Optimization of the Viscosity of Wack (Cameroon) Clay Slurry for Coating of a Filtration Layer over a Tubular Ceramic Support Layer by the Slip Casting Technique for Domestic Water Treatment
The objective of this work is to optimize the viscosity of Wack clay slurry for coating of a filtration layer over a tubular ceramic membrane support by the slip casting technique for application in domestic water treatment. Coating of a slurry over tubular ceramic membrane support by the slip casting technique requires a clay slurry of appropriate viscosity for it to adhere to the ceramic support by capillary suction. The clay slurry is elaborated using a mixture experimental design with constraint used to determine the optimum viscosity of the slurry, the proportions of raw materials in the slurry and the level of influence and interactions between the proportions of raw material on the viscosity of the slurry. The experimental domain used for the raw materials was: proportion of clay between 10% and 12%, proportion of binder between 11% and 22% and proportion of water between 66% and 79%. It resulted that the proportion of clay has the highest positive influence on the viscosity of the slurry and the interaction proportion of clay-proportion of binder influences positively the viscosity of the slurry. The optimal viscosity was found to be 40.4 mPa?s for optimal proportions of clay, binder and water/dispersant of 10%, 11% and 79% respectively. The prepared optimal slurry was then cast over the support for contact times of 2, 4 and 6 minutes in order to determine the effect time on the compromise homogeneity (no cracks) and thickness (5 - 15 μm) of the deposited layer. When each contact time was attended, it was dried, sintered at 900?C and characterized. It resulted that as the contact time increases, there is an increase in the thickness of the deposited layer from 8.8 to 23 μm with the gradual appearance of cracks from 4 minutes. The tubular membrane coated for 2 minutes gave the best results in terms of homogeneity and thickness of 8.8 μm. The porosity, permeability and average pore size this multilayer membrane were determined. It resulted from this that the membrane had a porosity of 32.6%, permeability of 305.67 L/h?m2 bar and an average pore size of 0.48 μm adapted for microfiltration.
References
[1]
Yanu, C.A., Sieliechi, J.M. and Ngassoum, M.B. (2020) Optimization of Ceramic Paste Viscosity Use for the Elaboration of Tubular Membrane Support by Extrusion and Its Application. JournalofMaterialsScienceandChemicalEngineering, 8, 1-22. https://doi.org/10.4236/msce.2020.83001
[2]
Nguiamba, N., Yanu, C.A., Belibi, P.D.B., Sieliechi, J.M. and Ngassoum, M.B. (2021) Identification of an Appropriate Formulation for Domestic Water Ceramic Filters from Soukamna Clay (Cameroon). JournalofMetallicMaterialResearch, 4, 12-18. https://doi.org/10.30564/jmmr.v4i1.3462
[3]
Ndiapa Wandji Fabrice (2020) Elaboration des membranes minérales multicouches de microfiltration contenant des nanoparticules d’argent pour le traitement de l’eau de consummation. Mémoire de soutenance du Doctorate/PhD en chimie industrielle de l’université de Ngaoundere.
[4]
Belibi Belibi, P., Nguemtchouin, M.M.G., Rivallin, M., Ndi Nsami, J., Sieliechi, J., Cerneaux, S., et al. (2015) Microfiltration Ceramic Membranes from Local Cameroonian Clay Applicable to Water Treatment. CeramicsInternational, 41, 2752-2759. https://doi.org/10.1016/j.ceramint.2014.10.090
[5]
Roseline, E. (2017) Matériaux membranaires en TiO2 sous-stœchiométrique pour le traitement de l’eau par procédé d’oxydation avancée électrochimique Pour obtenir le grade de DOCTEUR de l’Université de MONTPELIER II Soutenue le 17 Novembre 2017.
[6]
Iaich, S. and Messaoudi, L. (2014) Mise au point et caractérisation des membranes minérales de microfiltration déposées sur des supports céramiques tubulaires à base d’une. Journal of Materials and Environmental Science, 5, 1808-1815.
