Seawater desalination using PVDF-HFP membrane in DCMD process: assessment of operating condition by response surface method. Issue 2 (1st February 2019)

• Record Type: Journal Article
• Authors: Fadhil, Sufyan; Alsalhy, Qusay F.; Makki, Hassan F.; Ruby-Figueroa, René; Marino, Tiziana; Criscuoli, Alessandra; Macedonio, Francesca; Giorno, Lidietta; Drioli, Enrico; Figoli, Alberto
• Is Part Of: Chemical engineering communications. Volume 206:Issue 2(2019)
• Page Start: 237
• Page End: 246
• Publication Date: 2019-02-01
• Subjects: Central compose design -- DCMD -- Membrane distillation -- Optimization -- Optimum operating conditions -- Response surface method; Chemical engineering -- Periodicals; 660.205
• DOI: 10.1080/00986445.2018.1483349
• Languages: English
• ISSNs: 0098-6445

Abstract

Abstract: Central composite design (CCD) was applied in this work to analyze the performance of poly(vinylidene fluoride-co-hexafluoropropylene) (PVDF-HFP) flat sheet membrane in the seawater desalination using direct contact membrane distillation (DCMD) process. It is the most popular in response surface method (RSM). Development on Quadratic Regression model for membrane performance as a function of the operating conditions was studied. The ranges for each operating condition were selected as follows: feed temperature ( T f ): 48–58 °C, feed flow rate ( Q f ): 80–180 mL/min, permeate temperature ( T p ):17–22 °C and permeate flow rate ( Q p ): 80–180 mL/min. The model R -squared of 0.9759 (adjusted to degree-of-freedom), Lack-of-fit test ( p = 0.4764), predicted residual error sum of squared (PRESS) statistic of 10.3 suggest that the model is adequate to correlate the impact of operating conditions on permeates. ANOVA analysis showed that factors as feed flow rate, feed temperature, and permeate temperature have a valuable impact ( p ≤ 0.05) on the response variable. Additionally, the interaction among feed temperature-feed flow rate, feed flow rate-permeate flow rate, and the quadratic impact of feed temperature, permeate temperature, and permeate flow rate have shown an important impact ( p ≤ 0.05) on the permeate flux. Optimization of operating conditions to make the permeate flux and salt rejection high as possible was determined according to desirability function approach. A desirability of 0.969 was achieved at a feed temperature of 58 °C, feed flow rate of 180 mL/min, permeate temperature of 18.8 °C, and permeate flow rate of 145.3 mL/min in which a permeate flux of 12.56 kg/m 2 h and a salt rejection of 99.97% was obtained.