Separation and Purification Technology, Journal Year: 2024, Volume and Issue: unknown, P. 130622 - 130622
Published: Nov. 1, 2024
Language: Английский
Separation and Purification Technology, Journal Year: 2024, Volume and Issue: unknown, P. 130622 - 130622
Published: Nov. 1, 2024
Language: Английский
AIChE Journal, Journal Year: 2025, Volume and Issue: unknown
Published: Jan. 31, 2025
Abstract Distillation is widely used for separating liquid mixtures, but its high heating demand poses challenges achieving net‐zero emissions. This study presents an innovative approach to electrifying distillation load adaptability and flexible operation, aligning with dynamic electricity markets driven by renewables. The integrates flash vapor circulation thermal storage into the optimize power usage capitalizes on economic opportunities from load‐flexible operation in response fluctuating pricing. A methanol/water case study, using two typical pricing scenarios, demonstrates that proposed more economically efficient than mechanical recompression distillation, especially lowering operational costs when latter operates under fixed However, compressor capital significantly impact overall costs, sensitivity analysis examining different cost models. can be applied general allowing integration sector programs, while enhancing flexibility, decarbonization, efficiency.
Language: Английский
Citations
1Computers & Chemical Engineering, Journal Year: 2025, Volume and Issue: unknown, P. 109144 - 109144
Published: April 1, 2025
Language: Английский
Citations
1Applied Thermal Engineering, Journal Year: 2025, Volume and Issue: unknown, P. 126559 - 126559
Published: April 1, 2025
Language: Английский
Citations
1Separation and Purification Technology, Journal Year: 2024, Volume and Issue: 360, P. 130994 - 130994
Published: Dec. 8, 2024
Language: Английский
Citations
5Joule, Journal Year: 2024, Volume and Issue: 8(10), P. 2938 - 2949
Published: Aug. 19, 2024
Language: Английский
Citations
4Separation and Purification Technology, Journal Year: 2025, Volume and Issue: unknown, P. 131552 - 131552
Published: Jan. 1, 2025
Language: Английский
Citations
0Processes, Journal Year: 2025, Volume and Issue: 13(2), P. 391 - 391
Published: Feb. 1, 2025
The benzene–toluene–xylene (BTX) system represents an energy-intensive petrochemical process with various industrial applications. Global climate changes have forced modern industry to act toward environmental safety, which requires technological changes. Thus, the divided wall column (DWC) a significant advancement in multicomponent mixture separation. To assess impact of conventional BTX and its intensification proposal based on DWC technology, it is necessary integrate eco-efficiency approach that jointly analyzes economic variables influencing system, such as water consumption, CO2 emissions, utility costs. An auxiliary plant was also considered for more realistic results terms energy identified lack many research studies performed overall sustainability analysis. showed scheme 37.5% eco-efficient than counterpart, mainly due 15.6% 30.3% savings respectively, provided 15.5% 16.7% reduction emissions costs, respectively. In addition, all other safety indicators waste algorithm (WAR) were reduced by approximately 16%. proved be convenient technology attractiveness friendliness.
Language: Английский
Citations
0Separation and Purification Technology, Journal Year: 2025, Volume and Issue: unknown, P. 132042 - 132042
Published: Feb. 1, 2025
Language: Английский
Citations
0AIChE Journal, Journal Year: 2025, Volume and Issue: unknown
Published: April 17, 2025
Abstract Electrification of distillation processes through discretely heat integrated columns (D‐HIDiC) is an effective approach to enhance energy efficiency and lower carbon emissions. For separating systems with high temperature lift, multi‐stage compression inter‐stage cooling are necessary link the high‐pressure rectifier low‐pressure stripper. Traditionally, recovery employs pumparound loops, but this study introduces liquid injection as a more efficient innovative alternative. Simulation results using methanol/water separation indicate that reduces both reboiler duty power, achieving up 50% primary savings compared conventional columns. Unlike continuous exchange in HIDiC (C‐HIDiC), D‐HIDiC simplifies integration, avoiding complex hardware penalties. Comparative analysis across multiple configurations, including SuperHIDiC, confirms potential fully electrify distillation, eliminate steam utility, significantly support sustainable industrial operations.
Language: Английский
Citations
0Applied Thermal Engineering, Journal Year: 2025, Volume and Issue: unknown, P. 126753 - 126753
Published: May 1, 2025
Language: Английский
Citations
0