4.7 Article

Design and control of extraction combined with extractive distillation for separation isopropanol-butanol-ethanol-water with organic Rankine cycle

Journal

SEPARATION AND PURIFICATION TECHNOLOGY
Volume 313, Issue -, Pages -

Publisher

ELSEVIER
DOI: 10.1016/j.seppur.2023.123443

Keywords

IBE purification; Waste heat recovery; Organic Rankine cycle; Multi -objective optimization; Dynamic control; B butanol

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The separation process of IBE mixture was studied systematically in this paper. The operating parameters of E-ED were optimized using a multi-objective genetic algorithm, and the energy usage of the optimized process was analyzed using the pinch point technique. A new configuration combining E-ED-HI and ORC was proposed to further reduce the total cost.
The high-purity isopropanol butanol ethanol (IBE) mixture is a highly efficient gasoline additive that can be directly used without further separation. The product of isopropanol-butanol-ethanol fermentation contains a large amount of water, and a large amount of energy will be consumed in the purification process. In this paper, the separation IBE process is systematically studied from the aspects of process optimization, energy recovery and process control. The operation parameters of extraction combined with extractive distillation (E-ED) are optimized by a multi-objective genetic algorithm. Then, the pinch point technique is used to analyze the energy usage of the optimized process, and the maximum heat recovery heat integration scheme is obtained. Compared with the optimized process, the low pressure steam consumption of the heat integration process is reduced by 100%, the cooling water consumption is saved by 58.80%, and the TAC is reduced by 35.95%. In view of massive waste heat in the heat integration of the extraction combined with extractive distillation (E-ED-HI) process, a new configuration combining the E-ED-HI and organic Rankine cycle (E-ED-HI-ORC) is further proposed. The organic Rankine cycle using R600a can further reduce TAC by 8.88% based on the HI-E-ED process. Finally, the control scheme of E-ED process is proposed. The performance of the control scheme is examined with +/- 10% disturbance of the feed flow rate and composition change, and the results show that the process of extractive distillation and separation of IBE has good controllability.

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