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VTT TECHNICAL RESEARCH CENTRE OF FINLAND LTD Doubling the output of synthetic biofuels - Exploiting synergies between biomass and other RE sources INTERNATIONAL SEMINAR ON GASIFICATION 2016 Dr Ilkka Hannula
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Page 1: Doubling the output of synthetic biofuels - Exploiting ......Bench-scale BFB gasification, filter and reformer testing facilities, 5 kg/h Pressurized (1-10 bar) fixed-bed pilot plant

VTT TECHNICAL RESEARCH CENTRE OF FINLAND LTD

Doubling the output of syntheticbiofuels - Exploiting synergies betweenbiomass and other RE sources

INTERNATIONAL SEMINAR ONGASIFICATION 2016Dr Ilkka Hannula

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2

Bioruukki Pilot CentreSpeed to scale-up of bio and circular economy innovations

VTT BioruukkiA new piloting ecosystemfor process industry scale-upand demonstrations.A former printing planttransformed to world scaleR&D centre.8000 m2, room for severalpilot units and laboratories.Located close to Otaniemicampus.

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324/10/2016 3

THERMOCHEMICALCONVERSION

PLATFORM

Gasification andpyrolysis

technologies forbiofuels,

biochemicals andmaterials

Full operationstarted 2015

1

BIOMASSPROCESSING

PLATFORM

Innovativebiomass

fractionation andprocessing fornew biobasedvalue chains

Starts at Bioruukki2017

3

GREEN CHEMISTRYPLATFORM

Sustainable processchemistry and

bioprocesses forbiochemicals andtailored biobasedhybrid materials

Starts at Bioruukki2018

4

ENERGY STORAGEPLATFORM

Storage conceptsfor solar and wind

energy throughmono carbon gases

to chemicals andmaterials

Starts at Bioruukki2016

2

Bioruukki Pilot Centre - Value from integration

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424/10/2016 4

Gasification pilots at BioruukkiKey research and scale-up offering

Excellent know-how on fuel chemistry and gasification processesUnique fluidized bed gasification, catalytic gas cleaning and hot filtration

test facilities from laboratory to pilot scaleCutting-edge tools for techno-economic evaluations and modelling

Main equipment at BioruukkiDual Fluidized-Bed steam gasification pilot plant for syngas applications.

Atmospheric pressure, feed capacity 80 kg/h. Hot filtration, catalytic reformingCFB gasification pilot plant for syngas and fuel gas. Air-blown operation,

steam-O2 gasification. Hot filtration, catalytic reformingBench-scale BFB gasification, filter and reformer testing facilities, 5 kg/hPressurized (1-10 bar) fixed-bed pilot plant for CHP and syngas

applications, feed capacity 80 kg/h

Development plans for BioruukkiNew test possibilities for waste and recycling raw materials

Gasification Platform is used for gasification process development, testingof new feedstocks and for the development of gas cleaning technologies.Gasification Platform is used for gasification process development, testingof new feedstocks and for the development of gas cleaning technologies.

BFB100 Test facility

DFB Test facility

Pressurized FixedBed Pilot Plant ( 2016 )

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524/10/2016 5

Timetable: 1.1.2016 – 31.12.2017, Total budget: 2.7 M€Industrial partners: Fortum, Gasum, Helen, Kumera Corporation, GasificationTechnologies, Brynolf Grönmark, ÅF-Consult, Woikoski, Dasos Capital,Kokkolanseudun Kehitys, MOL / Hungary.

Timetable: 1.1.2016 – 31.12.2017, Total budget: 2.7 M€Industrial partners: Fortum, Gasum, Helen, Kumera Corporation, GasificationTechnologies, Brynolf Grönmark, ÅF-Consult, Woikoski, Dasos Capital,Kokkolanseudun Kehitys, MOL / Hungary.

BTL2030-projectBTL2030-project: Production of transport fuels from biomass by gasification-based concepts integrated to energy consuming industries and district heat powerplants – pilot tests and feasibility studies

Website: http://www.vtt.fi/sites/BTL2030/en

The target of this project is a medium-scale BTL concept, which can beintegrated to different kind of energy intensive industries and district heatingpower plantsThe new gasification process is being developed at the DFB pilot plant ofVTT Bioruukki and the feasibility of the process is studied together withindustrial partners representing different potential applications and rolesin the value chain.

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624/10/2016 6

Displacement of crude oil derived productswith carbon neutral alternatives

Possibly the most difficult aspect of climate change mitigationLack of attention (electricity, electricity, electricity)Deeply related to decarbonisation of transportation

Many confusing aspects/arguments around the problem:The Great Electricification will solve the problemMcKinsey curve argument: important, but not yetIntricate sustainability issues: biomass as an umbrella termPerceived supply constraints of sustainable biomass

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724/10/2016 7

Global transportation energy demand in 2050

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824/10/2016 8

Global transportation energy demand in 2050

Global transportation energydemand in the reference year 201092 EJ/yr

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924/10/2016 9

Global transportation energy demand in 2050

IEA baseline estimate fortransportation energyconsumption in 2050 is 161 EJ/yr.

