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Applied pilot-scale studies on ceramic membrane processes for the treatment of wastewater streamsView Crossref metadata(active tab) <div id="edit-xml" class="form-item form-type-item"> <?xml version="1.0"?> <doi_batch version="4.4.1" xmlns="http://www.crossref.org/schema/4.4.1" xmlns:jats="http://www.ncbi.nlm.nih.gov/JATS1" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.crossref.org/schema/4.4.1 http://www.crossref.org/schemas/crossref4.4.1.xsd"><head><doi_batch_id>000695</doi_batch_id><timestamp>1714012075</timestamp><depositor><depositor_name>University of the Aegean</depositor_name><email_address>uoa@university.com</email_address></depositor><registrant>Global NEST Journal</registrant></head><body><journal><journal_metadata><full_title>Global NEST Journal</full_title><full_title>Global NEST: the international Journal</full_title><issn media_type="print">1790-7632</issn><issn media_type="electronic">2241-777X</issn></journal_metadata><journal_issue><titles><title>Issue 1</title></titles><publication_date><month>03</month><year>2024</year></publication_date><journal_volume><volume>8</volume></journal_volume><issue>1</issue></journal_issue><journal_article><titles><title>Applied pilot-scale studies on ceramic membrane processes for the treatment of wastewater streams</title></titles><abstract xmlns="http://www.ncbi.nlm.nih.gov/JATS1"><p>Asymmetric multilayer Al2O3 ceramic membranes with pore sizes ranging from 3 to 500 nm are synthesized in tubular form with external diameter of 14mm, internal diameter of 8mm and length of 340mm. The membrane synthesis took place on commercially available supports, with the dip-coating technique either from aloumina particle suspensions or from boehmite sols. The membranes are subsequently mounted in a pilot-scale module able to accept six specimens, and used in micro- and ultra- filtration experiments for the purification of aqueous streams from suspended solids. The experimental module is equipped with a back-flushing circuit that can be activated on demand to prevent the fouling of the membranes and the associated reduction in permeability. For the microfiltration experiments membranes with 100nm pore size are used. In the case of an aqueous solid suspension with a concentration of 0.1 to 1 wt.% consisting of solid particles with an average size of 0.5 μm, complete solid rejection is observed. The process has a capability of treating 0.8 m3 of feed per hour per square meter of membrane surface under an average pressure difference of 3 x 105 Nt m-2. The fouling of the membranes can be quite effectively reduced by back flushing at regular time intervals. Under complete retentate recycling conditions, more than 95% of the feed volume can be recovered as microparticle free water. For the ultrafiltration experiments membranes with 3 nm pore sizes are used. In the case of an aqueous solid suspension of nanoparticles with a concentration of 0.1 to 1 wt.% consisting of solid particles with sizes of 20-30 nm the rejection was also almost complete. The process has in this case a capability of treating 0.16 m3 of feed per hour per square meter of membrane surface under an average pressure difference of 3 x 105 Nt m-2. Fouling appears not to cause serious permeability drop in this case probably because even after the nanoparticle deposition the membrane hydraulic resistance is the permeability determining step. Almost the entire feed volume can be recovered as nanoparticle free water under complete retentate recycling conditions. Purification experiments are also performed in olive oil mill wastewater. Best results are achieved by using a two step membrane process with gradually decreasing pore size. Although complete rejection of solids and significant reduction of the BOD5 and phenol content of the wastes is achieved, the very low permeability is the main draw back of the process.</p></abstract><publication_date><month>04</month><day>29</day><year>2013</year></publication_date><pages><first_page>23</first_page><last_page>30</last_page></pages><publisher_item><identifier id_type="pii">366</identifier></publisher_item><doi_data><doi>10.30955/gnj.000366</doi><timestamp>1714012075</timestamp><resource>https://journal.gnest.org/publication/366</resource></doi_data></journal_article></journal></body></doi_batch> </div>
