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TCCS9 Trondheim 2017
www.ecn.nl
STEPWISE: cost effective capturing
of CO2 in the Iron & Steel industry
Sorption-Enhanced Water-Gas Shift (SEWGS)
TCCS9, Trondheim
13/06/2017
TCCS9 Trondheim 2017
Sorption-Enhanced Water Gas Shift
Sorption-Enhanced Water-Gas Shift - SEWGS
• Platform Technology for Syngas Treatment – Upgrade Blast Furnace Gas: remove CO2, convert CO to H2
– Valorization of H2 in CO2/CO containing syngas streams
• Technology - High carbon capture ratio with unique low steam use (H2O/CO2 < 1.0)
- Able to operate under sour conditions and to remove H2S as well as CO2
- SEWGS technology builds further on the vast industrial experience with PSA systems.
- Combination of several process steps into one (process intensification)
- Highest efficiencies for short-to-medium term developments
• Cost effective CCS solution for BFG – For BFG, cost per ton CO2 avoided estimated 25% lower than state of the art
TCCS9 Trondheim 2017
ECN’s current involvement in
decarbonisation of the Iron & Steel industry
Decarbonisation of blast furnace gas (BFG) for the iron & steel industry power plant
Utilization of the energy content of the residual steel gases for production of methanol from CO2
Use timely power price opportunities, in order to provide affordable H2 for current uses in the steel making processes
Wednesday 13:20-40 D5-CCUS
TCCS9 Trondheim 2017
SEWGS
• Sorption-Enhanced Water-Gas Shift (SEWGS) – Initial targeted application Carbon Capture and Sequestration (CCS)
– Power production with CO2 capture
CO + H2O CO2 + H2 DH = -41 kJ/mol
• Practical Reaction Conditions – Two stage conversion of CO
– 12% 3% 0.5%
– 350-400°C 180-250°C
– 20-30 bar
In situ removal of carbon dioxide
TCCS9 Trondheim 2017
Stepwise pilot approach
CC BFG
WGS SEP
CO2
- Hot separation - Pre-shift ↓
>10 GJ/tonne CO2
Heat exchange
TCCS9 Trondheim 2017
The Intensification Step
• Combines the Water-Gas-Shift reaction with sorbent material to simultaneously produce H2 at high temperature whilst also capturing CO2
H2
H2O
H2O
CO
H2
CO2
H2O H2O
CO2
Water-Gas Shift: CO + H2O CO2 + H2
Carbonate Formation
Decarbonisation
TCCS9 Trondheim 2017
Process Intensification Intensified
PSA SEWGS
Dry Syngas
>50% H2
99.9%+ H2 purity 99%+ H2 recovery
H2/CO/CO2
(30% H2)
CO2
(99%+ CO2)
Syngas
<65% CO+CO2
H2O
Ads1
Ads2
Ads3
Ads4
Ads1
CO2 capture H2S capture COS conversion CO conversion
H2
TCCS9 Trondheim 2017
Development Timeline
• 2004 – First experimental tests
– proving feasibility of high temperature CO2 capture
• 2005 – First systems analysis – indicating high efficiency compared to base-case systems
• 2006 – High Pressure Single-Column Unit – 2m column taking industrial relevant materials
• 2007 – SEWGS for gasification
– proving feasibility in sour gas applications
• 2008 – Multi-Column Unit – 6x6m column system demonstrations of full cycle
• 2010 – Process Improvements – significant reduction in steam use for regeneration
• 2011 – New sorbent class
– boosting performance by 100%
• 2012 – Techno-economic evaluation – 35% lower that base-case state-of-the-art system IGCC
• 2014 – Further reduction in steam demand
– New cycles for Blast Furnace Gas
• 2015 – Industrial Scale Production of Sorbent
• 2016 – Start construction pilot plant 800m3/hr
Major Innovations
Sorbent Stability
H2S recovery Shift Activity
H2S/CO2
separation “Stress Test” Low steam
demand WGS
TCCS9 Trondheim 2017
Stepwise Pilot Demonstration:
Progress
CC
BFG WGS SEWGS
CO2
Utilities
Blast Furnace
TCCS9 Trondheim 2017
WGS: Impact of BFG conditions
14
1) BFG composition significantly different from conventional WGS operation
Fe2O3 ↔ Fe3O4 ↔ FeO → Fe
At S/CO=2.8 mol/mol
Dry gas (%) CO CO2 H2 N2 R
SRG 12.9 7.5 56.5 22.5 1.6
BFG 20.3 24.5 3.3 51.4 0.3
2) BFG contains 10-30 ppm H2S+COS
fresh active phase over-reduction
side-reactions1)
CO+3H2 → CH4+H2O 2CO → C+CO2
OHCO
HCOR
22
2
<1.62)
1) Twigg, Catalyst Handbook, second edition, 1989 2) Smith et al., Int.J.Chem.Reaction.Eng., 8, 2010, review R4
TCCS9 Trondheim 2017
WGS catalyst lab testing
• Promising performance of FeCr-based catalyst in presence of 15 ppm H2S
15
= lowered steam operation
clean BFG 15ppm H2S BFG
temperature CH4
temperature
CH4
25 bar, pellets, simulated BFG
15
TCCS9 Trondheim 2017
SEWGS sorbent
• Chemical composition tuned and validated – Al–Mg content
• Industrial production of 14 tonnes base material – Utilization of industrial standards and procedures
• Optimization of processing and shaping – On-going activities
16
TCCS9 Trondheim 2017
Main Message in One Sheet
Sorption-Enhanced Water-Gas Shift - SEWGS
• Technology - High carbon capture ratio with unique low steam use
- Able to operate under sour conditions and to remove H2S as well as CO2
- SEWGS technology builds further on the vast industrial experience with PSA systems.
- Combination of several process steps into one (process intensification)
- Highest efficiencies
- For BFG, costs per ton CO2 avoided estimated to be 25% lower than state of the art
- Better understanding of H2O/CO2 interaction leads to new cycle design
• Platform technology for syngas treatment, near future – STEPWISE will extend the SEWGS technology to TRL6 for BFG
TCCS9 Trondheim 2017
7th High Temperature Solid
Looping Cycles Network Meeting
• 4-5th September 2017
• Luleå, Northern Sweden
Pilot Grand Opening
http://www.ieaghg.org/networks/high-temperature
TCCS9 Trondheim 2017
Acknowledgement
This presentation is part of the STEPWISE project that has received funding from the European
Union’s Horizon 2020 research and innovation programme under grant agreement No. 640769
www.stepwise.eu
TCCS9 Trondheim 2017
Thank you for your attention
ECN
Westerduinweg 3 P.O. Box 1
1755 LE Petten 1755 ZG Petten
The Netherlands The Netherlands
T +31 88 515 49 49 [email protected]
F +31 88 515 44 80 www.ecn.nl
Iron & Steel related projects STEPWISE – decarbonised power FReSMe – methanol H2Future – H2-fueled production CURE – Urea from residual steel gases Other opportunities SEWGS for decarbonisation of H2 streams