Structural investigation of La2SrDyCu2Oy complexities

Emetere, M. E.; Sanni, Samuel Eshorame; Abodurin, J.T.; Okoro, Emeka Emmanuel; Atayero, A. A.; Akinsiku, Anuoluwa Abimbola

doi:10.1016/j.matchemphys.2019.03.052

Cited by 4 publications

(1 citation statement)

References 30 publications

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“…The heating utility can be used only above the pinch and the cooling utility only below it (Sojitra 2016). The heat exchanger cannot be used across the pinch point, because all heat flows must be increased with this heat transferred (Mamudu et al 2019). Violation of this condition results in higher energy requirements than the minimum requirements theoretically possible.…”

Section: Process Descriptionmentioning

confidence: 99%

Rate and equilibrium based modeling with the sequential quadratic programming optimization method for glycol dehydration of produced natural gas

Okoro

Otuekpo²,

Ekeinde

et al. 2020

Braz. J. Chem. Eng.

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Determining the optimum temperature and pressure for the dehydration of natural gas in a glycol absorption unit and the recovery of the glycol from the glycol water mixture in a desorption unit is of great importance. Although, the equilibrium base model for the absorption column design had been in use, the rate based model for the absorption unit offers a promising technique and had been proven to be more accurate in determining the parameters for the design. In this study, dehydration of a natural gas plant was modelled with optimization of its parameters. The effects on cost were adequately studied. Sensitivity analysis resulting from the simulation showed that a lower temperature for effective absorption of the water from the gas stream by triethylene glycol (TEGlycol) solvent is expected, while a higher temperature and higher reboiler duty is required for the regeneration of the solvent from the Rich TEGlycol stream in a distillation column. The sequential quadratic programming (SQP) direct optimization method was employed to optimize the major parameters of the natural gas dehydration plant. The optimum temperature of 267 °F and Reboiler duty of 169,789 Btu/h gave a 0.99 TEGlycol recovery purity. A minimized capital cost of 3.73 million US Dollars and operating cost of approximately 1 million US dollars was also observed.

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Section: Process Descriptionmentioning

confidence: 99%