Dataset for "3D Printed Fouling-Resistant Composite Membranes"

698 66 11796 2 34161 document 11796 Digital wavy support.jpg image/jpeg 56a86e5c2b001e7880d0ca5a926147dc MD5 31262 2019-08-22 11:20:52 https://researchdata.bath.ac.uk/698/1/Digital%20wavy%20support.jpg 698 1 1 image/jpeg other Digital image of wavy support en public

Digital wavy support.jpg

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Optical wavy support.jpg

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SEM micrograph of cross section of active layer.jpg

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SEM micrograph of surface of 3D composite membrane.jpg

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SEM micrograph of surface of 3D support.jpg

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SEM micrograph of surface of active layer.jpg

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SEM micrograph of wavy support.jpg

data 11803 2 34175 document 11803 Permeance recovery ratio.xlsx application/vnd.openxmlformats-officedocument.spreadsheetml.sheet 58493538e32df769c1a9e9dace20b5df MD5 35933 2019-08-22 11:25:55 https://researchdata.bath.ac.uk/698/8/Permeance%20recovery%20ratio.xlsx 698 8 8 application/vnd.openxmlformats-officedocument.spreadsheetml.sheet other Excel file for original data of permeance recovery ratio with different Re numbers en public

Permeance recovery ratio.xlsx

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Pore size distrbution.xlsx

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http://eprints.org/relation/isVersionOf https://researchdata.bath.ac.uk/id/document/11802 http://eprints.org/relation/isVolatileVersionOf https://researchdata.bath.ac.uk/id/document/11802 http://eprints.org/relation/issmallThumbnailVersionOf https://researchdata.bath.ac.uk/id/document/11802 archive 8912 disk0/00/00/06/98 2019-08-23 12:40:52 2024-07-15 10:59:13 2019-08-23 12:40:52 data_collection show Mazinani Saeed S.Mazinani@bath.ac.uk 0000-0001-8834-2803 University of Bath FALSE Al-Shimmery Abouther A.T.H.Al-Shimmery@bath.ac.uk University of Bath FALSE Chew John Y.M.Chew@bath.ac.uk 0000-0003-2888-834X University of Bath FALSE Mattia Davide D.Mattia@bath.ac.uk 0000-0002-7679-4105 University of Bath FALSE Dataset for "3D Printed Fouling-Resistant Composite Membranes" JH0060 JK0040 JK0500 dept_chem_eng This dataset reports the permeance recovery ratio values for flat and wavy composite membranes that were tested by using bovine serum albumin (BSA) solution in a cross-flow ultrafiltration setup. The transmembrane pressure was regulated at 1 bar and the cross-flow Reynolds number (Re) varied between 400 and 1000. In comparison to the flat composite membrane, the wavy membrane showed superior performance in terms of pure water permeance (PWP) (10% higher) and permeance recovery ratio (87% vs 53%) after the first filtration cycle at Re = 1000. Prolong testing showed that the wavy membrane could retain approximately 87% of its initial PWP after 10 complete filtration cycles. The dataset includes the all original data that were generated from this experimental work and also images that were taken by scanning electron microscope (SEM) and digital microscope. 2019-08-23 University of Bath public RightsHolder University of Bath Engineering and Physical Sciences Research Council https://doi.org/10.13039/501100000266 EP/M01486X/1 SynFabFun - From Membrane Material Synthesis to Fabrication and Function case Numerical simulations: the conservation of mass and momentum equations, and particle tracing model for steady state and laminar flow conditions were solved by using a commercial CFD software COMSOL MultiphysicsTM v5.4 to elucidate the fluid mechanics of the filtration process of flat and wavy 3D composite membranes. Fabrication of membrane support: the building material for the membrane support was a UV-cured polyurethane acrylate oligomer with the commercial name VisiJet M3-X. This ABS-like thermoplastic material has a high tensile strength and resistance to temperature along with good durability and stability which make it suitable being a membrane support.34 The support material was hydroxylated wax with the commercial name VisiJet S300. Fabrication of the 3D composite membranes: there were three main steps to fabricate the 3D printed composite membrane: (i) printing of the 3D supports, (ii) preparation of selective layer by non-induced phase separation and (iii) deposition of selective layer over the support. Filtration and anti-fouling performance: the filtration performance of the membranes was evaluated by using a circulating cross-flow apparatus (Figure S1 in the Supporting Information). Prior to the filtration experiments, the membranes were pre-compacted using pure water at 2 bar until steady permeance was reached. The required duration for pre-compaction was just less than 2 hrs. 1. 3D printer (ProJet 3500 HD Max printer, 3D Systems, USA) 2. Contact angle goniometer (OCA machine, Data Physics, Germany) 3. Scanning electron microscope (JEOL FESEM6301F) and a digital microscope (VHX - 6000, Japan). 4. Crossflow cell 5. AFM (AFM; Nanosurf EasyScan 2 Flex, Switzerland) 2017-09-05 2018-11-01 en 1 10.15125/BATH-00698 https://doi.org/10.1021/acsami.9b07764 pub open