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Renewable and Sustainable Energy Reviews
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Role of stage-separation in the ubiquitous development of Anaerobic
Digestion of Organic Fraction of Municipal Solid Waste: A critical review
Biswabandhu Chatterjee
⁎
, Debabrata Mazumder
1
Department of Civil Engineering, Environmental Engineering Cell, IIEST, Shibpur, Howrah, 711103 West Bengal, India
ARTICLEINFO
Keywords:
Biohythane
Digestate
OFMSW
Stage-separation
Three-stage AD
Two-stage AD
ABSTRACT
Managing the ever increasing load of municipal solid waste (MSW) has been one of the biggest challenges for
municipalities all over the world. According to World Bank reports, the global generation of MSW per year is
expectedtoriseto2.2billiontonsby2025.Organicfractionofthemunicipalsolidwaste(OFMSW)accountsfor
more than 40% of the generated MSW. Anaerobic digestion (AD) has been a popular technique for OFMSW
management due to its potential to generate methane and a semi-stabilized digestate, which can be further
processedasasubstituteforinorganicfertilizers.Mostoftheexistingfull-scaleADtreatmentplantsstabilizing
OFMSW are single-stage based. However, with the increase in OFMSW generation-rate phase separation in AD
has become more pertinent. Compared to single-stage AD systems, multi-stage AD systems are capable of not
onlytreatinganincreasedloadofOFMSWbutalsoproducinggreatermethaneandbio-hydrogen.Mostrecently
onlyahandfuloffull-scaleADplantsinEuropehaveshiftedtotwo-stagesystems.Efciencyintermsofenergy
recoveryhasbeenreportedtobeupto94.5%and86%formulti-andsingle-stageADsystems,treatingorganic
solidwaste,respectively.Thiscanbeonlyenhancedfurtheriftheoperatingconditionsoptimumforeachphase
is properly maintained. In three-stage AD systems, pH suitable for hydrolysis (4–5), acidogenesis (5–6.5) and
methanogenesis (6.8–7.5) can be easily maintained. Not only that, three-stage AD systems also ofer provision
for variation in loading-rates and retention-times suitable for individual phases. Furthermore, multi-stage AD
systems provide a scope for improved trace-element supplementation, which results in 10–50% performance
increase per unit reactor volumes. The present review clearly illustrates the need to switch over to two- and
three-stage AD systems for stabilizing OFMSW.
1. Introduction
EarlyADofOFMSWwasmostlycarriedoutinsingle-stagedigesters.
As such, till the end of the 20th century majority of the researchers
worked on the development of AD of OFMSW, based on single-stage
systems.Themainproblemwiththesingle-stagebasedADsystemswas
low biogas production. With the increase in the demand for biogas
basedenergytwo-stageADofOFMSWcameintothefore.Assuch,since
thestartofthe21stcenturymostofthemajordevelopmentsinthe feld
of AD of OFMSW have been based on two-stage AD systems. The se-
paration of the methanogenic phase, from the hydrolytic and the
acidogenicphasenotonlyledtofasterdegradationofthefeedstockbut
https://doi.org/10.1016/j.rser.2019.01.026
Received 4 April 2018; Received in revised form 18 November 2018; Accepted 10 January 2019
Abbreviations: AD, Anaerobic Digestion; AcoD, Anaerobic co-digestion; AOA, Ammonia Oxidizing Archaea; AOB, Ammonia Oxidizing Bacteria; ATP, Adenosine
Triphosphate; BCS, Biofertiliser Certifcation Scheme; BMP, Biomethane Potential; BOD, Biochemical Oxygen Demand; CNG, Compressed Natural Gas; COD,
Chemical Oxygen Demand; CST, Continuous Stirred Type; DOC, Dissolved Organic Carbon; EBA, European Biogas Association; FA, Free Ammonia; FAN, Free
Ammonia Nitrogen; FVW, Fruit and Vegetable Waste; FW, Food Waste; HRT, Hydraulic Retention Time; KW, Kitchen Waste; LCFA, Long Chain Fatty Acid; NP,
NitrogenPhosphorus;OFMSW,OrganicFractionofMunicipalSolidWaste;OLR,OrganicLoadingRate;ORP,OxidationReductionPotential;PAS,PubliclyAvailable
Specifcation;QP,QualityProtocol;RDF,RefuseDerivedFuel;SCFA,ShortChainFattyAcid;sCOD,solubleChemicalOxygenDemand;SHARON,SinglereactorHigh
activity Ammonia Removal Over Nitrite; S-L, Solid-Liquid; SMP, Specifc Methane Production; SRT, Solids Retention Time; SS, Suspended Solids; TAN, Total
AmmoniaNitrogen;tCOD,totalChemicalOxygenDemand;TE,TraceElement;TKN,TotalKjeldahlNitrogen;TN,TotalPhosphorus;TOC,TotalOrganicCarbon;TP,
TotalNitrogen;TPAD,TemperaturePhasedAnaerobicDigestion;TS,TotalSolids;TSAD,Three-StageAnaerobicDigestion;UASB,Up-fowAnaerobicSludgeBlanket;
VFA,VolatileFattyAcid;VS,VolatileSolids;VSS,VolatileSuspendedSolids;VW,VegetableWaste;WAS,WasteActivatedSludge;WRAP,Waste&ResourcesAction
Programme
⁎
Correspondence to: Indian Institute of Engineering Science and Technology (IIEST), Shibpur, Howrah, 711103 West Bengal, India.
E-mail address: debabrata@civil.iiests.ac.in (D. Mazumder).
1
Postal address: Indian Institute of Engineering Science and Technology (IIEST), Shibpur, Howrah, 711103 West Bengal, India.
Renewable and Sustainable Energy Reviews 104 (2019) 439–469
1364-0321/ © 2019 Elsevier Ltd. All rights reserved.
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