctionIII-VPVcell.
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6Biologicalproduction
Therearetwomainbiologicalprocessesthatcanbeusedtoproducehydrogen:fermentationandbiophotolysis.
Thefermentationprocessharnessesmacro-nutrients(longmolecules)frombiomass,whicharebrokendown
intohydrogen,andshortmoleculessuchasalcohols,simplesugars,andvolatilefattyacids.Variousfermentationtechnologiesarelistedbelow,anditshouldbenotedthatphotofermentationandMECmustbecoupledwith
thefirststepofdarkfermentationinatwo-stepprocess.
IDarkfermentation(fermentationwithoutlight),wherethesubstrateusedisacomplexorganicmatter.Large-scalebacteriacanperformdarkfermentation.
IIPhoto-fermentation(fermentationassistedbylight),wherethesubstrateusedissmallorganicacids.
IIIMECfermentation(assistedbyalowelectricalcurrent),wherethesubstrateusedisasimplecarbonsourcesuchasC2toC6(volatilefattyacids,singlesugarandalcohols).
WhileBiophotolysisproduceshydrogenfromlightandwater,cyanobacteriaandgreenalgaecansplitwaterintohydrogenandoxygenusingtheirhydrogenaseornitrogenaseenzymesystem.
Macro-nutrientsfrombiomass
Carbohydrates,
proteins,
lipids
Image:iS
(alcohols,simple
sugars,volatile
fattyacids)
Bacteria
H2+shortmolecules
16IntroductiontoLowCarbonGasTechnologies
Diversification
7Geologicalextraction
TherearetwomainwaysofproducingH2throughgeologicalextraction:
Naturalhydrogenproduction(“white”hydrogen)
H2ismainlyproducedthroughnaturalwater-rockreactions,suchasserpentinisation,wherewater
reactswithiron-richmineralswithintheEarth’s
crust.Thishydrogenper
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