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Processes and Catalysts

The following discussion of base metal catalyst regeneration uses the hydrocracking process and catalyst, specifically UOP HC Unibon, as an example. [Pg.224]

This chapter follows the organization used in the past. A summary of the electronic properties leads into reports of electrocyclic chemistry. Recent reports of studies of HDS processes and catalysts are then summarized. Thiophene ring substitution reactions, ring-forming reactions, the formation of ring-annelated derivatives, and the use of thiophene molecules as intermediates are then reported. Applications of thiophene and its derivatives in polymers and in other small molecules of interest are highlighted. Finally, the few examples of selenophenes and tellurophenes reported in the past year are noted. [Pg.77]

Catalytic hydrogenation is typically carried out in slurry reactors, where finely dispersed catalyst particles (<100 (tm) are immersed in a dispersion of gas and liquid. It has, however, been demonstrated that continuous operation is possible, either by using trickle bed [24] or monoHth technologies [37]. Elevated pressures and temperatures are needed to have a high enough reaction rate. On the other hand, too high a temperature impairs the selectivity of the desired product, as has been demonstrated by Kuusisto et al. [23]. An overview of some feasible processes and catalysts is shown in Table 8.1. [Pg.176]

In this study, we developed microchannel PrOx reactor to control CO outlet concentrations less than 10 ppm from methanol steam reformer for PEMFC applications. The reactor was developed based on our previous studies on methanol steam reformer [5] and the basic technologies on microchaimel reactor including design of microchaimel plate, fabrication process and catalyst coating method were applied to the present PrOx reactor. The fabricated PrOx reactor was tested and evaluated on its CO removal performance. [Pg.654]

Any short review is bound to be incomplete and the selection of successful processes and catalysts expresses only the opinion of the author. There is, however, no doubt about the magnitude of important developments of the last 40 years, with at least ten breakthrough accomplishments, and there is every indication that the trend of the last 40 years will continue. [Pg.75]

Consider the effect of every impurity or potential impurity in every feedstock, in the solvents in the ligand and in the catalyst. What harm, if any, will befall the product or catalyst if these impurities enter the process, and in particular, if they accumulate Is the product stable in both the reaction and separation system If byproducts form, what affect will they have on the process and catalyst life ... [Pg.36]

Conventional Processes and Catalysts for Hydrogen Generation and Their... [Pg.195]

Homogeneous catalysis is an area of chemistry where computational modeling can have a substantial impact [6-9], Reaction cycles are usually multistep complicated processes, and difficult to characterize experimentally [10-12], An efficient catalytic process should proceed fastly and smoothly and, precisely because of this, the involved intermediates are difficult to characterize, when possible at all. Computational chemistry can be the only way to access to a detailed knowledge of the reaction mechanism, which can be a fundamental piece of information in the optimization and design of new processes and catalysts. [Pg.3]

Abdul-Sada, A. K. Atkins, M. P. Elhs, B. et al. Process and catalysts for the alkylation of aromatic hydrocarbons. World Patent WO 95, 21806 (1995) Abdul-Sada, A. K. Ambler, P. W. Hodgson, P. K. G. et al. Ionic liquids of imidazobum habde for oligomerization or polymerization of olefins. World Patent WO 95, 21871 (1995) Bowlas, C. J. Bruce, D. W. Seddon, K. R. Liquid-crystalline ionic liquids, Chem. Commun., 1996, 1625-1626. [Pg.127]

Haensel and Haensel [2] describe the criticaUty of the role of catalyst characterization in process and catalyst development They conclude that catalyst characterization is the cornerstone for the science of catalysis and for industrial progress. They emphasize that the characterization must have a purpose and be targeted for understanding and solving a specific problem in order to achieve commercial success. [Pg.85]

Recent process and catalyst-related development in FCC. Appl Catal, 63, 197-258. [Pg.567]

Franklin, N.L., Pinchbeck, P.H., and Popper, F. (1958), A Statistical Approach to Catalyst Development. Part II. The Integration of Process and Catalyst Variables in the Vapour Phase Oxidation of Naphthalene, Trans. Instn. Chem. Engrs., 36, 259-369. [Pg.420]

Catalytic Cracking Processes and Catalysts for Increasing Propylene... [Pg.77]

CATALYTIC CRACKING PROCESSES AND CATALYSTS FOR INCREASING PROPYLENE PRODUCTION... [Pg.82]

I.F.P. (France) and Idemitsu Kosan (Japan), as a member of RAP AD (Research Association for Petroleum Alternative Development), are involved in process and catalysts development for alcohols synthesis. This paper details most of our recent results. [Pg.42]

A. Corma, S. Iborra, S. Miquel and J. Primo, in Process and catalysts for the selective production of esters offatty acids , EP, 1998. [Pg.92]

Evaluation of catalysts, kinetics of catalytic processes, and catalyst reactions in general. [Pg.104]

Forschner TC, Powell JB, Slaugh LH, Weider PR (2000) Process and catalysts for preparing 1,3-propanediol from methyl 3-hydroxypropionate. WO 2000/018712... [Pg.98]


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