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Rate of Formation of Industrial Lubricant Additive Precursors from Maleic Anhydride and Polyisobutylene
[Image: see text] The Alder-ene reaction of neat polyisobutylene (PIB) and maleic anhydride (MAA) to produce the industrially important lubricant additive precursor polyisobutylene succinic anhydride (PIBSA) is studied at 150–180 °C. Under anaerobic conditions with [PIB] ∼ 1.24 M (550 g mol(–1) grad...
Autores principales: | , , , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
American Chemical Society
2022
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Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9486990/ https://www.ncbi.nlm.nih.gov/pubmed/36158466 http://dx.doi.org/10.1021/acs.oprd.2c00207 |
Sumario: | [Image: see text] The Alder-ene reaction of neat polyisobutylene (PIB) and maleic anhydride (MAA) to produce the industrially important lubricant additive precursor polyisobutylene succinic anhydride (PIBSA) is studied at 150–180 °C. Under anaerobic conditions with [PIB] ∼ 1.24 M (550 g mol(–1) grade, >80% exo alkene) and [MAA] ∼ 1.75 M, conversion of exo-PIB and MAA follows second-order near-equal rate laws with k(obs) up to 5 × 10(–5) M(–1) s(–1) for both components. The exo-alkene-derived primary product PIBSA-I is formed at an equivalent rate. The less reactive olefinic protons of exo-PIB also react with MAA to form isomeric PIBSA-II (k(obs) up to 6 × 10(–5) M(–1) s(–1)). Some exo-PIB is converted to endo-PIB (containing trisubstituted alkene) in a first-order process (k(obs) ∼ 1 × 10(–5) s(–1)), while PIBSA-I is difunctionalized by MAA to bis-PIBSAs very slowly. The MAA- and PIB-derived activation parameter ΔG(‡)(150 °C) 34.3 ± 0.3 kcal mol(–1) supports a concerted process, with that of PIBSA-I suggesting a late (product-like) transition state. |
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