Forward Osmosis: Temperature Effects By Using Pome as Feed Solution

https://doi.org/10.22146/ajche.49691

Hanizah Arifin(1*), Thomas S.Y. Choong(2), Chan Kam Rong(3), Fakhru'l Al-Razi Ahmadun(4), Luqman Chuah Abdullah(5)

(1) Faculty of Engineering, Department of Chemical and Environmental Engineering, Universiti Putra Malaysia, 43400, UPM Serdang, Selangor, MALAYSIA
(2) Faculty of Engineering, Department of Chemical and Environmental Engineering, Universiti Putra Malaysia, 43400, UPM Serdang, Selangor, MALAYSIA; INTROP, Universiti Putra Malaysia , 43400, UPM Serdang, Selangor, MALAYSIA
(3) Faculty of Engineering, Department of Chemical and Environmental Engineering, Universiti Putra Malaysia, 43400, UPM Serdang, Selangor, MALAYSIA
(4) Faculty of Engineering, Department of Chemical and Environmental Engineering, Universiti Putra Malaysia, 43400, UPM Serdang, Selangor, MALAYSIA
(5) Faculty of Engineering, Department of Chemical and Environmental Engineering, Universiti Putra Malaysia, 43400, UPM Serdang, Selangor, MALAYSIA
(*) Corresponding Author

Abstract


Forward osmosis (FO) has recently been considered as one of the promising technologies for low energy applications. Factors that influence FO performance are draw solution, types of membrane, membrane orientation, cross flow velocity, module configuration and temperature effect. In this study, the influence of temperature on the performance of FO process has been studied in terms of water flux by using raw POME as feed solution. A higher temperature creates a higher water fluxes at various draw solution concentrations. Percentages of water flux increments for raw POME are between 7% to 9% from 25ºC to 35ºC and 32% to 75% from 25ºC to 45ºC.

Keywords


Forward Osmosis, POME, temperature, membrane orientation, concentration polarization, water flux

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References

  1. Abdurahman N. H., Rosli Y. M.; and Azhari N. H. (2011). Development of a membrane anaerobic system (MAS) for palm oil mill effluent (POME) treatment. Desalination, 266, 208–212.
  2. Achilli A., Cath T. Y. ; and Childress A. E.(2009). Power generation with pressure retarded osmosis : An experimental and theoretical investigation Journal of Membrane Science, 343, 42–52.
  3. Achilli A., Cath T. Y., Marchand E. A.; and Childress A. E. (2009). The forward osmosis membrane bioreactor : A low fouling alternative to MBR processes. Desalination, 239, 10–21.
  4. Ahmad A. L., Chong M. F.; and Bhatia S. (2009). A comparative study on the membrane based palm oil mill effluent (POME) treatment plant. Journal of Hazard. Materials. 171, 166–174.
  5. Ahmad A.L., Chong M.F., Bhantia S.; and Ismail S. (2006). Drinking water reclamation from plam oil mill effluent (POME) using membrane technology. Desalination, 191, 35-44.
  6. Ahmad A.L., Ismail S.; and Bhatia S. (2003). Water recycling palm oil mill effluent (POME) using membrane technology. Desalination, 157, 87-95.
  7. Anna V. S., Ferreira Marczak L. D.; and Tessaro I. C. (2012). Membrane concentration of liquid foods by forward osmosis : Process and quality view. Journal of Food Engineering, 111, 483–489.
  8. Cath T. Y., Childress A. E.; and Elimelech M. (2006). Forward osmosis : Principles , applications , and recent developments. Journal of Membrane Science, 281, 70–87.
  9. Damayanti A., Ujang Z.; and Salim M. R. (2011). The influenced of PAC, zeolite, and Moringa oleifera as biofouling reducer (BFR) on hybrid membrane bioreactor of palm oil mill effluent (POME). Bioresource Technology, 102, 4341–4346.
  10. Holloway R. W., Childress A. E., Dennett K. E.; and Cath T. Y. (2007). Forward osmosis for concentration of anaerobic digester centrate. Water Research, 41, 4005–4014.
  11. Lee K. L., Baker R. W.; and Lonsdale H. K. (1981). Membranes for power generation by pressure-retarded osmosis. Journal of Membrane Science, 8, 141–171.
  12. Mandell A.; and McGinnis R. (2011). Guest Post: Desalination Realization. greentechmedia.
  13. McCutcheon J. R.; and Elimelech M. (2006). Influence of concentrative and dilutive internal concentration polarization on flux behavior in forward osmosis. Journal of Membrane Science, 284, 237–247.
  14. McCutcheon J. R., McGinnis R. L.; and Elimelech M. (2005). A novel ammonia- carbon dioxide forward ( direct ) osmosis desalination process. Desalination, 174, 1–11.
  15. Phuntsho S., Kyong Shon H., Vigneswaran S., Kandasamy J., Hong S.; and Lee S. (2012). Influence of temperature and temperature difference in the performance of forward osmosis desalination process. Journal of Membrane Science, 415–416, 734–744.
  16. Rupani P. F., Singh R. P., Ibrahim M. H.; and Esa N. (2010). Review of Current Palm Oil Mill Effluent (POME) Treatment Methods : Vermicomposting as a Sustainable Practice. World Applied Science Journal, 10, 1190–1201.
  17. Wei J., Qiu C., Tang C. Y, Wang R.; and Fane A. G. (2011). Synthesis and characterization of flat-sheet thin film composite forward osmosis membranes. Journal of Membrane Science, 372 (1–2), 292–302.
  18. Yacob S., Ali M., Shirai Y., Wakisaka M.; and Subash S. (2005). Baseline study of methane emission from open digesting tanks of palm oil mill effluent treatment. Chemosphere, 59, 1575– 1581.
  19. Yejian Z., Li Y. A. N., Xiangli Q., Lina C. H. I., Xiangjun N. I. U., Zhijian M. E. I.; and Zhenjia Z. (2008). Integration of biological method and membrane technology in treating palm oil mill effluent. Journal of Environmental Science, 20, 558–564.
  20. Zhao S.; and Zou L. (2011). Effects of working temperature on separation performance, membrane scaling and cleaning in forward osmosis desalination. Desalination, 278, 157–164.



DOI: https://doi.org/10.22146/ajche.49691

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ASEAN Journal of Chemical Engineering  (print ISSN 1655-4418; online ISSN 2655-5409) is published by Chemical Engineering Department, Faculty of Engineering, Universitas Gadjah Mada.