Design and optimization of a reactive divided-wall column for production of Fischer-Tropsch fuel: Unit operation for mini-scale power-to-liquid energy storage plants

被引:2
|
作者
Nezhad, Pouria Mohammad [1 ]
Arjomand, Alireza [2 ]
Panahi, Mehdi [1 ]
机构
[1] Ferdowsi Univ Mashhad, Fac Engn, Dept Chem Engn, Mashhad 9177948974, Iran
[2] Shahrood Univ Technol, Fac Chem & Mat Engn, Shahrood 3619995161, Iran
关键词
Energy storage; Power-to-liquid; Fischer-Tropsch-fuel; Process intensification; Reactive divided-wall column; Response surface methodology; RESPONSE-SURFACE METHODOLOGY; DISTILLATION; HYDROGEN; FEASIBILITY; FRAMEWORK; AMMONIA; MODEL; GAS;
D O I
10.1016/j.est.2024.110736
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Power -to -liquid (PtL) can serve as long-term energy storage and help maintain grid stability. In addition, the local generation of power promotes compact, small-scale, and container -based unit operations adjacent to the renewable energy source. So, it facilitates the proximity of energy sources to end users and improves energy supply security. This paper deals with the intensification of mini -scale Fischer-Tropsch synthesis and downstream upgrading units in a single divided -wall column for a PtL process. Due to the complexity of the simulated model, a surrogate model was used for optimization. Three methods of response surface methodology (RSM), least squares support vector machine, and multi -layer perceptron neural networks were used to find the best surrogate model. The results showed that RSM was the best surrogate model for the studied plant. The results of the analysis of variance sensitivity analysis showed that the most important design variable was the liquid split fraction over the wall. The proposed design was optimized for maximum variable income with a genetic algorithm. The optimal conversions of hydrogen and carbon monoxide were 82.09 % and 77.36 %, respectively. The proposed optimal plant required 3896.74 kW of energy, while the plant itself produced 4584.79 kW of energy. The optimization results showed that the optimal plant, which was fed with 85,120.08 standard cum/d of syngas, produced 569.08 kg/h of different hydrocarbon cuts, which was equivalent to 18.24 standard cum/d. This product, with its high volumetric energy density, has considerable potential for energy storage.
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页数:17
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