[7]
Vinoth Kumar, R., Kumar Ghoshal, A. and Pugazhenthi, G. (2015) Elaboration of Novel Tubular Ceramic Membrane from Inexpensive Raw Materials by Extrusion Method and Its Performance in Microfiltration of Synthetic Oily Wastewater Treatment. JournalofMembraneScience, 490, 92-102. https://doi.org/10.1016/j.memsci.2015.04.066
[8]
Chen, Z., Li, J., Liu, C., Liu, Y., Zhu, J. and Lao, C. (2019) Preparation of High Solid Loading and Low Viscosity Ceramic Slurries for Photopolymerization-Based 3D Printing. CeramicsInternational, 45, 11549-11557. https://doi.org/10.1016/j.ceramint.2019.03.024
[9]
Papadopoulou, A., Gillissen, J.J.J., Tiwari, M.K. and Balabani, S. (2020) Effect of Particle Specific Surface Area on the Rheology of Non-Brownian Silica Suspensions. Materials, 13, Article No. 4628. https://doi.org/10.3390/ma13204628
[10]
Ghouil, B., Harabi, A., Bouzerara, F. and Brihi, N. (2016) Elaboration and Characterization of Ceramic Membrane Supports from Raw Materials Used in Microfiltration. DesalinationandWaterTreatment, 57, 5241-5245. https://doi.org/10.1080/19443994.2015.1021098
[11]
Ha, J., Lee, S., Abbas Bukhari, S.Z., Choi, J.R., Lee, J., Song, I., et al. (2017) Preparation and Characterization of Alumina-Coated Silicon Carbide Supports. CeramicsInternational, 43, 9481-9487. https://doi.org/10.1016/j.ceramint.2017.04.126
[12]
Habib, B.A., Abd El-Samiae, A.S., El-Houssieny, B.M. and Tag, R. (2021) Formulation, Characterization, Optimization, and in-Vivo Performance of Febuxostat Self-Nano-Emulsifying System Loaded Sublingual Films. DrugDelivery, 28, 1321-1333. https://doi.org/10.1080/10717544.2021.1927247
[13]
Tayefi, M., Razavi-Nouri, M. and Sabet, A. (2020) Using Constrained Mixture Design Method for Optimizing the Properties of Organoclay Filled Ethylene-Octene Copolymer Nanocomposites. MaterialsResearchExpress, 7, Article ID: 015321. https://doi.org/10.1088/2053-1591/ab61aa
[14]
Natoli, C. (2020) An Introduction to Mixture Design, Statcoe-Report-11-2020.1871-1874.
[15]
Myers and Raymond, H. (2016) Response Surface Methodology; Process and Pro-duction Optimization Using Designed Experiments. 4th Edition, John Willey and Sons, Inc.
[16]
Bates, B.M. and Ancey, C. (2017) The Dam-Break Problem for Eroding Viscoplastic Fluids. JournalofNon-NewtonianFluidMechanics, 243, 64-78. https://doi.org/10.1016/j.jnnfm.2017.01.009
[17]
Basumatary, A.K., Kumar, R.V., Ghoshal, A.K. and Pugazhenthi, G. (2015) Synthesis and Characterization of MCM-41-Ceramic Composite Membrane for the Separation of Chromic Acid from Aqueous Solution. JournalofMembraneScience, 475, 521-532. https://doi.org/10.1016/j.memsci.2014.10.055
[18]
Sarkar, P., Ghimire, S., Vlasov, S. and Mukhopadhyay, K. (2023) Effect of Clay-Zwitterionic Interactions in Controlling the Viscoelastic Properties in Organomodified Clays. iScience, 26, Article ID: 108388. https://doi.org/10.1016/j.isci.2023.108388
[19]
Habib, B.A., Abdeltawab, N.F. and Salah Ad-Din, I. (2022) D-Optimal Mixture Design for Optimization of Topical Dapsone Niosomes: In Vitro Characterization and in Vivo Activity against Cutibacteriumacnes. DrugDelivery, 29, 821-836. https://doi.org/10.1080/10717544.2022.2048131
[20]
Das, D., Baitalik, S., Haldar, B., Saha, R. and Kayal, N. (2017) Preparation and Characterization of Macroporous Sic Ceramic Membrane for Treatment of Waste Water. JournalofPorousMaterials, 25, 1183-1193. https://doi.org/10.1007/s10934-017-0528-5
[21]
Jarrar, R., Abbas, M.K.G. and Al-Ejji, M. (2024) Environmental Remediation and the Efficacy of Ceramic Membranes in Wastewater Treatment—A Review. EmergentMaterials, 7, 1295-1327. https://doi.org/10.1007/s42247-024-00687-0