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1024/10/2016 10

Global transportation energy demand in 2050

IEA estimate for transportation energydemand in 2050 that is consistent with2°C scenario is 99 EJ/yr (2357 Mtoe/a).

62 EJ

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1124/10/2016 11

Global transportation energy demand in 2050

Global transport emissions in 2010 were 8 GtCO2-eq/yr.

To achieve 60 % reduction (relative to 2010),2050 emissions < 3.2 GtCO2-eq/yr

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1224/10/2016 12

Global transportation energythought experiment*

Two ”Though Experiments”created to highlight energysupply needs in 2050.

*Adapted from GEA, 2012

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1324/10/2016 13

Global transportation energythought experiment*

Capping emissions at 3.2 GtCO2-eq/yrMax 38 EJ/yr Crude Oil Derived Products (CODPs) allowedBalance needs to come from carbon-neutral electricity & fuels

38EJ/yr

*Adapted from GEA, 2012

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1424/10/2016 14

Global transportation energythought experiment*

Scenario”IEA BEV” (BEV = Battery Electric Vehicle) is based on IEA2050 estimate on transportation electricity demand: 2500 TWh/yr.

9 EJ/yr

*Adapted from GEA, 2012

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1524/10/2016 15

Global transportation energythought experiment*

Whatever the balance of 55 EJ/yr will be,it needs to fulfill two requirements1) Be a fuel2) Be carbon-neutral

55EJ/yr

*Adapted from GEA, 2012

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1624/10/2016 16

Global transportation energythought experiment*

Scenario ”Max BEV” assumes completeelectrification of the light road sector: 7800 TWh/yr.

28 EJ/yr

*Adapted from GEA, 2012

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1724/10/2016 17

Global transportation energythought experiment*

The need for carbon-neutralfuels in this scenario is 17 EJ/yr

17 EJ/yr

*Adapted from GEA, 2012

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1824/10/2016 18

Global transportation energythought experiment*

For context: 1 EJ/yr equals 700 synfuelplants each having 100 MWbiomass capacity

17 EJ/yr55EJ/yr

*Adapted from GEA, 2012

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1924/10/2016 19

What is the supply potential of sustainablebiomass?

From AR5 (IPCC, 2014):“…This assessment agrees on a technical bioenergy potential ofaround 100 EJ (medium evidence, high agreement), and possibly300 EJ and higher (limited evidence, low agreement)…”

From IEA (2011):“…with a sound policy framework in place, it should be possible toprovide … 145 EJ of total biomass for biofuels, heat and electricityfrom residues and wastes, along with sustainably grown energy crops.”

80 EJ of biomass assumed for generating heat and power65 EJ of biomass assumed available for biofuel feedstock

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2024/10/2016 20

What is the supply potential of sustainablebiomass?

Assuming 80 EJ for heat and power and 50 % overall BTL efficiencySupply potential estimate based on

IPCC data = 10 EJIEA data ~ 30 EJ

Demand of CNFMax Electric = 17 EJ/yrIEA Electric = 55 EJ/yr

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2124/10/2016 21

What is the supply potential of sustainablebiomass?

Assuming 80 EJ for heat and power and 50 % overall BTL efficiencySupply potential estimate based on

IPCC data = 10 EJIEA data ~ 30 EJ

Demand of CNFMax Electric = 17 EJ/yrIEA Electric = 55 EJ/yr

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2224/10/2016 22

PEAT AMMONIAPLANTOULU, FINLAND, 1991

SYNGAS FOR FT-DIESELo Large-scale O2-blown gasifiero Innovative hot gas cleaningo Technology from Finlando R&D and IPR support from VTTo Large-scale plants > 300 MW

HYDROGEN FORAMMONIA (140 MW)oCoal gasification

applied to peatoR&D support

by VTT

NSE BIOFUELS DEMO, VARKAUS, FINLAND,2011

NEW PROCESS FOR SMALLER SCALEo Simpler process and lower capexo Wide feedstock basis, target scale 30-150 MWo Biofuels, SNG, hydrogen, bio-chemicalso Process development at VTT in 2016-18o Industrial demonstration in 2019-20

PILOT PLANT AT VTT BIORUUKKI, ESPOO, 2016

2010 2015 20201985 2005 203020001995 2025

Biomass gasification for biofuels and bio-chemicalsLong experience of medium-to-large scale thermochemical biorefineries

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Biomass can be converted to synfuels with an efficiency in the range of 50 – 60 %(LHV), depending on the process configuration and end-product.

