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1 
October 01, 2014 
Marco Linders 
Solvent development for biogas 
TNO Customers 
TNO is a technology development and consulting company 
with over 30 years of experience in (Renewable) Gas 
technology 
TNO Facts 
! Independent Research Organization 
! Technology development, consulting, and contract R&D 
! Approximately 3800 employees 
! 600 million Euro Revenue, 1/3 government funding 
Markets 
! Energy, Defence & Safety, Industry, Healthy Living, Living 
Environment
2 
October 01, 2014 
Marco Linders 
Solvent development for biogas 
Gas Treatment: Our Focus Areas 
Processes 
for 
purifica1on, 
separa1on 
& 
treatment 
of: 
Flue 
Gas 
Natural 
Gas 
/ 
Syngas 
/ 
Biogas 
U1liza1on
3 
October 01, 2014 
Marco Linders 
Solvent development for biogas 
Algae for CO2 capture & utilization 
Technology 
Innova1ons 
CO2-­‐lean 
solvent 
CO2-­‐rich 
solvent 
Smart CO2 Feeding 
Combining CO2 capture with algae cultivation to: 
! Decrease in energy requirement for solvent regeneration 
! Increase in algae growth rates & CO2 feeding efficiency 
! Create potential revenue from bio-products
4 
October 01, 2014 
H2S removal technology 
Technology Innovations 
Marco Linders 
Solvent development for biogas 
Principle of technology: 
2 Fe(III)NTA + H2S à 2 Fe(II)NTA + S0 + 2 H+ 
2 Fe(II)NTA + ½ O2 + 2 H+ à 2 Fe(III)NTA + H2O 
• High removal efficiency up to 99,9% 
• Sulphur removal of 0,1 to 20 t/d 
• H2S is directly converted to 
elemental sulphur 
• No Claus-SRU required 
• Low CAPEX/OPEX
5 
October 01, 2014 
Marco Linders 
Solvent development for biogas 
Process Development 
TNO Approach 
Molecular 
modelling 
Synthesis 
Proof 
of 
Principle 
-­‐ 
VLE 
& 
batch 
tes1ng 
Proof 
of 
Concept 
-­‐ 
Mini 
pilot 
Pilot 
plant 
design 
& 
scale 
up 
Pilot 
plant 
(Lab 
scale)
6 
October 01, 2014 
Marco Linders 
Solvent development for biogas 
Carbon Clean Solutions MethPure Solvent development 
for biogas scrubbers – approach 
! Goal: outperform current used state-of-the-art solvents (e.g. aMDEA) 
with respect to general performance, stability, operating costs 
! Benchmark: amine, pressure swing adsorption and water scrubbers for 
CO2 removal 
! Approach: 
Miniplant 
tes1ng 
Demonstra1on 
Solvent 
Mixture 
op1misa1on 
Solvent 
component 
iden1fica1on 
Equilibrium 
Thermal stability 
Physical characteristics 
(Kinetics) 
Stripper pressure 
Stripper temperature 
Solvent loading 
European Partner; 
Capacity 6000 m3/day 
Benchmark against 
aMDEA
Equilibrium testing 
7 
October 01, 2014 
Marco Linders 
Solvent development for biogas 
Equilibrium 19% thermal 
energy savings compared to 
benchmark aMDEA 
! Mixtures significantly better than MDEA at required partial pressure 
! Mixture 2 selected because it has higher thermal stability (see next)
Thermal stability testing 
8 
October 01, 2014 
Marco Linders 
Solvent development for biogas 
! CO2 loaded samples stored at 160°C for 3 weeks (accelerated aging)
Physical characteristics 
9 
October 01, 2014 
Marco Linders 
Solvent development for biogas 
! At high CO2 loadings, viscosity can be an issue
Miniplant testing 
10 
October 01, 2014 
Marco Linders 
Solvent development for biogas 
! Solvent performance testing in a continuous absorption-desorption 
miniplant 
! Solvent handling and practical issues such as foaming
Miniplant testing 
11 
October 01, 2014 
Marco Linders 
Solvent development for biogas 
Characteristics: 
! Mobile and fully automated 
! Capacity of 4 m3/h of flue gas 
! Absorber section: packed bed (Sulzer Mellapak 2X), totally 3.5 m 
high with 4 packed beds each of 0.5 m 
! Diameter of 4.5 cm 
! Stripper section same dimension/packing as absorber 
! Total liquid inventory of the system is about 20 L 
! Measurement of process parameters such as temperatures, flows, 
liquid level, pH lean and rich, CO2 concentration
Miniplant testing 
12 
October 01, 2014 
Marco Linders 
Solvent development for biogas 
! Parametric testing for two weeks to find optimum performance 
Parameter Range CO2 Capture 
rate (%) 
Stripper pressure 
change 0.9-1.0 bar at 120 °C 90-94 
Lower stripper 
temperature 
110-115°C 
81-95 
Higher stripper 
