کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
623332 1455338 2015 13 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Multi-walled carbon nanotube/PVDF blended membranes with sponge- and finger-like pores for direct contact membrane distillation
ترجمه فارسی عنوان
غشاهای مخلوط شده با نانولوله های کربنی چند دیواره با منافذ اسفنجی و انگشتی برای تقطیر با غلظت تماس مستقیم
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی تصفیه و جداسازی
چکیده انگلیسی


• MWCNT/PVDF blended membranes prepared by phase inversion method
• Membranes tested in direct contact membrane distillation (DCMD) of salty water
• Large sponge-like pores and small membrane thickness allow complete salt rejection.
• Functionalization of MWCNTs and PVP addition are not recommended.
• The membrane with 0.2 wt.% of pristine MWCNTs exhibited the best performance.

Polyvinylidene fluoride (PVDF) flat sheet membranes were blended with multi-walled carbon nanotubes (MWCNTs) by the phase inversion method for direct contact membrane distillation (DCMD) of salty water (35 g L− 1 NaCl). The membrane properties and performances depended markedly on the synthesis parameters such as MWCNT loading, polyvinylpyrrolidone (PVP) addition and MWCNT surface chemistry. MWCNT/PVDF membranes prepared with functionalized MWCNTs have a smaller pore size (determined by bubble point measurements) and lower contact angles, thus, functionalization of MWCNTs is not recommended for this application. For membranes presenting the same pore size, the pore morphology and the membrane thickness are crucial for efficient salt rejection. Sponge-like pores and the smallest possible thickness (i.e., membranes prepared without PVP) allow complete salt rejection (i.e., 100%), in contrast with larger thickness and elongated finger-like pores (resulting from PVP addition) whose salt exclusion ranged from 88.8 to 98.6%. Overall, the MWCNT/PVDF blended membrane prepared with 0.2 wt.% optimal content of pristine MWCNTs (without adding PVP) exhibited the best performance in DCMD, presenting total salt rejection and a higher permeate flux (9.5 × 10− 3 kg m− 2 s− 1) than that obtained with a commercial PVDF membrane (7.8 × 10− 3 kg m− 2 s− 1).

Figure optionsDownload as PowerPoint slide

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Desalination - Volume 357, 2 February 2015, Pages 233–245
نویسندگان
, , , ,