The role of metal catalysts on the curing characteristics of bisphenol A‐based cyanate ester resin systems was investigated using Fourier transform infrared spectroscopy, differential scanning calorimetry, and rheological measurements. Bisphenol A dicyanate was cured with the octoates and naphthenates of zinc and manganese and with cobalt acetylacetonate at concentrations ranging from 0 to 750 ppm metal. Nonylphenol at concentrations between 0 and 8 phr was used as the cocatalyst. The results show that at metal catalyst concentrations less than 100 ppm and nonylphenol concentrations less than 4 phr, a maximum glass transition temperature of 250 to 260°C is obtained, irrespective of the type of catalyst used. For samples cured without nonylphenol, the maximum Tg was 298 to 302°C. At high catalyst concentrations, the Tg decreases with increasing catalyst concentration for the zinc catalysts, whereas no concentration effect was observed for samples cured with either manganese or cobalt. Nonylphenol was effective as a cocatalyst in achieving high conversions; however, the Tg at full conversion was found to decrease with increasing nonylphenol levels.

The kinetics of cyclotrimerization and the thermal stability of bisphenol Abased cyanate ester resin systems were determined using Fourier transform infrared spectroscopy, differential scanning calorimetry, and thermogravimetry. The bisphenol A dicyanate was cured with 4 phr nonylphenol and with the octoates of zinc and manganese, and cobalt acetylacetonate at concentrations ranging from 0 to 750 ppm metal. An empirical rate law was used to predict the cyanate concentration profiles. The observed reaction rate showed a first‐order dependenće on the initial metal concentration and a second‐order dependence on the cyanate concentration in the kinetically controlled regime. For the uncatalyzed systems, the kinetics was described by a second‐order autocatalytic model. The thermal stability of the network was found to be dependent on the catalyst concentration for the zinc catalysts. For the samples cured with manganese, no effect of concentration on the thermal stability was observed.

The adsorption of benzene and dibenzothiophene by hydrodesulfurization catalysts in oxidic and sulfided states has been measured. The equilibrium isotherms were Langmurian, with the adsorption capacity depending on the size of the adsorbate molecule and determined by the area of the adsorbing surface. Sulfidation created an increase in the adsorbing area and in the adsorption capacity. It also caused a strengthening of the adsorption bond involving the heteroatom and inhibition of bonds involving the benzene ring. The kinetics were in agreement with a model based on activated surface diffusion in the pores. The energy of activation for diffusion was related to the strength of the adsorption bond when the adsorbate was taken up from the gaseous phase. The adsorption of dibenzothiophene from the liquid phase was too slow to be measurable when the catalyst was in an oxidic state but proceeded at a measurable rate on the sulfided catalyst.