The DMX™ process: An original solution for lowering the cost of post-combustion carbon capture

Raynal, Ludovic; Alix, Pascal; Bouillon, Pierre-Antoine; Gomez, Adrien; Nailly, Marie le Febvre de; Jacquin, Marc; Kittel, Jean; Lella, Angella di; Mougin, Pascal; Trapy, J.

doi:10.1016/j.egypro.2011.01.119

Cited by 166 publications

(74 citation statements)

References 14 publications

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“…In a new project (started in Oct. 2016), ROLIN-CAP (CORDIS 2016), a consortium of 12 partners funded by EU seeks to develop specialized RPBs for biphasic solvents. Biphasic solvents have shown low regeneration energy requirement of about 2.4 GJ/ton of CO 2 compared to about 4 GJ/ton of CO 2 for MEA (Raynal et al 2011). RPBs on the other hand have also shown good potential in replacing conventional packed beds.…”

Section: Combination Of New Solvents and Processmentioning

confidence: 99%

“…• Biphasic solvents: These solvents under regulated conditions undergoes liquid-liquid phase separation to give a CO 2 lean and rich phases respectively (Raynal et al 2011). Analysis of DMX TM process which uses biphasic solvents shows about 50% less regeneration energy and lower reboiler temperature compared to the MEA process.…”

Section: New Solventsmentioning

confidence: 99%

“…These drawbacks of MEA has been addressed through development of new solvents which include mixed amine solvents such as mixtures of MEA and MDEA, AMP and PZ among others (Dubois and Thomas 2012), ammoniabased solvents (Darde et al 2010), amino acid solvent (Brouwer et al 2005), biphasic solvents (Raynal et al 2011) and ionic liquid-based solvents (Boot-Handford et al 2014;Zacchello et al 2016). The new solvents have shown great potential.…”

Section: Solventsmentioning

confidence: 99%

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Current status and future development of solvent-based carbon capture

Oko

Wang

Joel

2017

Int J Coal Sci Technol

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Solvent-based carbon capture is the most commercially-ready technology for economically and sustainably reaching carbon emission reduction targets in the power sector. Globally, the technology has been deployed to deal with flue gases from large scale power plants and different carbon-intensive industries. The success of the technology is due to significant R&D activities on the process development and decades of industrial experience on acid gas removal processes from gaseous mixtures. In this paper, current status of PCC based on chemical absorption-commercial deployment and demonstration projects, analysis of different solvents and process configurations-is reviewed. Although some successes have been recorded in developing this technology, its commercialization has been generally slow as evidenced in the cancellation of high profile projects across the world. This is partly due to the huge cost burden of the technology and unpredictable government policies. Different research directions, namely new process development involving process intensification, new solvent development and a combination of both, are discussed in this paper as possible pathways for reducing the huge cost of the technology.

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Section: Combination Of New Solvents and Processmentioning

confidence: 99%

Section: New Solventsmentioning

confidence: 99%

Section: Solventsmentioning

confidence: 99%

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Current status and future development of solvent-based carbon capture

Oko

Wang

Joel

2017

Int J Coal Sci Technol

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“…It has been described with further details in [11,12] and only a quick description is given hereafter. The main objective being to present the techno-economic comparison with the MEA process.…”

Section: Dmx Tm Process Descriptionmentioning

confidence: 99%

ACACIA Project – Development of a Post-Combustion CO₂Capture Process. Case of the DMX^TMProcess

Gomez

Briot

Raynal

et al. 2014

Oil Gas Sci. Technol. – Rev. IFP Energies nouvelles

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“…The DMX process by IFPEN is based on special solvents forming two immiscible phases and is now under testing in Italy (Raynal, et al, 2011). This process is claimed to give a specific reboiler duty as low as 2.1 GJ/tonne CO 2 captured which is significantly lower than the 3.0-3.7 GJ/t CO 2 reported for the modified and classical 30wt% MEA reference processes.…”

Section: Introductionmentioning

confidence: 99%

Binary and ternary VLE of the 2-(diethylamino)-ethanol (DEEA)/3-(methylamino)-propylamine (MAPA)/water system

Hartono

Saleem

Arshad

et al. 2013

Chemical Engineering Science

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The DMX™ process: An original solution for lowering the cost of post-combustion carbon capture

Cited by 166 publications

References 14 publications

Current status and future development of solvent-based carbon capture

Current status and future development of solvent-based carbon capture

ACACIA Project – Development of a Post-Combustion CO₂Capture Process. Case of the DMX^TMProcess

Binary and ternary VLE of the 2-(diethylamino)-ethanol (DEEA)/3-(methylamino)-propylamine (MAPA)/water system

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The DMX™ process: An original solution for lowering the cost of post-combustion carbon capture

Cited by 166 publications

References 14 publications

Current status and future development of solvent-based carbon capture

Current status and future development of solvent-based carbon capture

ACACIA Project – Development of a Post-Combustion CO2Capture Process. Case of the DMXTMProcess

Binary and ternary VLE of the 2-(diethylamino)-ethanol (DEEA)/3-(methylamino)-propylamine (MAPA)/water system

Contact Info

Product

Resources

About

ACACIA Project – Development of a Post-Combustion CO₂Capture Process. Case of the DMX^TMProcess