scientific session: renewable energy sources

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www.fcirce.es Scientific Session: Renewable Energy Sources T OWARDS NON-CARBON ENERGY PRODUCTION: TECHNICAL AND ENVIRONMENTAL ASSESSMENT OF ENHANCED STRATEGIES IN CO 2 PURIFICATION FOR GEOTHERMAL POWER PLANTS Andrea Hernández Pedrero, Maryori C. Díaz Ramírez, Víctor J. Ferreira, Ana M. López Sabirón, Ana Martínez Santamaría Follow us: 10/10/2019, Athens ANDREA HERNÁNDEZ PEDRERO Researcher Email: [email protected]

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Page 1: Scientific Session: Renewable Energy Sources

www.fcirce.es Síguenos en:

Scientific Session: Renewable Energy Sources

TOWARDS NON-CARBON ENERGY

PRODUCTION: TECHNICAL AND ENVIRONMENTAL

ASSESSMENT OF ENHANCED STRATEGIES IN

CO2 PURIFICATION FOR GEOTHERMAL

POWER PLANTS

Andrea Hernández Pedrero, Maryori C. Díaz Ramírez, Víctor J. Ferreira, Ana M. López Sabirón, Ana Martínez Santamaría

Follow us:

10/10/2019, Athens

ANDREA HERNÁNDEZ PEDRERO

ResearcherEmail: [email protected]

Page 2: Scientific Session: Renewable Energy Sources

Towards non-carbon energy production:

CONTENTS

1. Context overview

1.1. Geothermal energy

1.2. Carbon capture, utilization and storage (CCUS)

2. Scope and objectives

3. Methodology

3.1. Dehydration technology selection

3.2. Second purification stage simulation

4. Results

4.1. Parametric analysis and optimization

4.2. Standard and enhanced process comparison

5. Conclusions

Technical and environmental assessment of enhanced strategies in CO2 purification for geothermal power plantsANDREA HERNÁNDEZ PEDRERO, MARYORI C. DÍAZ RAMÍREZ, VÍCTOR J. FERREIRA, ANA M. LÓPEZ SABIRÓN, ANA MARTÍNEZ SANTAMARÍA

Page 3: Scientific Session: Renewable Energy Sources

1. CONTEXT OVERVIEW

1.1. GEOTHERMAL ENERGY

Figure 1.Scheme of a geothermal power plant(extracted from powearthful.com)

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Figure 2. Installed geothermal power capacity in 2018 by country(adapted from statista.com)

• Geothermal energy is present in underground reservoirs of hot water, steam, brines, etc.

• Steam and hot water can be tapped to generate electricity or to heat and cool buildings directly

• Advantages:

• Renewable energy

• Always available (unaffected by weather, day/night or seasonal variations)

• Potential to mitigate climate change (no combustion process emitting CO2)

• Disadvantages:

• Low geothermal gas emissions (H2S, CO2, CH4, etc.)

• Local induced seismic events

Page 4: Scientific Session: Renewable Energy Sources

1.2. CARBON CAPTURE, UTILIZATION AND

STORAGE (CCUS)

• CCUS technologies will play a very important role in meeting energy and climate goals

• Policy support is critical

(Image extracted from sfc.ac.uk)

Figure 4. Additional CO2 emissions reductions in the Sustainable Development Scenario (SDS) vs. New Policies scenario (NPS)

(extracted from iea.org)

Figure 3. CO2 capture rate by country (adapted from iea.org)

United States10 projectsCO2 capture: 24.85 Mtpa

Canada2 projectsCO2 capture: 2 Mtpa

Brazil1 projectCO2 capture: 1 Mtpa

Norway2 projectsCO2 capture: 1.7 Mtpa

Saudi Arabia1 projectCO2 capture: 0.8 Mtpa

China1 projectCO2 capture: 0.6 Mtpa

Australia1 projectCO2 capture: 4 Mtpa

Page 5: Scientific Session: Renewable Energy Sources

• Scope: application of a two-stage CO2 purification technology in geothermal power plants to reduce the associated environmental impacts

• First stage: amine-based selective H2S absorption

• Second stage: dehydration and CO2 capture by cryogenic separation from the non-condensable gases (NCG)

• Focus: second purification stage

• Objectives:

