Production of Biomethane/Synthetic Natural Gas (SNG… · Production of Biomethane/Synthetic...

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Production of Biomethane/Synthetic Natural Gas (SNG) from Dry Biomass A Technology Review 2015 Serge Biollaz, Tilman Schildhauer Paul Scherrer Institut, Switzerland Jörgen Held Renewtec AB, Sweden Reinhard Seiser University of California San Diego, USA

Transcript of Production of Biomethane/Synthetic Natural Gas (SNG… · Production of Biomethane/Synthetic...

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Production of Biomethane/Synthetic

Natural Gas (SNG) from Dry Biomass –

A Technology Review 2015

Serge Biollaz, Tilman Schildhauer

Paul Scherrer Institut, Switzerland

Jörgen Held

Renewtec AB, Sweden

Reinhard Seiser

University of California San Diego, USA

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Gasification Methanation Gas conditioning

for natural gas grid

dust, S, Cl, (CO2), etc. H2O, CO2, (H2)

SNG Biomass Gas cleaning &

- conditioning

For each process step several options exist

Biomass and Bioenergy. 2009, 33, 1587 – 1604, M. Gassner, F. Maréchal

Find the “best” combination

Power-to-Gas

Conversion Process “Biomass-to-SNG” Multiple concepts & combination of unit operation exist

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Gasification Methanation Gas conditioning

for natural gas grid

SNG Biomass Gas cleaning &

- conditioning

Conversion Process “Biomass-to-SNG” Carbon management

CO + 3 H2 CH4 + H2O methanation

CO + H2O CO2 + H2 water gas shift

C2H4 + 2 H2O 2 CO + 4 H2 steam reforming

C2H4 + x H2 C2H6, CH4 hydrogenation

C + ½ O2 CO gasification

C + H2O CO + H2 steam gasification

C + CO2 2 CO CO2 gasification

Gasification

Methanation, shift, etc.

x = 1 or 2

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Gasification Methanation Gas conditioning

for natural gas grid

dust, S, Cl, (CO2), etc. H2O, CO2, (H2)

SNG Biomass Gas cleaning &

- conditioning

Conversion Process “Biomass-to-SNG” Sulfur management

C4H4S + 4 H2 H2S + C4H10 hydrodesulfurisation

H2S + Me(O) MeS + H2(O) chemisorption

Sulfur chemistry

MeS + 1.5 O2 MeO + SO2 regeneration

COS + H2O CO2 + H2S hydrolysis

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0

5

10

15

1 10 100 1000

Biomass input [MWFuel]

bio

me

tha

ne

pro

du

cti

on

co

st

[c€

/kW

h]

~ large ~ medium ~ small

biomass, thermo-chemical

biogas

coal, thermo-chemical

Indicative classification

for different scales:

GoBIGas I E.On Bio2G

biogas

GoBIGas I GoBIGas II

(planning)

Bio2G

(planning)

hRNG: 60 … 70 %

hheat: 0 … 20 %

biomass, biological

Scale of SNG/RNG/Biomethane Installations

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EF

Gasification technologies: HPR: Heat pipe Reformer DFB: Dual Fluidized Bed

BFB: Bubbling Fluidized Bed CFB: Circulating Fluidized Bed EF: Entrained Flow

Selected key Technologies for SNG production Application Range

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Large-scale Thermo-chemical Conversion: Coal

• Dakota Gasification Company: Great Plains Synfuels Plant

• New coal-to-SNG in China (4’000 MWfuel, coal) : Siemens, Haldor Topsoe

• New methanation technology VESTA,

demonstration in China

http://www.gasification.org/uploads/eventLibrary/GTC-2012-5-4.pdf

http://www.gasification.org/uploads/eventLibrary/07HANNEMANN.pdf

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Large-scale Biomass Plants (>200 MWfuel)

• Lower specific investment and non-fuel operating costs

costs due to large plant size.

• Use of established technologies from the coal and refining

industry.

• Oxygen plant and pressurized systems can be employed.

• Difficult feedstock logistics. (Near ports or inclusion of coal

in the feedstock mix)

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• Acceptable feedstock logistics (size similar to existing

biomass boilers)

• Easier to match excess heat with local heat or steam

demand

• Down-scaling of large-scale technologies generally leads to

unattractive specific investment costs.

• Indirect gasification and fluidized-bed methanation are

technologies with high conversion efficiency.

• Gas cleanup becomes economic hurdle due to several

process steps.

Medium-scale Biomass Plants (~100 MWfuel)

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Indirect Gasification – Industrial-scale Plants

Location/

Technology

Usage or

product

Fuel/Product

MW/MW

Start up Status

Güssing, AUT

FICFB

Gas engine/

BioSNG demo

8fuel / 2el

1 MWSNG

2002

2009

Operational

-

Oberwart, AUT

FICFB

Gas engine/ORC 8.5fuel / 2.8el 2008 Operational

Senden, DE

FICFB

Gas engine/ORC 14fuel / 5el 2011 Operational

Burgeis, IT

FICFB

Gas engine 2fuel / 0.5el 2012 Operational

Gothenburg, SWE

FICFB

BioSNG 32fuel / 20SNG 2013 Operational

Alkmaar, NL

MILENA

BioSNG 4fuel / 2.8SNG Planned

FICFB = Fast Internally Circulating Fluidised Bed

MILENA = Multipurpose Integrated Lab-unit for Explorative and Innovative Achievements in biomass gasification

