Recent advances in biological biogas upgrading and valorization · 2020. 1. 16. · Recent advances...

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Recent advances in biological bio gas upgrading and valorization Raúl Muñoz Institute of Sustainable Processes, University of Valladolid (Spain)

Transcript of Recent advances in biological biogas upgrading and valorization · 2020. 1. 16. · Recent advances...

Page 1: Recent advances in biological biogas upgrading and valorization · 2020. 1. 16. · Recent advances in biological biogas upgrading and valorization Raúl Muñoz Institute of Sustainable

Recent advances in biological biogas upgrading and valorization

Raúl Muñoz Institute of Sustainable Processes, University of Valladolid (Spain)

Page 2: Recent advances in biological biogas upgrading and valorization · 2020. 1. 16. · Recent advances in biological biogas upgrading and valorization Raúl Muñoz Institute of Sustainable

Change in AD perception

WasteReduction

Technology

Electricityproduction

Multi-productBiorefinery

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AD as a multi-product Biorefinery Anaerobic Digestion as an effective Carbon and Nutrient recycling platform

Multi-productBiorefinery

ELECTRICITY & INDUSTRIAL HEAT

BIOMETHANE FORNATURAL GAS GRIDS

BIOMETHANE FOR VEHICLES

FINE & BULK CHEMICALS

BIOFERTILIZERS

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Biogas production plants in Europe

(EBA, 2018)

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Primary energy production from Biogasin Europe

Legal limitations in the use of energy crops

Lower tax incentives to electricity production

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Primary energy production from Biogasin Europe

Annual production of biogas in the EU will reach 41 Mtoe in 2030 (EBA)

Estimated annual production potential of biogas in the world can reach 658 Mt CH4

Other sourcesLivestock waste, urban solid

waste, energy crops, etc

(EBA, 2018)

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Electric capacity from Biogas in Europe

(EBA, 2018)

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Biogas quality requirements

UpgradingRequirements

INTERNAL COMBUSTION ENGINEES

Siloxanes < 9-44 ppmvH2S <200-1000 ppmv

TURBINES & MICROTURBINES

Siloxanes < 0.006 ppmvH2S <10000 ppmv

FUEL CELLS

Siloxanes < 1 ppmvH2S <10 ppmv

INJECTION INTONATURAL GAS GRIDS Standard

EN 16723-1

VEHICLE FUEL

Standard EN 16723-2

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Biogas upgrading plants in the IEA Bioenergy Task 37 group countries

(IEA Bioenergy 2018)

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Biomethane production in Europe

(EBA, 2018)

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Distribution of Biogas upgrading plantsin the IEA Task 37 group countries

2017

(EBA, 2018)

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The price of Biomethane

(Biosurf, 2016)

Biom

etha

ne c

ost(

ct€

kw

h-1)

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CO2 Removal Technologies

º

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CO2 Removal Technologies

PhysicalChemical

Biological

Scrubbing Water Chemical Organic solvent

Pressure Swing Adsorption

Membrane Separation

CryogenicSeparation

Photosynthetic

Electromethanogenesis

Others• Enzymatic• Fermentative• PPB-assisted

Hydrogenotrophic

A large portfolio of technologies

ABADBioenergy

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Distribution of CO2 removal technologiesin IEA Task 37 group countries

2012 2017

Membrane 25%

Water Scrubber 30%

ChemicalScrubber 18%

PSA

(IEA, 2018)(IEA, 2014)

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Biological CO2 Removal Technologies

Photosynthetic Upgrading

BIOFERTILIZER

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Photosynthetic Upgrading

Biological CO2 Removal Technologies

CH4

CO2

N2

O2

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Photosynthetic Upgrading

Key operational parameter: Recycling Liquid/Biogas ratio

Biological CO2 Removal Technologies

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Photosynthetic Upgrading

Biological CO2 Removal Technologies

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Photosynthetic Upgrading

Biological CO2 Removal Technologies

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Photosynthetic Upgrading

Upgrading Capacity: 300 Nm3/h of biogas

Biological CO2 Removal Technologies

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Photosynthetic Upgrading

Biological CO2 Removal Technologies

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Hydrogenotrophic Upgrading

Hydrogenotrophic archaea

Direct conversion

Indirect conversionKey

players

4H2 + CO2 → CH4 + 2H2O 𝞓𝞓G0 = -130.4 kJ mol-1

Biological CO2 Removal Technologies

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Biological CO2 Removal Technologies

Hydrogenotrophic In-situ Upgrading CH4

Gas Rate

CO2

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Hydrogenotrophic Ex-situ Upgrading

Biological CO2 Removal Technologies

Liquid recycle

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Hydrogenotrophic Ex-situ Upgrading

Biological CO2 Removal Technologies

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Hydrogenotrophic Ex-situ Upgrading

Biological CO2 Removal Technologies

Full Scale: in 2-3 years

eFUEL Project - Midtfyn Biogas Plant

BioUpgrade Project - Lemvig Biogas plant

Pilot Scale

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Biological CO2 Removal Technologies

