代表性研究成果
[1]Feng, Z.*; Zhang, J.; Leng, J.; Fan, S.; Wan, Q.; Dong, L.*Enhancing Economic, Exergy Efficiency and Environment of Extractive Distillation Processes via Integrating Two-Enthalpy-Feed and Vapor Recompression Heat Pump.Sep. Purif. Technol.2025, 360 (P1), 130950.
[2]Feng, Z.*; Li, Q.; Rangaiah, G. P.; Leng, J.; Fan, S.; Wang, W.; Dong, L.*Economic and Exergy Analysis of Three-Product Dividing-Wall Column and Double Liquid-Only Side-Stream Distillation Processes.Chem. Eng. Res. Des.2023, 200, 729–740.
[3]Feng, Z.*; Wang, W.; Xu, D.; Rangaiah, G. P.; Dong, L.*Dynamic Controllability of Temperature Difference Control for the Operation of Double Liquid-Only Side-Stream Distillation.Comput. Chem. Eng.2022, 164, 107870.
[4]Feng, Z.; Shen, W.; Rangaiah, G. P.*; Lv, L.; Dong, L.*Process Development, Assessment, and Control of Reactive Dividing-Wall Column with Vapor Recompression for Producing n -Propyl Acetate.Ind. Eng. Chem. Res.2019, 58 (1), 276–295.
[5]Feng, Z.; Shen, W.; Rangaiah, G. P.*; Dong, L.*Proportional-Integral Control and Model Predictive Control of Extractive Dividing-Wall Column Based on Temperature Differences.Ind. Eng. Chem. Res.2018, 57 (31), 10572–10590.
[6]Rangaiah, G. P.*; Feng, Z.; Hoadley, A. F. Multi-Objective Optimization Applications in Chemical Process Engineering: Tutorial and Review. Processes 2020, 8 (5), 508.
[7]Feng, Z.; Shen, W.; Rangaiah, G. P.*; Dong, L.*Design and Control of Vapor Recompression Assisted Extractive Distillation for Separating N-Hexane and Ethyl Acetate.Sep. Purif. Technol.2020, 240, 116655.
[8]Feng, Z.; Shen, W.; Rangaiah, G. P.*; Dong, L.*Closed-Loop Identification and Model Predictive Control of Extractive Dividing-Wall Column.Chem. Eng. Process. - Process Intensif.2019, 142, 107552.
[9]Li, Q.;Feng, Z.*; Rangaiah, G. P.; Dong, L.*Process Optimization of Heat-Integrated Extractive Dividing-Wall Columns for Energy-Saving Separation of CO2and Hydrocarbons.Ind. Eng. Chem. Res.2020, 59 (23), 11000–11011.
[10]Fan, S.; Leng, J.;Feng, Z.*; Lu, R.; Dong, L.*; Lu, C. Dynamic Control of Bottom Flash Heat Pump-Assisted Extractive Distillation Process for Separating n-Hexane and 1,2-Dichloroethane.Sep. Purif. Technol.2025, 354 (P2), 128830.
[11]Leng, J.; Fan, S.; Dong, L.*;Feng, Z.*Design and Optimization of Energy-Saving Heterogeneous Azeotropic Distillation Processes for the Separation of Ternary Mixture of Ethyl Acetate/n-Propanol/Water.Sep. Purif. Technol.2025, 359 (P2), 130537.
[12]Song, C.; Leng, J.; Dong, L.*;Feng, Z.*Design and Optimization of Reactive Diving Wall Distillation Column Process for Methyl Methacrylate Production.Sep. Purif. Technol.2025, 360 (P2), 130992.
[13]Li, Q.; Machida, H.; Ren, X.;Feng, Z.*; Norinaga, K.*Design and Optimization of the Flexible Poly-Generation Process for Methanol and Formic Acid from CO2 Hydrogenation under Uncertain Product Prices. Int. J. Hydrogen Energy 2023, 54, 635–651.
[14]Fan, S.;Feng, Z.*; Lu, R.; Lv, L.; Dong, L.*Enhanced Extractive Distillation Processes for Separating N-Hexane and 1,2-Dichloroethane via Bottom Flash Heat Pump.Chem. Eng. Process. - Process Intensif.2022, 179, 109069.
[15]He, Q.; Li, Q.; Tan, Y.; Dong, L.*;Feng, Z.*Multi-Objective Optimization of Sustainable Extractive Dividing-Wall Column Process for Separating Methanol and Trimethoxysilane Azeotrope Mixture.Chem. Eng. Process. - Process Intensif.2022, 181, 109141.
[16]Zhang, J.; Fan, S.;Feng, Z.; Dong, L.; Dai, Y. Supervised Integrated Deep Deterministic Policy Gradient Model for Enhanced Control of Chemical Processes. Chem. Eng. Sci. 2025, 301, 120762.
[17]Li, Q.; Machida, H.;Feng, Z.; Norinaga, K. LNG Oxy-Fuel Power and Green Methanol Poly Generation Systems Associated with CO2 Condensation Capture: Techno-Economic Environmental Assessment.Energy and Fuels2024, 38 (14), 13089–13103.
[18]Zhang, J.; Zhang, M.;Feng, Z.; Ruifang, L. V.; Lu, C.; Dai, Y.; Dong, L. Gated Recurrent Unit-Enhanced Deep Convolutional Neural Network for Real-Time Industrial Process Fault Diagnosis.Process Saf. Environ. Prot.2023, 175, 129–149.
[19]Zhang, J.; Dai, Y.;Feng, Z.; Dong, L. An Enhanced Temporal Algorithm- Coupled Optimized Adaptive Sparse Principal Component Analysis Methodology for Fault Diagnosis of Chemical Processes.Process Saf. Environ. Prot.2023, 174, 663–680.
[20]Leng, J.; Fan, S.; Lu, C.;Feng, Z.; Dong, L. Sustainable Design and Multi-Objective Optimization of Heat Pump Assisted Extractive Distillation Process for Separating a Ternary Mixture of Methyl Acetate, Tetrahydrofuran and Methanol.J. Clean. Prod.2023, 419, 138186.
[21]Chan, W.; Li, H.; Li, X.; Chang, F.; Wang, L.;Feng, Z.Exergoeconomic Analysis and Optimization of the Allam Cycle with Liquefied Natural Gas Cold Exergy Utilization. Energ. Convers. Manag. 2021, 235, 113972.