• Analyse, select and design the best dehydration technology to remove water from the sweet gas and allow for the cryogenic separation of CO2 from the NCG

• Convert waste gaseous streams into value-added products (high purity CO2)

1.2. CARBON CAPTURE, UTILIZATION AND

STORAGE (CCUS)

• CCUS technologies will play a very important role in meeting energy and climate goals

• Policy support is critical

(Image extracted from sfc.ac.uk)

2. SCOPE AND OBJECTIVES

Page 6: Scientific Session: Renewable Energy Sources

Figure 5. Dehydration technology selection chart(extracted from J. Olijhoek and B. Leeuw,

CAPEX and OPEX Considerations for Gas Dehydration Technologies, 2015)

3. METHODOLOGY

3.1. DEHYDRATION TECHNOLOGY SELECTION

• Dehydration is a well-stablished process in the natural gas industry

• Different dehydration technologies: absorption, adsorption, membranes, etc.

• Main decision factor: required dehydration level

• Cryogenic separation: high purity CO2 at -55°C

(-67°F) at 60 bar

• Hydrate formation temperature ca. -65°C (-85°F)

• Advanced glycol dehydration

• Lower costs associated

• Simple operation and maintenance

• Equipment easily automated

• Triethylene glycol (TEG) is the solvent most commonly used. Advantages:

• More easily regenerated

• Lower vapor losses

• Lower operating costs

-85°F

Page 7: Scientific Session: Renewable Energy Sources

• Cryogenic CO2 separation: compression and refrigeration of the gas stream to conditions at which CO2 can condense

• Aspen HYSYS – CPA property package: suitable for vapor/liquid equilibria of mixtures with hydrocarbons/non-hydrocarbons/polar compounds

3.2. SECOND PURIFICATION STAGE SIMULATION

• Advanced glycol dehydration:

• Main influencing factor on dehydration level: glycol concentration

• Modification to standard dehydration: injection of dry gas in the reboiler to enhance glycol regeneration, and thus increase its concentration

Standard glycol dehydration

CO2 cryogenic separation

Page 8: Scientific Session: Renewable Energy Sources

4. RESULTS

4.1. PARAMETRIC ANALYSIS AND OPTIMIZATION

• The second purification stage is optimized following an iterative parametric analysis in order to:

• Achieve hydrate formation temperatures of -65°C

• Minimize energy consumption

• Minimize solvent loss

• Optimized parameters

BOILING POINTS:100°C for water

vs.288°C for TEG

Page 9: Scientific Session: Renewable Energy Sources

• The second purification stage is also simulated based on an standard dehydration

• The environmental impact associated to the second purification stage is analysed• LCA approach• Functional unit: 1 kg of absorbed water• Environmental impact method: CML IA• Results based on the relative variation with respect to

the standard dehydration

4.2. STANDARD AND ENHANCED PROCESS COMPARISON

Geothermal heat

H2S content in sour gas ≈10-1 ppm

Page 10: Scientific Session: Renewable Energy Sources

5. CONCLUSIONS

Geothermal power plants have some gas emissions associated

Policy support for CCUS technologies is essential to achieve the ambitions of the Paris Agreement

We propose a two-stage purification technology to convert waste gaseous emissions from geothermal power plants into value-added products

The first stage consists on an amine-based absorption and reduces H2S content in the gas mixture to 0.98 ppmw

The second stage involves a dehydration process and a cryogenic separation. As a result, a CO2 stream with 99.0 % purity is produced

An enhanced glycol dehydration is required to achieve a hydrate formation temperature of -64.9°C.

The enhanced glycol dehydration reduces by 70% the impact on climate change (total CO2 eq.) with regard to the standard dehydration

Page 11: Scientific Session: Renewable Energy Sources

Tel. : [+34] 976 976 859· [email protected]

www.fcirce.es

ACKNOWLEDGEMENTS

Page 12: Scientific Session: Renewable Energy Sources

Tel. : [+34] 976 976 859· [email protected]

www.fcirce.es

Thank you for your attention

Page 13: Scientific Session: Renewable Energy Sources

Tel. : [+34] 976 976 859· [email protected]

www.fcirce.es

Thank you for your attention

ANY QUESTIONS?