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    Cheracterisation of Battery Materials Using Surface Science Techniques
    (The University of Manchester, 2025) Alsaedi, Abdulrhman; Lockyer, Nicholas; Walton, Alex
    LiNixMnyCozO2 (NMC) layered oxide cathodes are commonly used in lithium-ion batteries (LIBs) for their high capacity and energy density, particularly with increased nickel content. However, nickel-rich NMC cathodes exhibit severe interaction with electrolyte that leads to formation of cathode electrolyte interphase (CEI) and rapid capacity fade. Comparably, the graphite anode, commonly used for its high capacity and stability, forms a solid electrolyte interphase (SEI) during cycling. These passivation layers act as protective barriers but are not ideal, which undergo dissolution, breakage, and repair throughout cycling, impacting battery performance. The further deployment of the LIBs requires a deeper understanding of the dynamic chemical process occurring on the electrode surface. This thesis employed Secondary Ion Mass Spectrometry (SIMS) and Hard X-ray Photoelectron Spectroscopy (HAXPES) to investigate the surface and subsurface of materials related to NMC cathode. In this context, in Chapter 4, we examine the effect of C60, Arn, (CO2)n and (H2O)n primary ion beams on MnO, MnO2, Co3O4 and NiO metal oxides. Results indicate that gas cluster ion beams (GCIBs) containing CO2 and H2O enhance metal oxide and metal hydroxide secondary ions yields compared to those with Ar only, providing insights into ion-beam interactions. In Chapter 5, we explore the application of HAXPES for analyzing the 1s orbital of first row transition metals (FRTMs) in cobalt, manganese and nickel compounds. By measuring the separation between transition metal (TM) satellite-main peaks and TM satellite-O 1peaks, we develop a reliable approach to differentiate oxidation states, providing a precise determination for each metal oxide. Chapter 6 compares the CEI layer across various cycling states for NMC111, NMC532 and NMC811 cathodes. The results reveal that the CEI begins forming in the not-charged (N.C.) and thickens in the single-charged (S.C.) state, with thickness increasing with nickel content. A detailed analysis of the CEI on the NMC111 electrode across N.C., S.C., single-charge-discharged (S.C.D.) and end-of-life (E.O.L.) states show that the CEI layer reaches its maximum thickness in the S.C. state before decreasing in subsequent states. SIMS analysis indicates that the CEI layer comprises a dual-layer structure. Additionally, the SEI layer on the graphite anode shows that electrolyte degradation starts in the N.C. state, peak in the S.C. state, and then decreases during subsequent cycles. Collectively, the work reported in this thesis demonstrates improved understanding of the methodology of electrode characterization using SIMS and HAXPES and through their application, the dynamic chemical processes occurring at LIB electrodes.
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    Selective dehydroisomerisation of cyclic monoterpenes to p-cymene over bifunctional metal-acid catalysts
    (Saudi Digital Library, 2023-10-02) Alsharif, Aliyah; Kozhevnikov, Ivan
    The dehydroisomerisation of α-pinene and limonene, naturally occurring abundant monoterpenes, is a clean sustainable route to produce p-cymene, an important intermediate in organic synthesis and ingredient in cosmetics and medicinal products. Currently, p-cymene is produced in a mixture with o- and m-isomers by the Friedel-Crafts alkylation of toluene with propene, followed by isomer separation, with an adverse effect on the environment. The aim of this work is to study the dehydroisomerisation of cyclic monoterpenes, such as α-pinene, β-pinene, limonene, α-terpinene, γ-terpinene and terpinolene, in the gas phase using silica-supported ZnO and CdO as new bifunctional metal-acid catalysts. It is demonstrated that all these monoterpenes can be converted to p-cymene with excellent yields of 90–100% using ZnO/SiO2 and CdO/SiO2 as the catalysts. The catalysts were prepared by wet impregnation of silica with metal nitrates from an aqueous solution followed by drying and calcination at 400–500 oC and characterised by BET, TGA, XRD, DRIFTS, H2-TPR and ICP-OES. The dehydroisomerisation reactions were carried out in a continuous flow fixed-bed microreactor with online GC analysis. It was found that dehydroisomerisation of α-pinene over ZnO/SiO2 produces p-cymene with 90% yield at 100% conversion at 370 oC and WHSV = 0.020 h-1. The reaction with limonene gives a 100% p-cymene yield at 325 oC and WHSV = 0.080 h-1. ZnO/SiO2 catalyst shows stable performance for over 70 h without co-feeding hydrogen to the reactor. The reaction over silica-supported ZnO catalysts with β-pinene produces a 100% p-cymene yield at 400 oC and WHSV = 0.080 h-1. The reaction with monocyclic terpenes such as limonene, α-terpinene, γ-terpinene and terpinolene gives a 100% p-cymene yield at 300–325 oC and WHSV = 0.16–0.08 h-1. The dehydroisomerisation of bicyclic monoterpenes, such as α-pinene and β-pinene, over CdO/SiO2 gives 91–95% p-cymene yields at 325–375 oC and WHSV = 0.010–0.020 h-1, whereas the more reactive monocyclic terpenes, such as limonene, α-terpinene, γ-terpinene, and terpinolene, give a 100% yield at 200–250 oC and WHSV = 0.040–0.080 h-1. This catalyst shows stable performance for over 25 h without co-feeding hydrogen. To the best of our knowledge, CdO/SiO2 has the highest efficiency in monoterpene-to-p-cymene dehydroisomerisation among the catalysts reported to date. The proposed mechanism of monoterpene dehydroisomerisation to p-cymene on bifunctional ZnO/SiO2 and CdO/SiO2 catalysts involves two steps: fast isomerisation of monoterpene reactant on Brønsted acid sites (silanol groups of silica support) to form p-menthadiene intermediates followed by their slow dehydrogenation on oxo-metal sites to p-cymene. The dehydrogenation is suggested to proceed through the abstraction of allylic hydrogen from the substrate by an oxo-metal site followed by the elimination of another hydrogen atom to form p-cymene π-bonded to metal ion (Zn(II) or Cd(II)). Then, the elimination of the p-cymene molecule and H2 closes the catalytic cycle.
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