2014
DOI: 10.1016/j.ijggc.2014.07.004
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Energetic evaluation of a power plant integrated with a piperazine-based CO 2 capture process

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Cited by 52 publications
(25 citation statements)
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References 18 publications
(26 reference statements)
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“…Van Wagener et al (2014) simulated a carbon capture process with 8 m PZ to estimate the steam, electricity, and cooling water requirements. Kvamsdal et al (2014) studied the integration of a configuration based on high-pressure flash regeneration with the upstream power plant. They found that a power plant integrated with the optimal PZ-based capture plant had a net electric efficiency of 37.4%, which is 7.2% less than the reference power plant without CO 2 capture.…”
Section: Alkanolaminementioning
confidence: 99%
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“…Van Wagener et al (2014) simulated a carbon capture process with 8 m PZ to estimate the steam, electricity, and cooling water requirements. Kvamsdal et al (2014) studied the integration of a configuration based on high-pressure flash regeneration with the upstream power plant. They found that a power plant integrated with the optimal PZ-based capture plant had a net electric efficiency of 37.4%, which is 7.2% less than the reference power plant without CO 2 capture.…”
Section: Alkanolaminementioning
confidence: 99%
“…While in thermodynamic simulations, to assess energy consumption of CO 2 capture processes, a measure of the energy consumption related to CO 2 capture is given by the specific primary energy consumption for CO 2 avoided (SPECCA, GJ/t CO 2 ) (Kvamsdal et al, 2014;Sanchez Fernandez et al, 2014), which is defined as:…”
Section: Energy Estimation For Conventional Processesmentioning
confidence: 99%
“…Goto et al [8] reviewed the impact of integration of the PCC plant for a number of alternative chemical solvents, and revealed that the efficiency penalty can be reduced to 8.0-8.5% points with NH 3 [16,17] and to 8.5% points with amine-blends, such as methyldiethanolamine/piperazine [18]. Moreover, studies by Kvamsdal et al [19] and Van Wagener et al [20] showed that the use of piperazine as a solvent can reduce the efficiency penalty to 7.0-7.2% points. An alternative to chemical solvent absorption is application of novel CO 2 membranes, which has the potential to reduce the efficiency penalty to 6.4-8.5% at a low cost [21].…”
Section: Introductionmentioning
confidence: 99%
“…Lower reboiler heat duty of chemical absorption systems can be achieved by, for example, using an improved process configuration (e.g., absorber intercooling, lean vapor compression, split-stream, etc. [24][25][26]) and/or solvents with better characteristics [18,23,[26][27][28].…”
Section: Discussionmentioning
confidence: 99%