TY - JOUR
T1 - Polypropylene hollow fiber membrane prepared with green binary diluents via TIPS
T2 - Effects of spinning process parameters and VMD desalination performance
AU - Wang, Yu Jie
AU - Liu, Yiqun
AU - Wei, Xin
AU - Ding, Li Ming
AU - Feng, Ying Nan
AU - Zhao, Zhi Ping
N1 - Publisher Copyright:
© 2022 Elsevier B.V.
PY - 2022/11/1
Y1 - 2022/11/1
N2 - Environmental-friendly castor oil (CO) and soybean oil (SO) were used as mixed diluents to spin polypropylene (PP) hollow fiber microporous membrane (HFMM) via thermally induced phase separation. With the addition of castor oil, the cloud point temperature gradually increases, and the region of liquid-liquid phase separation becomes larger. The membrane pore structure changes from a spherulitic form to a continuous sponge-like pore structure. Particularly, the effects of spinning process parameters (spinning speed, spinneret temperature and bore liquid temperature) on HFMM properties (e.g., mechanical properties, water contact angle, pore size and pore size distribution) and desalination performance of vacuum membrane distillation (VMD) were further studied. A higher spinning speed and smaller temperature difference between dope and spinneret/bore fluid increase pore size and reduce membrane porosity. The PP HFMM produced under the spinneret temperature of 160 °C, the bore fluid temperature of 113 °C, and spinning speed of 16.1 m/min reached relatively high VMD desalination performance both feeding 10 g/L NaCl solution (water flux 18.4 kg/m2·h and salt rejection 99.99 %) and petrochemical saline wastewater (water flux 14.0 kg/m2·h and salt rejection 99.5 %). This paper has important guiding significance for the mass production of PP HFMMs.
AB - Environmental-friendly castor oil (CO) and soybean oil (SO) were used as mixed diluents to spin polypropylene (PP) hollow fiber microporous membrane (HFMM) via thermally induced phase separation. With the addition of castor oil, the cloud point temperature gradually increases, and the region of liquid-liquid phase separation becomes larger. The membrane pore structure changes from a spherulitic form to a continuous sponge-like pore structure. Particularly, the effects of spinning process parameters (spinning speed, spinneret temperature and bore liquid temperature) on HFMM properties (e.g., mechanical properties, water contact angle, pore size and pore size distribution) and desalination performance of vacuum membrane distillation (VMD) were further studied. A higher spinning speed and smaller temperature difference between dope and spinneret/bore fluid increase pore size and reduce membrane porosity. The PP HFMM produced under the spinneret temperature of 160 °C, the bore fluid temperature of 113 °C, and spinning speed of 16.1 m/min reached relatively high VMD desalination performance both feeding 10 g/L NaCl solution (water flux 18.4 kg/m2·h and salt rejection 99.99 %) and petrochemical saline wastewater (water flux 14.0 kg/m2·h and salt rejection 99.5 %). This paper has important guiding significance for the mass production of PP HFMMs.
KW - Environmental-friendly diluents
KW - Polypropylene hollow fiber microporous membranes
KW - Spinning process parameters
KW - Thermally induced phase separation (TIPS)
KW - Vacuum membrane distillation
UR - http://www.scopus.com/inward/record.url?scp=85135711998&partnerID=8YFLogxK
U2 - 10.1016/j.desal.2022.116026
DO - 10.1016/j.desal.2022.116026
M3 - Article
AN - SCOPUS:85135711998
SN - 0011-9164
VL - 541
JO - Desalination
JF - Desalination
M1 - 116026
ER -