Journals / Sigma Mühendislik ve Fen Bilimleri Dergisi / 2016 / Cilt: 34 - Sayı: 1

THE EFFECTS OF FERRIC IRON AND ORGANIC MATTER ON ARSENITE REMOVAL FROM WATER BY DIRECT CONTACT MEMBRANE

Pages
81–89
Publication Date
2016-03-01
DOI
—
🏛️Bibliographic metadata and full text access for this article are provided via DergiPark.
DergiPark Record ↗
✨

AI Summary & Key Takeaways

AI Insight
⚡ TL;DR(Too Long; Didn't Read)

In presence of Fe(III) and at feed temperature of 40 and 50 oC, As(III) was non-detectable in the permeate.

📌 3 Key Takeaways

🎯
Objective & Hypothesis:The present study investigated the influence of ferric iron (Fe (III)) and organic matter (OM) on arsenite (As (III)) rejection from a synthetic contaminated water by direct contact membrane distillation (DCMD).
📊
Key Findings & Data:Two different pore sizes (0.22 μm and 0.45 μm) of hydrophobic membranes made of Polytetrafluoroethylene (PTFE) were used at different feed temperature (40, 50 and 60 oC).
💡
Conclusion & Impact:In presence of Fe(III) and at feed temperature of 40 and 50 oC, As(III) was non-detectable in the permeate.
🔬Design:Research Article
📍Scope:Comprehensive Sample
⚙️Variables:Arsenite removal · contaminated water · hydrophobic membrane

Abstract

The present study investigated the influence of ferric iron (Fe (III)) and organic matter (OM) on arsenite (As (III)) rejection from a synthetic contaminated water by direct contact membrane distillation (DCMD). Two different pore sizes (0.22 μm and 0.45 μm) of hydrophobic membranes made of Polytetrafluoroethylene (PTFE) were used at different feed temperature (40, 50 and 60 oC). The operating temperatures, the feed solution Fe (III) and OM concentration have been varied during the study to follow pollutants rejection efficiency and flux behavior. Fe (III) and OM concentration in the solution did not affect negstively As(III) rejection; both membranes used had high rejection efficiency and permeate arsenic (As) concentration was lower than recommended 10 μg/L. As (III) concentration was below detection limit in many permeates. Fe(III) and OM contributed to higher rejection of As(III) and better transmembrane flux. Conductivity and As(III) was rejected up to 99%. In presence of Fe(III) and at feed temperature of 40 and 50 oC, As(III) was non-detectable in the permeate.

🔖

Cite This Article

ZOUNGRANA, A., ZENGİN, İ. H., ELCİK, H., YEŞİLIRMAK, D., ÇAKMAKCI, M. (2016). THE EFFECTS OF FERRIC IRON AND ORGANIC MATTER ON ARSENITE REMOVAL FROM WATER BY DIRECT CONTACT MEMBRANE. Sigma Mühendislik ve Fen Bilimleri Dergisi, Cilt: 34 - Sayı: 1, 81–89. https://ajindex.com/articles/419449

📄 Full Text PDF Viewer

📄

PDF görüntüleyici hazırlanıyor...

References (14)

  1. Qu, D., Wang, J., Hou, D., Luan, Z., Fan, B., Zhao, C. (2009), “Experimental study of arsenic removal by direct contact membrane distillation”, Journal of Hazardous Materials, 163, 874–879
  2. Criscuoli, A., Bafaro, P., Drioli, E. (2012), “Vacuum membrane distillation for purifying waters containing arsenic”, Desalination xxx xxx–xxx
  3. Singh R., Singh S., Parihar P., Singh V.P., Prasad S.M. (2015). “Arsenic contamination, consequences and remediation techniques: A review”, Ecotoxicology and Environmental Safety112(2015)247–270. doi.org/10.1016/j.ecoenv.2014.10.009
  4. Manna, A.K., Sen, M., Martin, A.R., Pal, P. (2010), “Removal of arsenic from contaminated groundwater by solar-driven membrane distillation”, Environ. Pollut., 158, 805-811
  5. Pal, P., Manna, K.A. (2010), “Removal of arsenic from contaminated groundwater by solar-driven membrane distillation using three different commercial membranes”, Water Res., 44, 5750-5760
  6. Jiang, J-Q., Ashekuzzaman, S. M., Jiang, A., Sharifuzzaman, S. M., Chowdhury, S.R. (2013), “Arsenic contaminated groundwater and its treatment options in Bangladesh”, Int. J. Environ. Res. Public Health, 10, 18-46
  7. Caniyilmaz, S. (2003), “Arsenic Removal from Groundwater By Fe-Mn Oxidation And Microfiltration”, B.S., Middle East Technical University
  8. Petrusevski, B., Sharma, S., Schippers, J.C. (UNESCO-IHE), Shordt, K. (IRC) (2007), “Arsenic in Drinking Water”, March 2007 IRC International Water and Sanitation Centre
  9. Mondal, P., Bhowmick, S., Chatterjee, D., Figoli, A, Van der Bruggen, B. (2013), “Remediation of inorganic arsenic ingroundwater for safe water supply: A critical assessment of technological solutions”, Chemosphere, 92, 157–170
  10. Cakmakci, M., Baspinar, A. B., Balaban, U., Uyak, V., Koyuncu, I., Kinaci, C. (2009), “Comparison of nanofiltration and adsorption techniques to remove arsenic from drinking water”, Desalination and Water Treatment, 9, 149–154
  11. Elcik, H., Cakmakci, M., Sahinkaya, E., Ozkaya, B. (2013), “Arsenic removal from drinking water using low pressure membranes”, Ind. Eng. Chem. Res., 52, 9958−9964
  12. Pal P. (2015). “Arsenic Removal by Membrane Distillation”, 2015 Elsevier Inc. doi.org/10.1016/B978-0-12-801281-9.00005-9
  13. Boubakri, S., Bouguecha, A-T., Dhaouadi, I., Hafiane, A. (2015), “Effect of operating parameters on boron removal from seawater using membrane distillation process”, Desalination, 373, 86–93
  14. Meng, S., Yea, Y., Mansouri, J., Chen, V. (2015