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Acid-Base Catalysis of the Elimination and Isomerization Reactions of Triose Phosphates

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Abstract

The nonenzymatic β-elimination, isomerization, and racemization reactions of L-glyceraldehyde 3-phosphate (LGAP) are through a common enediolate intermediate which partitions between leaving group expulsion, C-1 protonation, and C-2 protonation, respectively. The elimination reaction mechanisms of LGAP and dihydroxyacetone phosphate (DHAP) are Elcb because enolate intermediates have been identified in very closely related systems.13,14 Strong general base catalysis of elimination demonstrates that the enediolate intermediate is formed essentially irreversibly by rate-determining substrate deprotonation. The pH rate profile for the elimination reaction of LGAP is first order in hydroxide at pH >10 due to direct substrate deprotonation by hydroxide, pH independent at pH 6–10 due to intramolecular deprotonation by the C-3 phosphate dianion, and first order in hydroxide at pH <6 due to a decrease in the reactive phosphate dianion form of the substrate. The Brønsted ² values for buffer catalysis of DHAP and LGAP elimination by 3-substituted quinuclidines are 0.48 and 0.45, respectively. The solvent deuterium isotope effect on the second-order rate constant for quinuclidinone catalysis of DHAP elimination is 1.1. At π.2 M concentrations of 3-oxo- and 3-hydroxy-substituted quinuclidine buffers there is curvature in the buffer catalysis plots for the elimination reaction of DHAP which is attributed to a change from rate determining substrate deprotonation to partially rate determining leaving group expulsion. The isomerization and racemization reactions of LGAP were followed by coupling the formation of DHAP and DGAP to enzymatic NADH oxidation under conditions where >90% of the product is from the elimination reaction. Uncatalyzed racemization is five times slower than uncatalyzed isomerization, and buffer-catalyzed racemization is estimated to be <20 times slower than buffer-catalyzed isomerization. The observed rate constant for LGAP isomerization is second order in total buffer concentration; the basic form of the buffer acts to increase the steady-state concentration of the enediolate, and the acidic form of the buffer increases the fractional partitioning of the enediolate to DHAP. Rate constant ratios kBH/ke and k−0/ke for partitioning of the enediolate between buffer-catalyzed or uncatalyzed protonation (kBH or k−0) and leaving group expulsion (ke) were obtained from the slopes and the intercepts respectively of linear plots of the isomerization/elimination rate constant ratio against buffer concentration. The Bronsted α value for enediolate protonation at C-l is 0.47. The (kBH/ke)H2O/(kBD/ke)D2O ratio for quinuclidinonium catalysis in H2O and D2O is 3.2. The pH dependence plot of kBH/ke values shows pH-independent regions at pH <7 and >10, with a 100-fold greater limiting kBH/ke value at pH >10. The increased kBH/ke value at high pH is due to slower leaving group expulsion from the enediolate phosphate dianion compared to that of the enediolate phosphate monoanion. The nonenzymatic reactions of triose phosphates are compared with the enzymatic reactions catalyzed by triose phosphate isomerase and methylglyoxal synthase.

Original languageEnglish
Pages (from-to)4926-4936
Number of pages11
JournalJournal of the American Chemical Society
Volume106
Issue number17
DOIs
StatePublished - Aug 1 1984

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