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It was observed that the apparent rate constants of the forward reactions increased linearly with increasing acid concentration.
For the three forward reactions: triglyceride to diglyceride, diglyceride to monoglyceride, and monoglyceride to glycerol, reaction rate constants are reported to be 9.3 × 10−7, 2.5 × 10−6, and 7.5 × 10−5 L/mol/s.
A three-site model predicted sorption rate constants for a pH 7.2 solution with a 75 150 μm granodiorite fraction to be 3.5, 0.012, and 0.012 mL/g-h for the forward reactions and 0.49, 0.0025, and 0.001 h− 1 for the reverse reactions.
The computations consider multi-component molecular transport and detailed chemical kinetics (19 species, 89 forward reactions) in the gas phase; semiempirically formulated vapor-liquid equilibrium with water vaporization/condensation at the liquid surface; and liquid species mass transfer and energy conservation in the liquid phase.
For the sake of the analysis, only the forward reactions are considered.
Furthermore, the rate constant of the forward reactions (k+0) is much larger than the rate constant of the reverse reactions (k-0).
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Forward reaction rate constants are calculated for the sub-reactions.
The forward reaction is first-order in butene.
Clofibric acid, ciprofibrate and fenofibrate showed pure non-competitive inhibition patterns in the forward reaction.
During this process, the dissolution of calcium naphthenate in the oil phase promotes the forward reaction.
The activation energy of the forward reaction was determined to 115.3 kJ/mol.
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