Electromethanogenesis

Biogas

CH4 : CO2

H2

e-

Electromethanogenesis

8:1 (e- : CO2)

CH4 : CO2: H2

CH4

Methanation CO2 + 4 H2 CH4

Renewable Energy

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Electromethanogenesis

Biological CO2 Removal Technologies

HCO3- as main charge balancing ion Simultaneous desulphurization

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Biological CO2 Removal Technologies

Electromethanogenesis

0

20

40

60

80

100

0 100 200 300 400

Current density [A m-2]

Rem

oval

[%]

4000 L CO2 m-2 d-1

2000 L CO2 m-2 d-1

1000 L CO2 m-2 d-1

CO2 loading rate

CH4

CO2

H2

CH4

CO2

rem

oval

(%)

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PPB-assisted Upgrading

Biological CO2 Removal Technologies

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H2S Removal Technologies

º

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Based on the action of lithoautotrophs: H2S as energy source

Aerobic

Anoxic

e- acceptor: O2 or NO3-

EBRT = 2-16 min H2S-RE = 99%

O2/NO3-

Biological H2S Removal Technologies

Biotrickling Filtration

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Biological H2S Removal Technologies

NO3-

Raw biogas

BIOTRICKLING FILTER

Digestate(NH4

+)

NITRIFICATION TANK

H2S-EC = 280 gS m-3 h-1 (RE = 96%) EBRT= 3 min

Biotrickling Filtration

NH4+ + 2.5O2 NO3 + 2H2O

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Biological H2S Removal Technologies

O2

H2S- free Biogas

No need for external desulfurization

No impact on AD

Periodical cleaning of AD headspace

Microaerobic AD

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Biological H2S Removal Technologies

Microaerobic ADO2 generator

93 ± 3 % O2

2400m3 sludge digesterO2 inyection into the headspace

WWTP for 100,000 p.e.

Biogas compositionInfra-red & electrochem.(CH4, CO2, O2, N2 ,H2S)

Biogas flow rateUltrasonic flowmeter

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Biological H2S Removal Technologies

Microaerobic AD

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Biological H2S Removal Technologies

Microaerobic AD

H2S removal over 99%

Minimum N2 or O2 contamination of biogas

Minimum sulfur deposits outside the membrane surface

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Operating Cost of H2S Removal Technologies

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Siloxanes Removal Technologies

º

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Biological Siloxane Removal Technologies

Siloxanes are biodegradable Siloxanes removal is limited by gas-liquid mass transfer

Two-Phase Partitioning Bioreactors

TPPBs are based on the addition to a bioreactor of an immiscible,non-volatile, biocompatible and non-biodegradable organicsolvent with a high affinity for the target gas pollutant…..

e. g.Silicone oilHeptamethylnonane

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Biological Siloxane Removal Technologies

Two-phase partitioning Bioreactors

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Biogas bioconversion into commercial bioproducts

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Biogas bioconversion into commercial bioproducts

BiogasBiorefinery

ECTOINESINGLE CELL PROTEIN

EXOPOLYSACCHARIDES

CHEMICAL BUILDINGBLOCKS

BIOPOLYMERS

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Biogas bioconversion into commercial bioproducts

Culture condition

PHA

PHA content(wt %)

HB fraction(mol %)

HV fraction(mol %)

Biogas 43.1 ± 1.8 100 0

Biogas + Acetic acid 52.3 ± 0.7 100 0

Biogas + Propionic acid 47.9 ± 0.7 98 2

Biogas + Butyric acid 52.2 ± 2.1 100 0

Biogas + Valeric acid 53.8 ± 0.8 75 25

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Biogas bioconversion into commercial bioproducts

100 % biogas to CHP

1000 Nm3 biogas h-1

55 % biogas to CHP+ 45 % biogas to PHA

100 % biogas to PHA

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Biogas bioconversion into commercial bioproducts

PHA production ~ 1,900 kg PHA d-1

PHA selling price ~ 7,1 € kg-1PHA production ~ 800 kg PHA d-1

PHA selling price ~ 4,4 € kg-1

+0,06 € Nm-3

+0,09 € Nm-3

+0,09 € Nm-3

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Biogas bioconversion into commercial bioproducts

Ectoine is an osmotic cellprotector with a highmarket value (> 1000 € kg-1)

TLR 5 TLR 7

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TAKE HOME MESSAGES

Anaerobic digestion can be engineered as a multi-product biorefinery

Biotechnologies for biogas upgrading are being successfully scale-up and validated

Biogas represents a valuable feedstock for the production of commodities and high-addedvalue products

Power-to-gas has attracted most research efforts in the field of biological biogas upgrading

TPPB can support an effective siloxane removal

Biological desulfurization methods provide high H2S-REs at low operating costs

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Acknowledgements

Funding agencies:

Co-authors

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