Energy from wet biomass waste -...

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Jan Zeevalkink

An assessment of existing and novel technologies

Energy from wet biomass waste

Energy from wet biomass, 6 May 20082

Energy from wet biomass

• Large potential of biomass/organic wastes with high water content (>50 %)

• Traditional, mature energy technology• Combustion: water content high• Anaerobic digestion: partial conversion of organics

• HydroThermal technology under development:• HTU® (HydroThemal Liquefaction) : diesel• Supercritical water gasification (SWG): H2/CH4

• Second generation option with no competition for food

Energy from wet biomass, 6 May 20083

Acknowledgment

• The evaluation was performed in the framework of the EMINENT 2 project, TREN/05/FP6EN/S07.56209/019886, funded by the European Community under the 6-th Framework Programme for Research and Technological Development

• More information on www.eminentproject.com

Energy from wet biomass, 6 May 20084

Content• Introduction• Wet biomass• Technology for energy from wet biomass• Hydro thermal processes

• The HTU process• Supercritical water gasification

• Alternatives• Combustion• Anaerobic digestion

• Processing chains• Results• Discussion• Concluding remarks

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Wet biomassExamples

• Wet solids, slurries with 10 to 50 % dry solids

• Organic fraction household waste (NL) `1.5 Mton/a (50 % dm)

• Road side grass (NL) 0.6 Mton/a (50 % dm)• Food and agro wastes (NL) 4.8 Mton/a (avrg 10 % dm)• Olive waste (EU) 3-5 Mton/a (dm)• Bagasse (world) 100 Mton/a (dm)

• Sustainable feedstock!

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SUFFICIENT RESOURCES?(HTU® opportunities at < 2€/GJ)

EUROPE• Agricultural / Industrial Residues 200 Mton dm/a (Olive Oil Waste 3-5 Mton dm/a)

•WORLD• Agricultural and industrial residues 5,000 Mton dm/a(Bagasse 100 Mton dm/a)

Total = 70 EJ/a

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POTENTIAL FOR ENERGY FROM BIOMASS

FROM POTENTIALLY AVAILABLE 250 EJ/YRLAND AREA

BIOMASS RESIDUES 70 EJ/YR

SHELL WORLD ENERGY SCENARIOS(spirit of the coming age) Biofuels 110 EJ/YR

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Energy from wet biomass

• Existing mature technology• Combustion water content high• Anaerobic digestion partial conversion of organics

• Technology in development• HTU® (HydroThemal Liquefaction) : biocrude (comparable

with an heavy oil) for diesel production,..• Supercritical water gasification (SWG): H2/CH4

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Hydrothermal Processing

• Processing in hot compressed water, liquid or supercritical

• Developments:1. biomass pre treatment for cellulose hydrolysis: production of

sugars (200 °C , 20 bar) without acid addition2. HTU®: proces for diesel, kerosine production (330 °C, 150 bar)3. SWG: Supercritical water gasification for production of methane

and/or hydrogen (600 ° C, 300 bar)

• No feedstock drying required!• Fit very well in biorefinery schemes: residual biomass processing

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Hydrothermal Upgrading

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HTU®

• Hydrothermal Upgrading/liquefaction

• Conversion at approx. 330°C en 150 bar to biocrude and CO2

• Raw materials: • wide variety of (wet) organic materials

sugar beet pulp, road side grass and others• Wood (residues)

• Biocrude: • High calorific value: 30 GJ/ton• Immiscible with water• Liquid above 80 °C• 10 – 15 % O2• Raw material for diesel fuel: hydrogenation

• Aim: production of renewable fuel

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HTU PRODUCT FLEXIBILITY

• Direct combustion as a liquid(replacement of fossil fuels)

• Combustion as a solid fuel (cofiring with coal)

• Emulsified fuel (type “Orimulsion”)

• Refinery feedstock

• Upgraded product

TP T

Heating

AutoclaveCollection vessel

Injector

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PROCESS DESIGN CASE STUDY

Basic process design by Jacobs Engineering Nederland

Case study:Feedstock: Sugar beet pulp, 22 %w dry matterIntake Capacity: 130,000 tonnes/year (dry basis)

Focus on heat integration, thermal efficiency and cost:

energy efficiency 75 % - 80 %

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Energy from wet biomass, 6 May 200815

HTU: business time line

Demonstration plant• 20 kton/a db (3 ton/hr db)• 17 Meuro capital investment

First commercial plant • 200 kton/a db (30 ton/hr db)• 32 Meuro capital investment

