<?xml version="1.0" encoding="UTF-8"?><?xml-stylesheet type="text/xsl" href="static/style.xsl"?><OAI-PMH xmlns="http://www.openarchives.org/OAI/2.0/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/ http://www.openarchives.org/OAI/2.0/OAI-PMH.xsd"><responseDate>2026-09-19T00:12:52Z</responseDate><request verb="GetRecord" identifier="oai:openscholar.dut.ac.za:10321/6212" metadataPrefix="oai_dc">https://openscholar.dut.ac.za/server/oai/request</request><GetRecord><record><header><identifier>oai:openscholar.dut.ac.za:10321/6212</identifier><datestamp>2025-09-05T01:00:47Z</datestamp><setSpec>com_10321_9</setSpec><setSpec>col_10321_10</setSpec></header><metadata><oai_dc:dc xmlns:oai_dc="http://www.openarchives.org/OAI/2.0/oai_dc/" xmlns:dc="http://purl.org/dc/elements/1.1/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xmlns:doc="http://www.lyncode.com/xoai" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/oai_dc/ http://www.openarchives.org/OAI/2.0/oai_dc.xsd">
   <dc:title>Application of chitosan-carbon nanotube hydrogel beads composite in the removal of antibiotic compounds and perfluoroalkyl substances from aqueous solution</dc:title>
   <dc:creator>Khumalo, Siphesihle Mangena</dc:creator>
   <dc:contributor>Rathilal, Sudesh</dc:contributor>
   <dc:contributor>Bakare, Babatunde Femi</dc:contributor>
   <dc:subject>Antibiotic compounds</dc:subject>
   <dc:subject>Adsorption</dc:subject>
   <dc:subject>Chitosan-carbon nanotube</dc:subject>
   <dc:subject>Hydrogel beads</dc:subject>
   <dc:subject>Sewage--Purification--Adsorption</dc:subject>
   <dc:subject>Sewage disposal plants</dc:subject>
   <dc:subject>Chitosan</dc:subject>
   <dc:subject>Nanogels</dc:subject>
   <dc:description>This thesis is submitted for the fulfilment of academic requirements for the degree of Doctor of Engineering: Chemical Engineering, Durban University of Technology, Durban, South Africa, 2025.</dc:description>
   <dc:description>The environmental occurrence of antibiotics and perfluoroalkyl acids (PFAAs), particularly in portable 
water sources, is very evident that current wastewater treatment plants cannot completely eradicate 
these emerging contaminants of environmental concern. On the other hand, long term exposure to these 
contaminants poses serious health risks to human and aquatic life. Available literature suggests that 
antibiotics and PFAAs can be eradicated by solid-liquid adsorption. Therefore, there is an urgent need 
to develop environmentally green and cost-effective adsorbents for the remediation of antibiotics and 
PFAAs. 
As such, the present study focuses on investigating the treatment efficiency of chitosan-carbon nanotube 
(CCNT) hydrogel beads for the removal of antibiotics viz. amoxicillin (AMX), ciprofloxacin (CIP), and 
sulfamethoxazole (SMX) as well as PFAAs i.e., perfluorooctanoic acid (PFOA) and perfluorooctane 
sulfonic acid (PFOS) from synthetic aqueous solutions. The scope of the present work includes 
elucidating the adsorption kinetics, isotherms, thermodynamic parameters as well as breakthrough 
curves for the uptake of AMX, CIP, SMX, PFOS and PFOS on CCNT hydrogel beads. Moreover, Monte 
Carlo simulations were performed to elucidate the interaction of PFOA, PFOS and sulfamethazine 
(SMT) with polyethylene (PE) and polypropylene (PP) relative to water. 
Herein, CCNT hydrogel beads were synthesised using a two-step precipitation approach and analysed 
using Fourier transformation infrared (FTIR) technology. From the FTIR results it was evident that the 
synthesised model adsorbent was characterised with strong peaks of carboxylic and hydroxyl functional 
groups which were essential for the uptake of the model adsorbates i.e., AMX, CIP, SMX, PFOA and 
PFOS. Post the adsorption process, band stretches were observed cementing the uptake of the model 
adsorbates on CCNT hydrogel beads. Single adsorption kinetics experimental data for the uptake of 
AMX, CIP, SMX, PFOA and PFOS were well fitted by the nonlinear pseudo-first order (PFO) kinetic 
model recording R2 values of more than 0.9 for all model adsorbates. It is worth noting that the 
competing PFO and pseudo-second order (PSO) kinetic models were validated by applying the 
Bayesian Information Criterion (BIC) as a statistical analysis parameter. Furthermore, the findings of 
the present study from the Weber-Morris kinetic model suggest that multiple processes were limiting 
the overall adsorption rate of AMX, CIP, SMX, PFOA and PFOS on CCNT hydrogel beads. 
