2022
DOI: 10.1016/j.jece.2022.108104
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CO2 capture process through hybrid gas hydrate-membrane technology: Complex approach for the transition from theory to practice

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Cited by 10 publications
(7 citation statements)
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“…In turn, cold energy from liquefied natural gas reduces the cost of maintaining the required temperature for the hydrate formation process. These options undoubtedly increase the hydrate formation’s energy efficiency and make it competitive with well-developed techniques [ 11 , 12 , 13 , 14 ]. However, such solutions can decrease the hydrate gas capacity, need promoter regeneration/water remediation, and significantly complicate the apparatus for continuously producing hydrates, especially at high pressures.…”
Section: Introductionmentioning
confidence: 99%
“…In turn, cold energy from liquefied natural gas reduces the cost of maintaining the required temperature for the hydrate formation process. These options undoubtedly increase the hydrate formation’s energy efficiency and make it competitive with well-developed techniques [ 11 , 12 , 13 , 14 ]. However, such solutions can decrease the hydrate gas capacity, need promoter regeneration/water remediation, and significantly complicate the apparatus for continuously producing hydrates, especially at high pressures.…”
Section: Introductionmentioning
confidence: 99%
“…SCHs are attractive as gas separation media because of their high selectivity and stability. Selectivities of SCHs for CO 2 /N 2 gas mixtures range from 3 to 40, depending on conditions of temperature, pressure, type of promoter, and their concentration . In the simulation of CO 2 recovery from flue gas (CO 2 /N 2 ) by SCH slurries, setting a two-stage process with CO 2 /N 2 selectivities of 30 and 40 resulted in a CO 2 recovery cost of $35/ton-CO 2 , which was below the goal of the U.S. Department of Energy ($40/ton-CO 2 in 2025) . However, in the simulation of systems that use the theoretical maximum absorption (H 2 O/CO 2 = 38:3) with TBAB for CO 2 capture, a significant amount of energy is required to cool the slurry, which is related to the amount of heat that forms during SCH formation and SCH dissociation.…”
Section: Introductionmentioning
confidence: 99%
“…The same amount of heat in the reaction is produced with opposite signs, so integrating the heat requirements for the process can improve energy efficiency . In the process simulations, operating pressures have ranged from 1.6 to 3.1 MPa. Gas separation simulations have shown that the compression process consumes the most energy among configurations at high-pressure (>2 MPa) conditions . Lowering the operating pressure can be expected to reduce the energy consumption in SCH-based CO 2 capture systems.…”
Section: Introductionmentioning
confidence: 99%
“…The most critical one is that the process has a high energy consumption requirement that is equal up to the 30% of power plant’s produced energy, resulting in a CO 2 capture cost of 40–100 $/ton and rise in electricity price of 50–90% [ 8 , 9 ]. This forced the world’s chemical engineering society to design new energy efficient processes that agree with the modern green chemistry principles [ 10 , 11 , 12 , 13 , 14 ].…”
Section: Introductionmentioning
confidence: 99%