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Sci Rep. 2017 Sep 25;7(1):12267. doi: 10.1038/s41598-017-12499-w.

Superhydrophilic Functionalization of Microfiltration Ceramic Membranes Enables Separation of Hydrocarbons from Frac and Produced Water.

Scientific reports

Samuel J Maguire-Boyle, Joseph E Huseman, Thomas J Ainscough, Darren L Oatley-Radcliffe, Abdullah A Alabdulkarem, Sattam Fahad Al-Mojil, Andrew R Barron

Affiliations

  1. Department of Chemistry, Rice University, Houston, Texas, 77007, USA.
  2. Energy Safety Research Institute, Swansea University, Bay Campus, Swansea, SA1 8EN, Wales, UK.
  3. Mechanical Engineering Department, College of Engineering, King Saud University, Riyadh, 11421, Saudi Arabia.
  4. Department of Civil Engineering, College of Engineering, King Saud University, Riyadh, 11421, Saudi Arabia.
  5. Department of Chemistry, Rice University, Houston, Texas, 77007, USA. [email protected].
  6. Energy Safety Research Institute, Swansea University, Bay Campus, Swansea, SA1 8EN, Wales, UK. [email protected].
  7. Department of Materials Science and Nanoengineering, Rice University, Houston, Texas, 77007, USA. [email protected].

PMID: 28947793 PMCID: PMC5612970 DOI: 10.1038/s41598-017-12499-w

Abstract

The environmental impact of shale oil and gas production by hydraulic fracturing (fracking) is of increasing concern. The biggest potential source of environmental contamination is flowback and produced water, which is highly contaminated with hydrocarbons, bacteria and particulates, meaning that traditional membranes are readily fouled. We show the chemical functionalisation of alumina ceramic microfiltration membranes (0.22 μm pore size) with cysteic acid creates a superhydrophilic surface, allowing for separation of hydrocarbons from frac and produced waters without fouling. The single pass rejection coefficients was >90% for all samples. The separation of hydrocarbons from water when the former have hydrodynamic diameters smaller than the pore size of the membrane is due to the zwitter ionically charged superhydrophilic pore surface. Membrane fouling is essentially eliminated, while a specific flux is obtained at a lower pressure (<2 bar) than that required achieving the same flux for the untreated membrane (4-8 bar).

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