Ammonia acid strength

If, for a given acid, we wish to increase the acid strength, then we choose a solvent which has a greater affinity for protons than has water. If we add ammonia to a solution of hydrogen chloride in water, the essential equilibrium is... 

XL30). Mossbauer spectroscopy (KFKIj was applied to follow the state of Fe species in the zeolites. Carbon monoxide and ammonia adsorption (monitored with FTIR) (EQUINOX 55) was used to determine the nature, concentration and acid strength of the active sites in the Fe-TON zeolites. 

All acid sites were first neutralized with ammonia and ammonia was then desorbed at 277°C (550K) for 30 min. The ratio A55o/Ao, where A550 and Ao are the intensities of NH4+band (at 1450 cm 1) after and before desorption, represents a fraction of NH4+ ions which survived the desorption and was taken as a measure of the acid strength. For the... 

Because of the base strength of liquid ammonia, acids that are weak in water ionize completely in liquid ammonia. 

Another thermal analysis method available for catalyst characterization is microcalorimetiy, which is based on the measurement of the heat generated or consumed when a gas adsorbs and reacts on the surface of a solid [66-68], This information can be used, for instance, to determine the relative stability among different phases of a solid [69], Microcalorimetiy is also applicable in the measurement of the strengths and distribution of acidic or basic sites as well as for the characterization of metal-based catalysts [66-68], For instance, Figure 1.10 presents microcalorimetry data for ammonia adsorption on H-ZSM-5 and H-mordenite zeolites [70], clearly illustrating the differences in both acid strength (indicated by the different initial adsorption heats) and total number of acidic sites (measured by the total ammonia uptake) between the two catalysts. 

Ammonia TPD is very simple and versatile. The use of propylamine as a probe molecule is starting to gain some popularity since it decomposes at the acid site to form ammonia and propene directly. This eliminates issues with surface adsorption observed with ammonia. The conversion of the TPD data into acid strength distribution can be influenced by the heating rate and can be subjective based on the selection of desorption temperatures for categorizing acid strength. Since basic molecules can adsorb on both Bronsted and Lewis acid sites, the TPD data may not necessarily be relevant for the specific catalytic reaction of interest because of the inability to distinguish between Bronsted and Lewis acid sites. 

In the case of alkenes, 1-pentene reactions were studied over a catalyst with FAU framework (Si/Al2 = 5, ultrastable Y zeoHte in H-form USHY) in order to establish the relation between acid strength and selectivity [25]. Both fresh and selectively poisoned catalysts were used for the reactivity studies and later characterized by ammonia temperature programmed desorption (TPD). It was determined that for alkene reactions, cracking and hydride transfer required the strongest acidity. Skeletal isomerization required moderate acidity, whereas double-bond isomerization required weak acidity. Also an apparent correlation was established between the molecular weight of the hard coke and the strength of the acid sites that led to coking. 

It is known that the activation temperature can influence the acid strength distribution. For example, measurements of the differential heats of ammonia adsorbed at 150°C for a HY zeolite have led to the conclusion that stronger acid sites, in the 150-180 kJ/mol range, are formed upon increasing the activation temperature from 300 to 650°C. Dehydroxylation at high temperature resulted in the formation of strong Lewis acid sites and the disappearance of intermediate and weak Brpnsted sites [62]. 

Acidic properties of zeolite L were observed to correlate well with its structural disorders. The Si-MAS-NMR spectrum of zeolite L having a Si/AI ratio different from 3 revealed that Al distribution deviated from the ideal and suggested the presence of six different boat-shaped 8-ring patterns. Differential molar heats of adsorption of ammonia changed step-wise with the adsorbed amount, which reflects the difference in the acid strength of protons located in structurally different 8-rings. 

In this study, we analyze this situation using Si-MAS-NMR spectroscopy and high-temperature ammonia-adsorption calorimetry. The acid strength will be determined from the heat of adsorption of ammonia. On adsorption of ammonia, the reaction. 

The conjugate acid of a weak base has acid strength. Ammonia is a weak base, so the ammonium ion behaves as an acid in water. Therefore, a solution of ammonium chloride will be acidic. 

Acidity and acid strength distribution were evaluated by temperature-programmed desorption of ammonia. The acid sites were classified as weak < 300°C, medium (M) 300 < T < 450° 0 and strong (S) 450 < T < 550° 0. Ultra strong acid sites (S in a. u ) are defined as a ratio of peak height for catalyst to alumina (Ni cat./AfjOj) at 550° C,... 

The distribution of surface acidity strength has been studied by measuring the differential adsorption heat of ammonia. The differential scanning calorimetry (Setaram DSC 111) and the FTIR spectrophotometry (Nicolet 740) have been simultaneously used in order to measure the heat associated with the neutralization of the acidic sites and the amount of chemisorbed base, respectively. Once the sample is saturated at 250 °C and the total acidity measurement is obtained as the amount of base used in the titration, the measurement of the total acidity has been verified by desorption of the base at programmed temperature (TPD). A ramp of 5 °C/min between 250 °C and 500 °C has been followed, with a He flow of 20 cm3/min and using the FTIR spectrophotometry for the measurement of the desorption products. 

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