4.5 Article

The Effect of Ceramic Membranes' Structure on the Oil and Ions Removal in Pre-Treatment of the Desalter Unit Wastewater

Journal

MEMBRANES
Volume 12, Issue 1, Pages -

Publisher

MDPI
DOI: 10.3390/membranes12010059

Keywords

ceramic membrane; oily wastewater; desalter unit; microfiltration; salt; oil rejection; permeation flux

Ask authors/readers for more resources

In this study, four inexpensive ceramic microfiltration membranes were synthesized and their performance in treating salt-containing wastewater was investigated. The results showed that the permeate flux of the membranes increased significantly at lower salt concentrations, but decreased at higher concentrations. Furthermore, the rejection of ions slightly increased with the increase in salt dosage, while the oil rejection remained relatively constant.
Salts, organic materials, and hazardous materials can be found regularly in the effluent from a desalter unit of crude oil. These materials should be separated from the wastewater. Four kinds of inexpensive and innovative ceramic microfiltration membranes (mullite, mullite-alumina (MA 50%), mullite-alumina-zeolite (MAZ 20%), and mullite-zeolite (MZ 40%)) were synthesized in this research using locally available inexpensive raw materials such as kaolin clay, natural zeolite, and alpha-alumina powders. Analyses carried out on the membranes include XRD, SEM, void fraction, the average diameter of the pores, and the ability to withstand mechanical stress. Effluent from the desalter unit was synthesized in the laboratory using the salts most present in the desalter wastewater (NaCl, MgCl2, and CaCl2) and crude oil. This synthesized wastewater was treated with prepared ceramic membranes. It was discovered that different salt concentrations (0, 5000, 25,000, 50,000, 75,000, and 100,000 mg L-1) affected the permeate flux (PF), oil rejection, and ion rejection by the membrane. Results showed that in a lower concentration of salts (5000 and 25,000 mg L-1), PF of all types of ceramic membranes was increased significantly, while in the higher concentration, PF declined due to polarization concentration and high fouling effects. Oil and ion rejection was increased slightly by increasing salt dosage in wastewater due to higher ionic strength. Monovalent (Na+) and multivalent (Ca2+ and Mg2+) ion rejection was reported about 5 to 13%, and 23 to 40% respectively. Oil rejection varied from 96.2 to 99.2%.

Authors

I am an author on this paper
Click your name to claim this paper and add it to your profile.

Reviews

Primary Rating

4.5
Not enough ratings

Secondary Ratings

Novelty
-
Significance
-
Scientific rigor
-
Rate this paper

Recommended

No Data Available
No Data Available