Simulation and analysis of CO2 capture process with aqueous monoethanolamine solution

Liu, Baohong; Zhang, Nan; Smith, Robin

doi:10.1016/j.apenergy.2015.07.010

Cited by 87 publications

(30 citation statements)

References 16 publications

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“…The stream cycle is integrated finally, and the CO 2 capture rate is 90.01%. 25 In this paper, the annual amount of CO 2 capture is about 70 000 tons, and the reboiler heat load is 8.19 MW. Table 5 contains the simulation results of main streams.…”

Section: Simulation Results and Validationsmentioning

confidence: 99%

“…These trends are well agreed with the work of Li. 25 In this paper, the annual amount of CO 2 capture is about 70 000 tons, and the reboiler heat load is 8.19 MW. The CO 2 loading is about 0.26 mol CO 2 /mol MEA, and the regeneration energy consumption is 3.67 MJ/kgCO 2 .…”

Section: Simulation Results and Validationsmentioning

confidence: 99%

“…It is used to calculate the physical properties of the gas phase by the RK equation, and the physical properties of the liquid phase are calculated by the NRTL activity coefficient model. [24][25][26] At the same time, the presence of fly ash can also lead to the degradation of MEA. Rate-based simulation models are known to be superior to equilibrium-state models for MEA modeling.…”

Section: Model Setupmentioning

confidence: 99%

“…Furthermore, many studies have shown that the existence of SO 2 can lead to the degradation of MEA. [24][25][26] At the same time, the presence of fly ash can also lead to the degradation of MEA. 27 Therefore, the exhaust gas should be purified by desulfurization, denitrification, and dust treatment before flowing into the carbon capture system, especially in power plants.…”

Section: Model Setupmentioning

confidence: 99%

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CO₂ capture from reheating furnace based on the sensible heat of continuous casting slabs

et al. 2018

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Summary Carbon capture and storage adopted by power plants has been extensively studied in recent years. However, little attention has been paid to carbon capture and storage for steel plants. After considering the differences between steel and power plants, a carbon capture system of reheating furnace flue gas is designed, based on the sensible heat of continuous casting slabs. As a result, a significant amount of waste heat resource from rolling mills can be effectively reused. By using Aspen Plus to optimize parameters of the capture system, such as regeneration pressure and reflux ratio, the regeneration energy consumption is obtained and the result is verified by comparing the data with that of other research. Under the constraint condition of 90% CO2 capture rate, simulation results show that the purity of CO2 obtained is 98.4%, and the annual CO2 capture capacity is about 70 000 tons. Finally, main parameters of continuous casting slabs and the heat recovery boiler are calculated. The heat load of the steam supplied for the reboiler is 8.5 MW, indicating that this steam generation method matches the carbon capture system.

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Section: Simulation Results and Validationsmentioning

confidence: 99%

Section: Simulation Results and Validationsmentioning

confidence: 99%

Section: Model Setupmentioning

confidence: 99%

Section: Model Setupmentioning

confidence: 99%

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CO₂ capture from reheating furnace based on the sensible heat of continuous casting slabs

et al. 2018

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“…Therefore, the addition of a small amount of alkanolamine enhances CO2 absorption rates. When designing new acid gas removal equipment, physical properties' data such as density, viscosity, solubility and kinetic data are essential [17,18].…”