If by-product heat from the process can also be utilised, additional 20 – 30 %-point improvement can be attained, leading to ~ 80 % overall efficiency

Despite the high energy efficiency, more than half of feedstock carbon isrejected from the process, as there is not enough hydrogen to convert it into fuels.

The traditional conversion route is therefore hydrogen constrained.

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Feed carbon

Surplus carbonFeed hydrogenBiomass

feedstockFuel

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By adding hydrogen from external source (enhancement),the surplus carbon could be hydrogenated to fuel as well.

Feed carbon

Surplus carbon

External hydrogen

Feed hydrogenBiomassfeedstock

Fuel

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By adding hydrogen from external source (enhancement),the surplus carbon could be hydrogenated to fuel as well.

Feed carbon

Fuel

Surplus carbon

External hydrogen

Feed hydrogenFuelBiomass

feedstock

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But the surplus carbon is in the form of CO2 instead of CO!

CO

FuelH2

H2Biomassfeedstock

Fuel

CO2

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Implications:- Only methane and methanol have reaction routes via CO2- More H2 is required to produce one mole of fuel from CO2 than from CO- CO2 has higher activation energy than CO- Byproduct water from CO2 hydrogenation inhibits methanol catalysts

CO

Fuel

CO2

H2

H2Biomassfeedstock

Fuel

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Despite challenges related to CO2 hydrogenation, the potentialincrease in fuel output is significant.

Fuel

CO

H2

CO2

Biomassfeedstock

H2

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The process is not sensitive to the source of hydrogen, butproduction from water via electrolysis using low-carbonelectricity is considered in this presentation

O2

Fuel

Conversion

CO

H2

CO2

Biomassfeedstock

H2Low-C

electricity Electrolysis

Conversion

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Gasoline via oxygen gasification (carbon flows)

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Gasoline via steam gasification

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Gasoline via enhanced steam gasification

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Gasoline via enhanced oxygen gasification

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Gasoline via oxygen gasification (energy)

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Gasoline via enhanced oxygen gasification (energy)

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SUMMARY

When the maximally enhanced by an external H2 source, followingincreases in fuel output can be observed:

2.2-fold (methane) or 1.9-fold (gasoline) for steam gasification;3.1-fold (methane) or 2.6-fold (gasoline) for oxygen gasification.

Overall carbon conversions for enhanced configurations:67.0% (methane) and 58.4% (gasoline) for steam gasification;98.0% (methane) and 79.4% (gasoline) for oxygen gasification.

Econ. feasible over base case when low-GHG H2 cost lower than2.2 €/kg (methane) and 2.7 €/kg (gasoline) for steam gasification;2.4 €/kg (methane) and 2.8 €/kg (gasoline) for oxygen gasification.

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GHG emission balances for H2 enhancedsynthetic biofuels

Source: Koponen and Hannula (2016)

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41Source: Koponen and Hannula (2016)

GHG emission balances for H2 enhancedsynthetic biofuels

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4224/10/2016 42

Take-home messages 1/2

Manufacture of synthetic biofuels makes for an efficient use ofbiomass, provided that close attention is paid to heat integrationissues.More than half of biomass carbon not utilised in fuel productionRenewable and sustainable carbon a scarce resource globallyBoth the use of biomass (energy efficiency) and land (resourceefficiency) for bioenergy purposes should be as efficient aspossible.This aspect not often discussed in relation to bioenergy.

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4324/10/2016 43

Take-home messages 2/2Significant increase in biofuel output could be attained via H2 enhancementHowever, to ensure deep emission savings, electricity needs to come froma very low carbon source: Significant impact presumes that electric gridsare first largelydecarbonised

Costs also a major issue.

H2 enhanced biofuelsstill the least-costsolution for largescale decarbonisationof the hydrocarbonsupply system?

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References

• GEA, 2012. Global Energy Assessment - Toward a Sustainable Future, Chapter 12 FossilEnergy, Cambridge University Press, Cambridge, UK and New York, NY, USA and theInternational Institute for Applied Systems Analysis, Laxenburg, Austria.

• Hannula, I. 2016. Hydrogen enhancement potential of synthetic biofuels manufacture in theEuropean context: A techno-economic assessment, Energy, Volume 104, Pages 199-212, ISSN0360-5442, http://dx.doi.org/10.1016/j.energy.2016.03.119.

• IEA, 2011. Technology Roadmap. Biofuels for transportation• IPCC (Intergovernmental Panel on Climate Change), 2014. Climate Change: Technical

Summary of Mitigation of Climate Change, Working Group III contribution to the 5th

Assessment Report of the Intergovernmental Panel on Climate Change.• Koponen, K. and Hannula I. (to be submitted), 2016. GHG emission balances for hydrogen

enhanced synthetic biofuels from solid biomass.

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