Pilot plant• 3 week trial run• 2 Meuro capital investment

Roll out in The Netherlands• 6 HTU plants 1,5 Mton/a db• 300 kton/a diesel (5 % of consumption)

First HTU consortium

New HTU consortium• Total, Paris• HVC, Alkmaar

2000

2005

2010

2015

2020

Lay out of demonstration plant (Jacobs Engineering)

Pilot plant at TNO Apeldoorn

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Hydrothermal Processing

Pilot plant 100kg/hr dry matter

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Supercritical Water GasificationConversion at approx. 600°C en 300 bar to H2, CH4 and CO2

• EC and national reseach projects with different feedstock• Ethanol, biodiesel, glycerol• Greenhouse waste (15 % slurry)• Diesel, gasoline

• Product gas: hydrogen, up to 60 % methane carbon dioxide, carbon monoxide C2-C4

• No tar, coke formation

• Very rapid reaction, mildly endothermic

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Process scheme SWG

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Supercritical Water Gasification• Aims

• development of multi-fuel processor

• production of high-pressure hydrogen as transportation fuel

• production of energy rich gas or SNG

• Specific advantage for• Wet feedstock

• Greenhouse waste• Household waste

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Supercritical Water Gasification

Continuouspilot

5 l/hr

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Economic perspective• 10 MWth output

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Case organic household waste

• Typical mass flow 35.000 ton/a dry matter

• Feedstock composition:• water content 50 %• ash content 30 % of dm• organics 40 % dm basis;

• of which: volatile organics 50 %, digestible forbiogas formation

• Low Heating value 11,3 MJ/kg (dm)

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Processing chainsShort name Step 1 2 3 4

Supercritical gasification SWG

Washing Wet milling SWG conversion

Gas combustion for power production

Hydrothermal liquefaction HTU®

Washing Wet milling HTU®

conversionCo

combustion for power production

Anaerobic digestion

Milling Anaerobic digestion

Gas engine for power production

Combustion Combustion Power generation

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Energy outputs and products

ProductInterme

diateIntermediate

Electricity

Cost indication

MW MWe M€/a

SWGhydrogen,

methane 10.5 gas 3.1 4.3*

HTU®

liquid fuel for

transport 10.5 crude 4.1 3.9*

Digestion SNG 6.6 gas 2.0 2.5*

Combustion 10.1 heat 2.8*** 5.6**

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Electricity output vs. water content

50 % water 70 % water 80 % water

SWG 3.1 3,1 3.1

HTU® 4.1 4.1 4.1

Digestion 2.0 2.0 2.0

Combustion 2.8*** 1.8 0.7

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Discussion• HTU® and SWG perform better than the existing mature technologies

anaerobic digestion and combustion.

• Power production of the combustion technology is for a feedstock containing 50 % water not inferior

• Advantage of the novel technology is more evident with higher water content.This underpins the definition for “wet biomass” slurries to have more than 50 % water

• Electricity production also depends on selected conversion process. SWG has a higher conversion factor to electricity when co combusted in power station or if fuel cells could be applied.

• Anaerobic digestion results in compost, HTU® in an alternative liquid fuel, SWG in an energy rich gas or hydrogen or methane. It also depends on the anticipated applications of the product which conversion technology to select.

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Conclusions• Hydrothermal processes provide efficient technology for the

conversion of sustainable biomass/organic wastes with a high water content

• HTU and SWG fit very well in biorefinery schemes for the processing of residual organic matter to obtain complete use of energy crops

• But: much R&D has to be done• HTU demonstration and product research• Research and development on SWG

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Thank you for your attention

Jan.zeevalkink@tno.nl

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AVAILABILITY OF ORGANIC RESIDUES IN THE NETHERLANDS

0

1000

2000

3000

4000

5000

-6 -4 -2 0 2 4 6

wood waste

food ind. waste

verge grasswood cuttings

beet leaves

houshold waste

potato leavesstraw

energy farming(NL)

Cumulativekton/year (db)

Price ( $/GJ )

Gasification,PyrolysisHTU

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SHELL WORLD ENERGY SECNARIOSspirit of the coming age

(in Exajoules/year) YEAR 2000 2050

WORLD PRIMARYENERGY DEMAND 400 1200

FOSSIL FUELS, 370 900Incl.Trad. Biomass & Nuclear

RENEWABLES 30 300

-HYDROPOWER 25 60

-BIOFUELS - 110

-OTHER RENEWABLES, INCL. BIOMASS POWER 5 130