A novel post-combustion CO2 capture design integrated with an Organic Rankine Cycle (ORC)

Malekli, Mohammadreza; Aslani, Alireza

doi:10.1016/j.psep.2022.10.076

Cited by 15 publications

(4 citation statements)

References 24 publications

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“…Decarbonization that is largely complete of flue gases provides low cost and ease of usage in numerous different flue gas sources with partial CO2 content. Also, The fact that post-combustion CO2 capture produces a solubility difference between CO2 and N2 at lower temperatures and pressures is a significant benefit (Blount et al, 2017;Malekli & Aslani, 2022) . Figure 6 represents the post-combustion carbon capture process.…”

Section: Carbon Capture and Storage Systemsmentioning

confidence: 99%

Evaluation of Decarbonization Methods on Ships

Bayramoğlu

2023

Journal of Marine and Engineering Technology

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Reducing CO2 emissions from ships is regulated by IMO due to global warming. The regulations aim to reduce carbon emissions gradually. This paper highlights the most recent developments for reducing carbon emissions from ships in compliance with the applicable regulations. Basically, three different techniques are used to reduce carbon emissions. These are the use of clean alternative fuels that do not contain carbon atoms such as Hydrogen and Ammonia, the other is the use of ship propulsion systems that can be propelled by electricity, and finally the use of carbon capture systems. As a result of the study, the potentials, advantages and disadvantages of the techniques used are mentioned. As a result of the study, it is seen that carbon capture systems reduce carbon emissions up to 90% levels. It is one of the findings that CO2 emissions can be significantly reduced with appropriate storage practices.

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Section: Carbon Capture and Storage Systemsmentioning

confidence: 99%

Evaluation of Decarbonization Methods on Ships

Bayramoğlu

2023

Journal of Marine and Engineering Technology

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“…In Ref. [ 33 ], a post-combustion CO 2 capture cycle coupled with an ORC unit was developed to attain a high CO 2 capture ratio and low energy utilization. The results showed that the carbon capture rate and the ratio of electricity production to consumption were 97.5% and 49.5%, sequentially.…”

Section: Introductionmentioning

confidence: 99%

Cost and environmental analysis and optimization of a new and green three-level waste heat recovery-based cogeneration cycle: A comparative study

Nikafshan Rad,

Ghasemi,

Marefati

2024

Heliyon

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“…As a result, 190 parties have ratified the Paris Agreement as of January 2021, pledging to develop a low-carbon economy. However, in their pursuit of low-carbon development, nations confront a paradox: energy is a crucial driver of economic development, but fossil energy has a negative impact on the environment and contributes to greenhouse gas emissions [21,22].…”

Section: Introductionmentioning

confidence: 99%

Optimization Study of CO2 Gas Absorption with NaOH Absorbent Continuous System in Raschig Ring Packing Column Using Box–Behnken Design

et al. 2023

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Increasing CO2 gas emissions results in climate change by increasing air temperature and worsening environmental problems. It is necessary to control CO2 gas in the air to overcome this. This research aims to optimize the absorption of CO2 gas in the air with 0.1 M NaOH absorbent in the tower of the Raschig ring stuffing material using the response surface methodology (RSM). This research was conducted using a continuous system of three independent variables by varying the contact time (10–80 min), the flow rate of NaOH absorbent (2–5 L/min), and the flow rate of CO2 gas (1–5 L/min). The response variables in this study were the absorption rate (L/min) and mass transfer coefficient, while the air flow rate was constant at 20 L/min. Air and CO2 gas mix before absorption occurs and flow into the Raschig ring packing column so that contact occurs with the NaOH absorbent. Mass transfer of CO2 gas occurs into the NaOH absorbent, resulting in absorption. The results showed that the effect of contact time (min), the flow rate of NaOH absorbent (L/min), and CO2 gas flow rate individually and the interaction on CO2 absorption rate and mass transfer coefficient were very significant at a p-value of 0.05. Chemical absorption of CO2 also occurred due to the reaction between CO2 and OH- to form CO32− and HCO3−, so the pH decreased, and the reaction was a function of pH. Optimization using Design Expert 13 RSM Box–Behnken Design (BBD) yielded optimal conditions at an absorption time of 80 min, NaOH absorbent flow rate of 5 L/min, CO2 gas flow rate of 5 L/min, absorption rate of CO2 gas of 3.97 L/min, and CO2 gas mass transfer coefficient of 1.443 mol/min m2 atm, with the desirability of 0.999 (≈100%).

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A novel post-combustion CO2 capture design integrated with an Organic Rankine Cycle (ORC)

Cited by 15 publications

References 24 publications

Evaluation of Decarbonization Methods on Ships

Evaluation of Decarbonization Methods on Ships

Cost and environmental analysis and optimization of a new and green three-level waste heat recovery-based cogeneration cycle: A comparative study

Optimization Study of CO2 Gas Absorption with NaOH Absorbent Continuous System in Raschig Ring Packing Column Using Box–Behnken Design

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