temperature 
130°C at 1.7 bar 
93 
Maximum rich loading Recirculation of solvent 
and no stripping - 
! Based on results solvent considered suitable for demonstration scale 
! Performed much better than the benchmark aMDEA
13 
October 01, 2014 
Marco Linders 
Solvent development for biogas 
Commercial Demonstration – European Biogas Partner 
! Source of biogas: Agricultural waste 
! Capacity: 6000 m3/day / Ongoing operation since July, 2014 
! Commercial validation of ‘MethPure’ solvent successfully with match 
customer requirement 
! Detailed solvent characterization obtained: results are as expected, 
leading to a database useable for further scaling up
Conclusion 
14 
October 01, 2014 
Marco Linders 
Solvent development for biogas 
! Solvent has higher capacity compared to benchmark aMDEA 
! Solvent has better thermal stability compared to benchmark aMDEA 
! Important aspects as well are viscosity, kinetics and energy efficiency 
! Miniplant tests showed good continuous performance, gave insight in 
optimal process conditions, and showed stable operation 
! Commercial validation proven successful and on-going 
! Multi-dimensional approach by means of expertise in solvent and process 
development and lab scale to pilot plant testing and detailed 
benchmarking against aMDEA
15 
October 01, 2014 
Marco Linders 
Solvent development for biogas 
Thank you for your time and attention 
Questions? 
! Marco Linders 
! marco.linders@tno.nl 
! Phone +31 88 866 1324 
! Mobile +31 6 225 450 18 
! Prateek Bumb 
! prateek@carboncleansolutions.com 
! Mobile +44 774743 4099/+91-9167555141 
http://www.hak.nl/index.php?nav=actueel&subnav=nieuwsarchief&id=62
Back-up slides 
16 
October 01, 2014 
Marco Linders 
Solvent development for biogas
3.5 
3 
2.5 
2 
1.5 
1 
0.5 
0 
17 
Mixture 1 Mixture 2 Mixture 3 Mixture 4 
Mixture 1 @ 24.53 kPa 
Mixture 2 @ 27.5 kPa 
Mixture 3 @ 25.07 kPa 
Mixture 4 @ 17.18 kPa 
Rate of reaction X 105 (kmol/m2 s) 
Kinetics Testing 
Corrosion – SS316L 
Rate of corrosion (*mpy) 0.035 
(Extraordinary) 
* mpy = mils per year 
October 01, 2014 
Marco Linders 
Solvent development for biogas

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TNO's Solvent Development for Biogas CO2 Capture

  • 1. 1 October 01, 2014 Marco Linders Solvent development for biogas TNO Customers TNO is a technology development and consulting company with over 30 years of experience in (Renewable) Gas technology TNO Facts ! Independent Research Organization ! Technology development, consulting, and contract R&D ! Approximately 3800 employees ! 600 million Euro Revenue, 1/3 government funding Markets ! Energy, Defence & Safety, Industry, Healthy Living, Living Environment
  • 2. 2 October 01, 2014 Marco Linders Solvent development for biogas Gas Treatment: Our Focus Areas Processes for purifica1on, separa1on & treatment of: Flue Gas Natural Gas / Syngas / Biogas U1liza1on
  • 3. 3 October 01, 2014 Marco Linders Solvent development for biogas Algae for CO2 capture & utilization Technology Innova1ons CO2-­‐lean solvent CO2-­‐rich solvent Smart CO2 Feeding Combining CO2 capture with algae cultivation to: ! Decrease in energy requirement for solvent regeneration ! Increase in algae growth rates & CO2 feeding efficiency ! Create potential revenue from bio-products
  • 4. 4 October 01, 2014 H2S removal technology Technology Innovations Marco Linders Solvent development for biogas Principle of technology: 2 Fe(III)NTA + H2S à 2 Fe(II)NTA + S0 + 2 H+ 2 Fe(II)NTA + ½ O2 + 2 H+ à 2 Fe(III)NTA + H2O • High removal efficiency up to 99,9% • Sulphur removal of 0,1 to 20 t/d • H2S is directly converted to elemental sulphur • No Claus-SRU required • Low CAPEX/OPEX
  • 5. 5 October 01, 2014 Marco Linders Solvent development for biogas Process Development TNO Approach Molecular modelling Synthesis Proof of Principle -­‐ VLE & batch tes1ng Proof of Concept -­‐ Mini pilot Pilot plant design & scale up Pilot plant (Lab scale)
