Ransfer reaction of 2-buten-1-ol into n-butanol. As ratio of Sr/P became larger, the selectivity toward n-butanol was enhanced [48]. The the molar ratio of Sr/P became greater, the selectivity toward n-butanol was enhanced [48]. density of strong acid and base internet sites Lumiflavin Autophagy improved as the molar Sr/P ratio improved, and the density of sturdy acid and base web pages elevated because the molar Sr/P ratio increased, plus the base website density was a lot larger than the acid site density. Aldol condensation the base internet site density was significantly greater than the acid internet site density. Aldol condensation was was expedited by base catalysis; as a result, the Sr catalyst having a greater base web site density expedited by base catalysis; hence, the Sr catalyst having a larger base web site density reresulted inside a higher catalytic activity for the production of 1-butanol from ethanol. sulted inside a greater catalytic activity for the production of 1-butanol from ethanol. Catalysts consisting of Mg and Al have already been investigated as an efficient catalytic Catalysts consisting of Mg and Al have been investigated as an effective catalytic method for the selective conversion of Diethyl phthalate-d10 web ethanol to n-butanol. For instance, modified MgO method for 450 selective conversiontransform ethanol into n-butanol [49]. It was proposed catalyst in the C and 1 atm could of ethanol to n-butanol. For example, modified MgO catalyst at 450 and 1 the ethanoltransform ethanol into n-butanol [49]. It wasto the case that the mechanism of atm could conversion over the MgO catalyst is equivalent proposed that the mechanism of your ethanoloxide activates the C bond in -position for the case of fundamental zeolite: the basic metal conversion over the MgO catalyst is similar of ethanol of simple zeolite: the basic metalwith a further ethanol molecule through dehydration, resulting followed by its condensation oxide activates the C bond in -position of ethanol followed formation of n-butanol [50]. Other acid ase catalysts, e.g., Mg l mixed oxides, in the by its condensation with an additional ethanol molecule through dehydration, resulting in the formation of n-butanol [50]. conversion of ethanol to n-butanol [51]. It was shown that were investigated inside a one-pot Other acid ase catalysts, e.g., Mg l mixed oxides, had been investigated in a one-pot conversion ofratio of 3to n-butanol [51]. It was shown that a Mga Mg l mixed oxide having a Mg/Al ethanol led to 38 selectivity toward n-butanol Al an ethanol conversion of 35 at 350led to 38 selectivity catalyst characterization at mixed oxide using a Mg/Al ratio of three C below 1 atm. The toward n-butanol at an ethanol proved that of 35 at 350and below 1 atm. The catalyst characterization benefits outcomes conversion adjacent acid medium standard web sites (Al inserted in MgO lattice or proved that adjacent 3acid andpromote the formation of butanol, since the presence of Mg inserted in Al2 O lattice) medium basic web-sites (Al inserted in MgO lattice or Mg insertedsites is2O3 lattice) promote the formation of butanol, because the presence of both each in Al needed to kind the reaction intermediate species. The Mg l oxide having a internet sites is necessary to formto a more quickly formation of intermediates to n-butanol (i.e.,using a Mg/Al Mg/Al ratio of 3:1 led the reaction intermediate species. The Mg l oxide acetaldehyde ratio crotonaldehyde) than the Mg l oxide having a Mg/Al ratio of 1:1 [52]. This was and and of three:1 led to a more quickly formation of intermediates to n-butanol (i.e., acetaldehyde due crotonaldehyde) than the Mg l oxide using a the Mg l oxide (Mg.