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BioSNG Pilot Plants

Location/

Technology

R&D Capacity Start up Status

Petten, NL

MILENA

ECN - R&D 800 kWfuel 2008 Operational

California, US

FICFB

Woodland project

- R&D fluidized

bed methanation

1 MWfuel 2013 Commissioning

Lyon, FR

FICFB

GAYA project -

R&D platform

500 kWfuel Under

construction

Gothenburg, SWE

Dual bed

Chalmers

R&D

2 MW 2007 Operational

Köping, SWE

WoodRoll®

Ultraclean syngas

- R&D

500 kWfuel Commissioning

Swindon, UK

FBG+Plasma

Gas cleaning -

R&D

500 kWfuel 2015 Operational

FBG = Fluidized Bed Gasifier

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https://www.dbfz.de/fileadmin/user_upload/B_Kraftstoffe/Final_project_report_biomethan.pdf

EU Project “BioSNG”: 2006-2009 FICFB gasification with fluidized-bed methanation

BioSNG pilot plant

Block flow diagram of BioSNG pilot plant

in Güssing, AT

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BioSNG Project in Sweden Industrial plant “GoBiGas”

http://www.ieatask33.org/app/webroot/files/file/2013/Workshop_Gothenburg/19/Thnuman.pdf

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BioSNG Project in the Netherlands ECN System for MEthanation (ESME)

ftp://ftp.ecn.nl/pub/www/library/report/2015/l15044.pdf ftp://ftp.ecn.nl/pub/www/library/report/2015/e15008.pdf

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http://www2.nationalgrid.com/UK/Our-company/Innovation/Gas-distribution-innovation/NIC-Projects/BioSNG-Process-Diagram/

BioSNG Project in United Kingdom Gas cleaning with plasma

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BioSNG Project in Japan Gasification concept for scaling DFB up to 200 MWfuel

http://www.nedo.go.jp/content/100545716.pdf, p. 40

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RNG Efforts in California

• Natural gas constitutes 33% of primary energy consumption

• Aggressive Greenhouse-gas reduction goals, various RNG incentives

• Electrical utility SMUD performing techno-economic evaluation of a

100 MWFuel, 60 MWRNG demonstration plant

Evaluation of gas-cleanup

technologies (sulfur compounds)

at small scale.

Solid adsorbents:

- Microporous, nanoporous

carbon (Brightblack)

- MOFs

Woodland RNG Research Project:

FICFB Pilot Plant, 1 MWFuel Laboratory-scale fluidized-

bed methanation (5 l/min).

CH4, CO2

Producer gas

Sulfur-free

producer gas

As part of the gas-cleanup chain

… …

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• Lower financial risk due to a lower investment cost

• Easier to secure the future feedstock supply

• Easier logistics since less feedstock is needed

• Best match with local heat demand in cold climates

• Possible synergies with existing biogas plants

• Indirect gasification is commercially available for small

scale plants

• Technologies developed for small scale preferred

compared to scaling down large-scale technologies

Small-scale Biomass Plants (~10 MWfuel)

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Lowering Investment and Operation Costs

• Larger plant size decreases specific investment and operating costs

Feedstock delivery to ports

Feedstock pretreatments

Blending with coal

• Increased automation

• Cheaper feedstocks: Urban wood, RDF, MSW – but tradeoff with

higher costs for separation, operational difficulties, and gas cleaning

• Higher carbon conversion by merging with power-to-gas route

• For methanation

Removal of organic sulfur compounds without removing BTX

Sulfur-tolerant methanation catalysts

Reduction/simplification of gas cleanup steps

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Projects on Thermo-chemical SNG Production Observation on the focus of the R&D activities

• A multitude of gasification processes exist to produce a syngas suitable

for SNG/biomethane production.

• DFB is the dominant design (FICFB, MILENA, TIGAR, ..)

Gasification

Reforming, shift, methanation, etc.

• A multitude of gas cleaning and methanation processes exist to

produce a (ultra) clean syngas suitable for SNG / biomethane

production.

• There is no dominant design yet.

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Acknowledgments

USA

Switzerland

Sweden

BFE KTI/CTI SNF

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Backup Slide - Natural Gas Consumption

UK* Nether- lands*

Switzer- land*

Sweden* Austria* US California

Natural gas consumption

[PJ/y] 3,300 1,430 115 65 290 26,200 2,638

Natural gas as fraction of prim. energy consumption

[%] 38% 44% 10% 3% 22% 26% 33%

Natural gas import dependency

(import-export) / consumption

42% 0% 100% 100% 75% 5% 90%

Biomass availability [% of prim. energy, 2020]

5% 5% 10% 20-25% 20% 8% 7%

http://www.ieatask33.org/app/webroot/files/file/2012/IEA%20Bioenergy%20Conference/SessionI1-van_der_Drift.pdf http://www.energydelta.org/mainmenu/energy-knowledge/country-gas-profiles http://www.energie-nederland.nl/wp-content/uploads/2011/08/Energie-in-Nederland-2011.pdf

*Sources: