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Performance Modeling and Cost Analysis of a Pilot-Scale Reverse Osmosis Process for the Final Purification of Olive Mill Wastewater
被引:6
|作者:
Miguel Ochando-Pulido, Javier
[1
]
Hodaifa, Gassan
[2
]
Dolores Victor-Ortega, Maria
[1
]
Martinez-Ferez, Antonio
[1
]
机构:
[1] Univ Granada, Dept Chem Engn, E-18071 Granada, Spain
[2] Univ Pablo de Olavide, Dept Mol Biol & Biochem Engn, Seville 41013, Spain
来源:
关键词:
olive mill wastewater;
advanced oxidation processes;
membrane processes;
reverse osmosis;
wastewater reclamation;
modelization;
D O I:
10.3390/membranes3040285
中图分类号:
Q5 [生物化学];
Q7 [分子生物学];
学科分类号:
071010 ;
081704 ;
摘要:
A secondary treatment for olive mill wastewater coming from factories working with the two-phase olive oil production process (OMW-2) has been set-up on an industrial scale in an olive oil mill in the premises of Jae n (Spain). The secondary treatment comprises Fenton-like oxidation followed by flocculation-sedimentation and filtration through olive stones. In this work, performance modelization and preliminary cost analysis of a final reverse osmosis (RO) process was examined on pilot scale for ulterior purification of OMW-2 with the goal of closing the loop of the industrial production process. Reduction of concentration polarization on the RO membrane equal to 26.3% was provided upon increment of the turbulence over the membrane to values of Reynolds number equal to 2.6 x 10(4). Medium operating pressure (25 bar) should be chosen to achieve significant steady state permeate flux (21.1 L h(-1) m(-2)) and minimize membrane fouling, ensuring less than 14.7% flux drop and up to 90% feed recovery. Under these conditions, irreversible fouling below 0.08 L h(-2) m(-2) bar(-1) helped increase the longevity of the membrane and reduce the costs of the treatment. For 10 m3 day(-1) OMW-2 on average, 47.4 m(2) required membrane area and 0.87 _ m(-3) total costs for the RO process were estimated.
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页码:285 / 297
页数:13
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