Marta Bausach

TL;DR: In this paper, Zeolite NaA membranes were synthesized on the inner side of porous titania (rutile) asymmetric tubular supports in a flow system where the synthesis gel was circulated through the support with flow rates in the range 1.5-4mLmin−1 by the action of gravity.

TL;DR: In this paper, the kinetics of the noncatalytic solid-gas reaction between Ca(OH)2 and SO2 at low temperature and in the presence of water vapor were investigated.

TL;DR: In this article, the effect of NO2 on the desulfurization reaction of simulated flue gas by Ca(OH)2 was investigated in a fixed-bed reactor at 333−353 K and at relative humidities (RHs) in the range of 30%−70%.

TL;DR: In this article, the selectivity and kinetics of liquid-phase addition of 2-propanol to isobutene to give isopropyl tert-butyl ether (IPTBE) were investigated in a batch reactor over the commercial oversulfonated ion-exchange Amberlyst-35 resin in the temperature range 60-90°C and 1.6-MPa for 2-Propanol/isobutenes initial ratios ranging from 0.5 to 3.0.

TL;DR: In this paper, a reaction mechanism consistent with the experimental observations and with its kinetic implications is discussed, and a new accessible Ca(OH)2 surface for further reaction with SO2, which might account for the general observation reported in the literature that water vapor exerts a substantial influence on the ability of commercial hydrated lime to retain SO2 in flue gas desulfurization (FGD) technologies.