Section: R R Nh Coo R R Nh R R Ncoo Carbamate R R Nhmentioning

confidence: 99%

Aspen HYSYS Simulation of CO2 Capture for the Best Amine Solvent

Qamar

Mushtaq

Ullah

et al. 2020

ARFMTS

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The developing issue of the present world is a worldwide temperature alteration, which is caused by ozone-harming substance impact. Carbon dioxide has the real commitment towards a worldwide temperature alteration as it is discovered copiously in climate given anthropogenic carbon dioxide outflows and advancement of vent gasses. Businesses are additionally debilitating corrosive gasses (CO2 and H2S) in the earth, which prompts the perilous conditions. To control such conditions lessening of these hurtful gasses is valuable for which ingestion of corrosive gasses is for the most part favoured. Amine gas treating is an appropriate system to complete this work as it expels CO2 and H2S at the same time from petroleum gas streams and also modern gas streams and decontaminate them for local use and solid condition individually. For this purpose, study the best solvent selection for CO2 capture in chemical absorption. In chemical absorption amines solvents are used. Amine is one of the applicant solvents which is utilized for carbon dioxide recuperation from the pipe gas by chemical absorption /desorption process. This research focus on the effect of various amine absorbents, their concentrations, the absorber and stripper section statures and the working conditions on the carbon dioxide recuperation plant for post-combustion carbon dioxide evacuation. For every amine dissolvable, the ideal stages for the absorber and stripper segments, and the ideal absorbent concentration, the ones that give the base conditions for carbon dioxide evacuation is determined by Aspen HYSYS simulation. The results obtained showed that carbon dioxide recuperation with 50 wt. % DGA requires the best ideal conditions for removal of CO2 with the following design and working conditions are 10-organize absorber column and 10-arrange stripper segment, 20.89 m 3 /hr circulation rate of solvent and 2545 kW of reboiler obligation and 100 o C as the regenerator-delta temperature and absorbed 93.6% CO2.

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Optimization of novel nonaqueous hexanol‐based monoethanolamine/methyl diethanolamine solvent forCO₂absorption

Cihan

Ali

Khalifa

et al. 2022

Intl J of Energy Research

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Chemical absorption of CO 2 into aqueous amine-based solvents is known as the most mature technology featuring high separation efficiencies and applicability of retrofitting. The high regeneration energy requirement of the process is a major drawback, and improvements in solvent design are required. This study investigated the CO 2 absorption and desorption performance of the nonaqueous monoethanolamine (MEA)/methyl diethanolamine (MDEA) blend experimentally using a stirred cell reactor. CO 2 loading, cyclic capacity loss, and initial absorption rate were measured for different solvent formulations and compared to single amines (MEA or MDEA). A mixture-process design and response surface methodology were employed to model and optimize the solvent formulation at different temperatures and pressures. The single-response optimization yielded 0:83 mol CO 2 =mol amine (at 0% MEA and 303 K/0.5 barg) and 3.17e-5 kmol/m 2 Ás (at 40% MEA and 310.67 K/0.5 barg) as optimal absorption capacity and rate of absorption, respectively. The multiresponse optimization was conducted using the composite desirability function yielding 0:653 mol CO 2 =mol amine and 2.987e-5 kmol/m 2 Ás (D = 0.903). The multiresponse optimization was also extended to include the impact of different initial settings and importance ratios between the absorption capacity and rate of absorption, in which the latter needed at least 1.6 higher importance level to influence the multiresponse optimization.

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Simulation and analysis of CO2 capture process with aqueous monoethanolamine solution

Cited by 87 publications

References 16 publications

CO₂ capture from reheating furnace based on the sensible heat of continuous casting slabs

CO₂ capture from reheating furnace based on the sensible heat of continuous casting slabs

Aspen HYSYS Simulation of CO2 Capture for the Best Amine Solvent

Optimization of novel nonaqueous hexanol‐based monoethanolamine/methyl diethanolamine solvent forCO₂absorption

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Simulation and analysis of CO2 capture process with aqueous monoethanolamine solution

Cited by 87 publications

References 16 publications

CO2 capture from reheating furnace based on the sensible heat of continuous casting slabs

CO2 capture from reheating furnace based on the sensible heat of continuous casting slabs

Aspen HYSYS Simulation of CO2 Capture for the Best Amine Solvent

Optimization of novel nonaqueous hexanol‐based monoethanolamine/methyl diethanolamine solvent forCO2absorption

Contact Info

Product

Resources

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CO₂ capture from reheating furnace based on the sensible heat of continuous casting slabs

CO₂ capture from reheating furnace based on the sensible heat of continuous casting slabs

Optimization of novel nonaqueous hexanol‐based monoethanolamine/methyl diethanolamine solvent forCO₂absorption