Abstract:A study on the catalytic properties of properly activated hydrotalcite (HT) with special attention to the nature and amount of active sites present in this solid base catalyst has been undertaken. Only a small fraction (5%) of the available basic sites in the rehydrated calcined HT is active in liquid-phase aldol condensations. These sites exhibit high catalytic activity and are most likely localized at the edges of the HT-platelets. Besides a high activity, these modified HTs also show a high selectivity. No … Show more
“…After heat treatment of HT as the surface area as well as the pore volume increased significantly. Only with HT heat micropores were observed, caused by the evolution of water and CO 2 during heat treatment of HT as [25,32,36,37]. After rehydration of the mixed oxide (HT re ) a BET surface area similar to that of HT as was found, whereas Pd/HT re exhibited a relatively low surface area.…”
Section: Catalyst Characterizationmentioning
confidence: 98%
“…To an aqueous solution (70 ml) containing 0. 35 To activate HT as [32,33] it was heated in a nitrogen flow to 723 K (10 K min À1 ) for 8 h and allowed to cool down to room temperature (HT heat ). HT heat was rehydrated by suspending it in decarbonated water under N 2 atmosphere for 1 h. Next, the sample was filtered under N 2 atmosphere and dried in N 2 flow at 293 K. The sample is further denoted as HT re .…”
Section: Preparation Of the Hydrotalcite Materialsmentioning
confidence: 99%
“…X-ray diffraction patterns of HT as , HT heat , HT re and 1 wt% Pd/HT re . [32,33,[37][38][39][40]. This low amount of accessible basic sites is best explained by further agglomeration of the HT platelets as could already be observed with activated HTs [33,37,38,41,42], induced by the additional heat treatment and rehydration procedure.…”
A comparative study was performed between Pd supported on activated hydrotalcites bi-functional catalysts and physical mixtures of activated hydrotalcites with Pd supported on carbon nanofibers for the single-stage liquid-phase synthesis of methyl isobutyl ketone from acetone and H 2 . Since it was found earlier that the dehydration reaction of diacetone alcohol over activated hydrotalcites is the rate-determining step in this process, Mg-Al hydrotalcites were investigated in the condensation of acetone to diacetone alcohol and its dehydration to mesityl oxide to enhance the activity. A correlation between the number of active base sites, as determined by volumetric CO 2 adsorption measurements at low pressures, and the activity in the dehydration reaction could be derived. A dependency on the Pd-loading (0-1 wt%) of Pd supported on activated hydrotalcites catalysts was found in the single-stage synthesis of methyl isobutyl ketone, whereas no such an effect was found when using physical mixtures of activated hydrotalcites with Pd on carbon nanofibers. Results from TEM, CO 2 chemisorption and N 2 physisorption as well as catalytic experiments in the hydrogenation of mesityl oxide and of cyclohexene indicate that this dependency is largely accounted for by entrapment of Pd particles in the agglomerates of the irregular stacks of hydrotalcite platelets, making these sites inaccessible for the reactants. #
“…After heat treatment of HT as the surface area as well as the pore volume increased significantly. Only with HT heat micropores were observed, caused by the evolution of water and CO 2 during heat treatment of HT as [25,32,36,37]. After rehydration of the mixed oxide (HT re ) a BET surface area similar to that of HT as was found, whereas Pd/HT re exhibited a relatively low surface area.…”
Section: Catalyst Characterizationmentioning
confidence: 98%
“…To an aqueous solution (70 ml) containing 0. 35 To activate HT as [32,33] it was heated in a nitrogen flow to 723 K (10 K min À1 ) for 8 h and allowed to cool down to room temperature (HT heat ). HT heat was rehydrated by suspending it in decarbonated water under N 2 atmosphere for 1 h. Next, the sample was filtered under N 2 atmosphere and dried in N 2 flow at 293 K. The sample is further denoted as HT re .…”
Section: Preparation Of the Hydrotalcite Materialsmentioning
confidence: 99%
“…X-ray diffraction patterns of HT as , HT heat , HT re and 1 wt% Pd/HT re . [32,33,[37][38][39][40]. This low amount of accessible basic sites is best explained by further agglomeration of the HT platelets as could already be observed with activated HTs [33,37,38,41,42], induced by the additional heat treatment and rehydration procedure.…”
A comparative study was performed between Pd supported on activated hydrotalcites bi-functional catalysts and physical mixtures of activated hydrotalcites with Pd supported on carbon nanofibers for the single-stage liquid-phase synthesis of methyl isobutyl ketone from acetone and H 2 . Since it was found earlier that the dehydration reaction of diacetone alcohol over activated hydrotalcites is the rate-determining step in this process, Mg-Al hydrotalcites were investigated in the condensation of acetone to diacetone alcohol and its dehydration to mesityl oxide to enhance the activity. A correlation between the number of active base sites, as determined by volumetric CO 2 adsorption measurements at low pressures, and the activity in the dehydration reaction could be derived. A dependency on the Pd-loading (0-1 wt%) of Pd supported on activated hydrotalcites catalysts was found in the single-stage synthesis of methyl isobutyl ketone, whereas no such an effect was found when using physical mixtures of activated hydrotalcites with Pd on carbon nanofibers. Results from TEM, CO 2 chemisorption and N 2 physisorption as well as catalytic experiments in the hydrogenation of mesityl oxide and of cyclohexene indicate that this dependency is largely accounted for by entrapment of Pd particles in the agglomerates of the irregular stacks of hydrotalcite platelets, making these sites inaccessible for the reactants. #
“…These similarities make rhodinol inseparable into individual geraniol and citronellol by normal distillation processes [10][11]. The oxidation product of rhodinol known as citral, has a wide range of valuable applications such as ingredient in fragrances and precursors for the synthesis of vitamin A, makes it highly demanded in the market [12][13]. Therefore, a chemical process which can selectively convert rhodinol to citral is desired.…”
Abstract. The oxidation method utilising H 2 O 2 -Pt black system was successfully adapted in the oxidation of rhodinol which is a mixture form of geraniol and citronellol. This green oxidation found to be selectively converted geraniol to citral using conventional method. The implementation of microwave irradiation (175 Watt, 90 0 C, 30 mins) and a higher molar of H 2 O 2 further improved the conversion rate (72.6%) and selectivity (81%) as compared to the conventional method.
“…In these studies, the actual condensation catalyst is a mixed oxide obtained by calcination of the hydrotalcite. Recently, extending the pioneering work of Tichit and co-workers [21][22][23][24] our group developed a highly active catalyst for the liquid-phase condensation of acetone at low temperatures, i.e., activated Mg-Al hydrotalcite (HT) [25,26]. Furthermore, this catalyst showed dehydration functionality of DAA to MO already at room temperature [2,26].…”
In this study, a catalyst mixture of activated Mg/Al hydrotalcite as solid base and Pd on carbon nanofibers was investigated for the single-stage liquid-phase synthesis of methyl isobutyl ketone (MIBK) from acetone and H 2 at 313 K and H 2 pressures of 1-20 bar. With this catalyst system acetone and H 2 are selectively converted into MIBK in a single reactor, even at 1.2 bar H 2 . Although the hydrogenation of one of the intermediates, mesityl oxide (MO), at 1.2 bar suffers from severe mass transfer limitations in H 2 , the catalytic activity in the single-stage synthesis is stable over several hours if the steady-state concentration of MO is kept low. Under the presented conditions the dehydration reaction of diacetone alcohol to MO is rate limiting in the production of MIBK.
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