  • 6. 6 October 01, 2014 Marco Linders Solvent development for biogas Carbon Clean Solutions MethPure Solvent development for biogas scrubbers – approach ! Goal: outperform current used state-of-the-art solvents (e.g. aMDEA) with respect to general performance, stability, operating costs ! Benchmark: amine, pressure swing adsorption and water scrubbers for CO2 removal ! Approach: Miniplant tes1ng Demonstra1on Solvent Mixture op1misa1on Solvent component iden1fica1on Equilibrium Thermal stability Physical characteristics (Kinetics) Stripper pressure Stripper temperature Solvent loading European Partner; Capacity 6000 m3/day Benchmark against aMDEA
  • 7. Equilibrium testing 7 October 01, 2014 Marco Linders Solvent development for biogas Equilibrium 19% thermal energy savings compared to benchmark aMDEA ! Mixtures significantly better than MDEA at required partial pressure ! Mixture 2 selected because it has higher thermal stability (see next)
  • 8. Thermal stability testing 8 October 01, 2014 Marco Linders Solvent development for biogas ! CO2 loaded samples stored at 160°C for 3 weeks (accelerated aging)
  • 9. Physical characteristics 9 October 01, 2014 Marco Linders Solvent development for biogas ! At high CO2 loadings, viscosity can be an issue
  • 10. Miniplant testing 10 October 01, 2014 Marco Linders Solvent development for biogas ! Solvent performance testing in a continuous absorption-desorption miniplant ! Solvent handling and practical issues such as foaming
  • 11. Miniplant testing 11 October 01, 2014 Marco Linders Solvent development for biogas Characteristics: ! Mobile and fully automated ! Capacity of 4 m3/h of flue gas ! Absorber section: packed bed (Sulzer Mellapak 2X), totally 3.5 m high with 4 packed beds each of 0.5 m ! Diameter of 4.5 cm ! Stripper section same dimension/packing as absorber ! Total liquid inventory of the system is about 20 L ! Measurement of process parameters such as temperatures, flows, liquid level, pH lean and rich, CO2 concentration
  • 12. Miniplant testing 12 October 01, 2014 Marco Linders Solvent development for biogas ! Parametric testing for two weeks to find optimum performance Parameter Range CO2 Capture rate (%) Stripper pressure change 0.9-1.0 bar at 120 °C 90-94 Lower stripper temperature 110-115°C 81-95 Higher stripper temperature 130°C at 1.7 bar 93 Maximum rich loading Recirculation of solvent and no stripping - ! Based on results solvent considered suitable for demonstration scale ! Performed much better than the benchmark aMDEA
  • 13. 13 October 01, 2014 Marco Linders Solvent development for biogas Commercial Demonstration – European Biogas Partner ! Source of biogas: Agricultural waste ! Capacity: 6000 m3/day / Ongoing operation since July, 2014 ! Commercial validation of ‘MethPure’ solvent successfully with match customer requirement ! Detailed solvent characterization obtained: results are as expected, leading to a database useable for further scaling up
  • 14. Conclusion 14 October 01, 2014 Marco Linders Solvent development for biogas ! Solvent has higher capacity compared to benchmark aMDEA ! Solvent has better thermal stability compared to benchmark aMDEA ! Important aspects as well are viscosity, kinetics and energy efficiency ! Miniplant tests showed good continuous performance, gave insight in optimal process conditions, and showed stable operation ! Commercial validation proven successful and on-going ! Multi-dimensional approach by means of expertise in solvent and process development and lab scale to pilot plant testing and detailed benchmarking against aMDEA
  • 15. 15 October 01, 2014 Marco Linders Solvent development for biogas Thank you for your time and attention Questions? ! Marco Linders ! marco.linders@tno.nl ! Phone +31 88 866 1324 ! Mobile +31 6 225 450 18 ! Prateek Bumb ! prateek@carboncleansolutions.com ! Mobile +44 774743 4099/+91-9167555141 http://www.hak.nl/index.php?nav=actueel&subnav=nieuwsarchief&id=62
  • 16. Back-up slides 16 October 01, 2014 Marco Linders Solvent development for biogas
  • 17. 3.5 3 2.5 2 1.5 1 0.5 0 17 Mixture 1 Mixture 2 Mixture 3 Mixture 4 Mixture 1 @ 24.53 kPa Mixture 2 @ 27.5 kPa Mixture 3 @ 25.07 kPa Mixture 4 @ 17.18 kPa Rate of reaction X 105 (kmol/m2 s) Kinetics Testing Corrosion – SS316L Rate of corrosion (*mpy) 0.035 (Extraordinary) * mpy = mils per year October 01, 2014 Marco Linders Solvent development for biogas