TY - JOUR
T1 - Energy Consumption of Nanofiltration Diafiltration Process
T2 - Identifying the Optimal Conditions of Continuous and Intermittent Feed Diafiltration
AU - Wang, Qian
AU - Sun, Shi Peng
AU - Wu, Qigang
AU - Huhe, Taoli
AU - Zhou, Zhengzhong
N1 - Publisher Copyright:
© 2022 American Chemical Society. All rights reserved.
PY - 2022/6/8
Y1 - 2022/6/8
N2 - The demand for the separation of small molecules (ions and small organics) is expanding with the development of various industries. The nanofiltration (NF) diafiltration process was developed to make up for the deficiencies of NF membrane performance to realize the separation of small molecules, but NF diafiltration is operated with high energy consumption. Therefore, optimizing the NF diafiltration process to reduce the required separation energy is inevitable. In this work, the minimum required separation energies (MRSEs) of continuous feed diafiltration (CFD) and intermittent feed diafiltration (IFD) under the reversible thermodynamic process and constant applied pressure mode are calculated and compared. Additionally, a reverse osmosis (RO) unit was designed to recycle the solvent, and the energy consumption of the integrated NF-RO process is evaluated and compared. Finally, based on the variation of osmotic pressure with solutes composition, the NF-RO process with various solute composition is modeled to calculate the MRSE. This work aims to provide guidance for the industrialization of NF diafiltration-RO concentration process, with potential application for small molecule separation.
AB - The demand for the separation of small molecules (ions and small organics) is expanding with the development of various industries. The nanofiltration (NF) diafiltration process was developed to make up for the deficiencies of NF membrane performance to realize the separation of small molecules, but NF diafiltration is operated with high energy consumption. Therefore, optimizing the NF diafiltration process to reduce the required separation energy is inevitable. In this work, the minimum required separation energies (MRSEs) of continuous feed diafiltration (CFD) and intermittent feed diafiltration (IFD) under the reversible thermodynamic process and constant applied pressure mode are calculated and compared. Additionally, a reverse osmosis (RO) unit was designed to recycle the solvent, and the energy consumption of the integrated NF-RO process is evaluated and compared. Finally, based on the variation of osmotic pressure with solutes composition, the NF-RO process with various solute composition is modeled to calculate the MRSE. This work aims to provide guidance for the industrialization of NF diafiltration-RO concentration process, with potential application for small molecule separation.
UR - http://www.scopus.com/inward/record.url?scp=85126088215&partnerID=8YFLogxK
U2 - 10.1021/acs.iecr.1c04868
DO - 10.1021/acs.iecr.1c04868
M3 - 文章
AN - SCOPUS:85126088215
SN - 0888-5885
VL - 61
SP - 7645
EP - 7653
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
IS - 22
ER -