Adsorption isotherm studies were conducted for a temperature range of 283 K, 293 K and 303 K for a 
contact time of 24 hours for AMX, CIP, and SMX, and 168 hours for PFOA and PFOS. The findings of 
the present study suggest that AMX, CIP, SMX, PFOA and PFOS single adsorption experimental data 
were well fitted by the nonlinear Freundlich isotherm model suggesting the heterogeneity of the surface 
as well as the exponential distribution of the active sites of the model adsorbent. On the other hand, the 
binary and ternary AMX, CIP, and SMX adsorption experimental data were well fitted by the nonlinear 
competitive extended Sips adsorption isotherm model. Furthermore, results for the binary and ternary 
adsorption systems explicitly demonstrated that the multicomponent adsorption systems exhibited both 
antagonistic and synergistic effects on the uptake of AMX, CIP and SMX. Interestingly, binary 
adsorption experimental data for PFOA and PFOS were well fitted by the extended-Langmuir isotherm 
model (R2=0.996 for PFOA and R2=0.995 for PFOS) and extended-Sips isotherm model (R2=0.996 for 
PFOA and R2=0.997 for PFOS), with the system strictly exhibiting antagonistic effects for the uptake 
of one adsorbate in the presence of another adsorbate. From thermodynamic studies, it is evident that 
the uptake of AMX, CIP, SMX, PFOA and PFOS is an endothermic process, and it cannot be explicitly 
classified as a chemical nor physical adsorption process but as a physicochemical adsorption process. 
The presence of sodium chloride (NaCl) and humic acid (HA) demonstrated antagonistic effects on the 
uptake of AMX, CIP and SMX by CCNT hydrogel beads due to formation of aggregates with an 
increase in ionic strength. Single factor analysis of variance results recorded p-values of less than 0.05 
for the uptake of AMX, CIP and SMX indicating that there was a statistical difference between the 
means of the independent and depended variables, thus cementing the negative effect of increasing ionic 
strength on the uptake of the mode adsorbates. However, NaCl ions exhibited minimal competitive 
effects with adsorbate molecules for active adsorption sites on CCNT hydrogel beads compared to HA.
On the other hand, the presence of NaCl as a competing ion exhibited synergistic effects in the uptake 
of PFOA and PFOS from aqueous solutions. 
Furthermore, for the present work, breakthrough curves from the experimental data were well fitted by 
the Thomas model recording R2
and adjusted-R
2 values of greater than 0.9 for all adsorbates investigated 
indicating that the breakthrough curves for the present work can be described by a symmetrical function. 
Additionally, the breakthrough points time predicted by the Thomas model was aligned with the 
experimentally determined breakthrough points time cementing its practical utility and superiority over 
the log-Gompertz and Bohart-Adams models. On the other hand, from the Monte Carlo simulation 
results, it is evident that, in an aqueous environment, both PFOA and PFOS may be taken up 
preferentially by PP and PE, although less strongly by PE. The degree of polymerisation of PE and PP 
did not significantly influence the observed behaviour. In terms of sorption affinity, the observed affinity 
was PFOA>PFOS>SMT which was consistent for both PE and PP. 
Based on the results obtained, it was concluded that CCNT hydrogel beads composites have the 
potential to be applied as adsorbents for the removal of antibiotics and PFAAs from aqueous solutions. 
Furthermore, the simulation results obtained suggest that Monte Carlo simulations in Material Studio 
can be used as an effective tool in elucidating the interaction between antibiotics and PFAAs with 
microplastics relative to water as co-existing contaminants. Therefore, the findings of the present work 
have successfully addressed the research questions for the current study</dc:description>
   <dc:description>D</dc:description>
   <dc:date>2025-09-04T13:27:11Z</dc:date>
   <dc:date>2025-09-04T13:27:11Z</dc:date>
   <dc:date>2024</dc:date>
   <dc:type>Thesis</dc:type>
   <dc:identifier>https://hdl.handle.net/10321/6212</dc:identifier>
   <dc:identifier>https://doi.org/10.51415/10321/6212</dc:identifier>
   <dc:language>en</dc:language>
   <dc:format>241 p</dc:format>
   <dc:format>application/pdf</dc:format>
</oai_dc:dc></metadata></record></GetRecord></OAI-PMH>