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Equilibrium catalysts

These effects of the reaction parameters were interpreted in terms of a catalyst equilibrium series, as shown in Eq. (28). [Pg.23]

With a suitable catalyst, equilibrium pressures can be measured for this dissociation. [Pg.281]

AlCls catalyst, equilibrium reached in less than 15-20 hours analysis by mass spectrometry (313). [Pg.220]

Haber demonstrated that the production of ammonia from the elements was feasible in the laboratory, but it was up to Carl Bosch, a chemist and engineer at BASF, to transform the process into large-scale production. The industrial converter that Bosch and his coworkers created was completely revised, including a cheaper and more effective catalyst based on extensive studies in high-pressure catalytic reactions. This approach led to Bosch receiving the Nobel Prize in chemistry in 1931, and the production of multimillion tons of fertilizer per year worldwide, see also Agricultural Chemistry Catalysis and Catalysts Equilibrium Le Chatelier, Henri Nernst, Walther Hermann Ostwald, Friedrich Wilhelm. [Pg.183]

Decomposition Reactions. Minute traces of acetic anhydride are formed when very dry acetic acid is distilled. Without a catalyst, equilibrium is reached after about 7 h of boiling, but a trace of acid catalyst produces equilibrium in 20 min. At equilibrium, about 4.2 mmol ot anhydride is present per liter of acetic acid, even at temperatures as low as 80°C (17). Thermolysis of acetic acid occurs at 442°C and 101.3 kPa (1 atm), leading by parallel pathways to methane [72-82-8] and carbon dioxide [124-38-9], and to ketene [463-51-4] and water (18). Both reactions have great industrial significance. [Pg.66]

Apart from these two complications, the formalism developed in Chapter 6 for noncatalytic reactions remains applicable as far as rate equations are concerned, but must be combined with modeling of the catalyst equilibria Where rate equations of transition-metal catalysis appeared in examples in earlier chapters, the quantity CMt is the concentration of the free catalyst and may have to be supplied by a catalyst equilibrium model. [Pg.206]

In a catalyzed reaction, both the forward rate and the backward rate are increased, but the Ktq (in this case 1000) remains unchanged. If the catalyst increases both the forward and reverse rates by a factor of 100, then the forward rate becomes 100,000 and the reverse rate becomes 100. Because of the dramatic increase in the rate of the forward reaction made possible by the catalyst, equilibrium is approached in seconds or minutes instead of hours or days. [Pg.166]

At room temperature in the absence of a catalyst, equilibrium is established extremely slowly. The strong acids that are used as catialysts in ordinary esterification serve equally well for alcoholysis. The most commonly used catalysts for alcoholysis, however, are the sodium alkoxides. They must be used in anhydrous sy ms since they are hydrolyzed by wafer and the resulting hydroxides hydrolyze the esters. The usual practice is to dissolve a small amount of sodium in the alcohol to be used... [Pg.711]

From an equilibrium point of view all oxygen is reacted, but due to the presence of a catalyst, equilibrium is also established in the steam reforming and shift reactions ... [Pg.46]

Figure 5.10 Decomposition of methane on supported nickel catalysts. Equilibrium constants for Ni/Si02 and Ni,Cu/Si02 catalysts from TGA measurements. The copper content of the catalyst does not affect the equilibrium constant. Bernardo et al. [49]. Reproduced with the permission of Elsevier. Figure 5.10 Decomposition of methane on supported nickel catalysts. Equilibrium constants for Ni/Si02 and Ni,Cu/Si02 catalysts from TGA measurements. The copper content of the catalyst does not affect the equilibrium constant. Bernardo et al. [49]. Reproduced with the permission of Elsevier.
The preparation procedure of the nickel supported catalysts (equilibrium adsorption in Ni(N03)2 aqueous solution, optimised washing step, activation conditions) in combination with a strong interaction between the nickel and the support [12] lead to a uniform distribution of the active component. One important precondition for the determination of effective diffusivities from reaction rate measurements is fulfilled. [Pg.461]

With the WClg—EtOH—AlEtCl2 system as catalyst, equilibrium is quickly obtained using a W A1 ratio of 1 4 and W olefin ratio of 1 10000. Neither constituent of this mixture catalyses metathesis alone. The same observation has also been made with the other systems, which are generally less reactive but more stable. [Pg.236]

Available to heat catalyst (neglecting losses) = 54,300 Btu (Catalyst equilibrium) circulation i/ 993(illo. 925)0 25 ... [Pg.793]


See other pages where Equilibrium catalysts is mentioned: [Pg.181]    [Pg.158]    [Pg.295]    [Pg.220]    [Pg.468]    [Pg.220]    [Pg.354]    [Pg.358]    [Pg.81]    [Pg.488]   
See also in sourсe #XX -- [ Pg.102 ]

See also in sourсe #XX -- [ Pg.71 ]

See also in sourсe #XX -- [ Pg.71 ]

See also in sourсe #XX -- [ Pg.405 ]




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