Numerical and Experimental Study of an Alpha-Type Stirling Water Dispenser

Easa, Ammar S.; Khalaf-Allah, Reda A.; Tolan, Mohamed; Mohamed, Sherif

doi:10.1007/s13369-021-06289-w

Cited by 9 publications

(1 citation statement)

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“…Utilizing selective codes, the developed models of a new gas cycle predict key thermodynamic cycle parameters such as power output, efficiency, combustion composition, and exhaust temperature. Numerous researchers have extensively studied CO2 absorption by amines; nevertheless, the majority of research has concentrated on the chemical reaction mechanism, mass transfer, and gas/liquid equilibrium, among other aspects of CO2 absorption [13][14][15]. However, significant amounts of heat are required to regenerate the amine solvent used in CO2 absorption.…”

Section: Literature Reviewmentioning

confidence: 99%

Simulation model of carbon capture with MEA and the effect of temperature and duty on efficiency

Majnoon,

Hajinezhad,

Moosavian

2024

fuen

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Humans continue to rely on fossil fuels to generate electricity. In other words, fossil fuels are the world's largest energy producers. Fossil fuels produce significant carbon dioxide, mostly in areas where humans live. Although the share of carbon dioxide produced in big cities is minimal compared to the carbon dioxide production of volcanoes, the production of carbon dioxide in big cities has destructive effects. Process Simulator is utilized to evaluate the effectiveness of their simulation model by subjecting it to various experimental conditions, including liquid loading, temperature, and CO2 absorption (PPS). Comparing empirical and simulated mass transfer coefficients distinguishes this study from others. This procedure consists of two steps: Carbon dioxide (CO2) absorption in a solvent produces highly concentrated CO2 gas following solvent regeneration. A chemical adsorption process's scalability depends on accurate simulation models, typically validated using data from a pilot plant. With the aid of this study, a simulation model of a desorption column is constructed with ASPEN PLUS and 42% MEA validated. In addition, the effect of the weight percentage of 20-42 MEA in the inlet stream on the efficiency is investigated, and the influence of the MEA inlet temperature on system efficiency is examined. Then, the recommended temperature is confirmed based on the MEA's heat tolerance capacity of 303 Kelvin.

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Section: Literature Reviewmentioning

confidence: 99%