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Daniels, reactor

The formation of propene oxide as a side product of the acrolein formation or dimerization reactions is reported by many authors. Daniel et al. [95,96] demonstrated that propene oxide is formed by surface-initiated homogeneous reactions which may involve peroxy radical intermediates. The epoxidation is increased by a large void fraction in the catalyst bed or a large postcatalytic volume. In view of these results, the findings of Centola et al. [84] are understandable, as the wall of the empty reactor may have been sufficiently active to initiate the reaction. [Pg.136]

Szpyrkowicz, L., M. Radaelli, and S. Daniele (2005). Electrocatalysis of chlorine evolution on different materials and its influence on the performance of an electrochemical reactor for indirect oxidation of poUutants. Catal. Today 100,425 429. [Pg.244]

Gas Separation by Adsorption Processes Ralph T. Hang Heterogeneous Reactor Design Hong H. Lee Molecular Thermodynamics of Nonideal Fluids Lloyd L. Lee Phase Equilibria in Chemical Engineering Stanley M. Walas Transport Processes in Chemically Reacting Flow Systems Daniel E. Rosner... [Pg.836]

Daniels and Lenney [32] give a detailed process description of a two-reactor CSTR system used to produce ethylene-vinyl acetate (EVA) copolymer latexes. A seed latex is fed to the first reactor. Korte and Silling [33] employed a tube-CSTR system for producing acrylonitrile-vinylacetate-acetate-styrene copolymers. The PFT generated the seed for the CSTR which was also fed with a stream which by-passed the tube. [Pg.566]

Corn fiber (Archer Daniels Midland, Co., Decatur, DL) was treated by three methods in a custom-made, jacketed, 50 gallon rotary reactor to hydrolyze the starch and hemicellulose fractions of the fiber. The reactor was equipped with a 0.55 MPa pop-off valve. All of the methods included initially hydrolyzing a 30%... [Pg.86]

Wigner, as research director at Clinton, assumed responsibility for the project. In this he was, unfortunately, not supported very well by the old timers (meaning those of us who had already been there for a couple of years) we could not understand how uranium at 100 per gram (1946 ) could ever be an economical fuel and besides, we were too involved with the MTR. Perhaps this lack of support was an important reason why the Daniels pile was never built, although many similar reactors have since been operated successfully. [Pg.13]

At Clinton two main projects were being pursued - the high-flux reactor (which culminated in the Materials Testing Reactor, MTR) and the Daniels Power Pile. In addition. Captain Rickover and his energetic navy aides came to learn nuclear energy, and to develop what became the Nautilus. [Pg.17]

The Power Pile referred to in this memorandum is the helium-cooled, BeO-moderated, high-temperature reactor of Professor Farrington Daniels. [Pg.242]

Daniel Hyman, Mixing and Agitation John Beck, Design of Packed Catalytic Reactors Douglass J. Wilde, Optimization Methods... [Pg.317]

In a plasma reactor fed with a gas mixture several different processes are at work, as summarized in the scheme of fig.l for the argon/methane system (Riccardi, 2001). In a cold plasma the characteristic discharge chemistry processes are mainly driven by free electrons which are by far the most energetic particles in the reactor, and include (Me Daniel, 1993) ... [Pg.170]

P. A. Lovell, T. H. Shah, and F. Heatley, in E. S. Daniels, E. D. Sudol, and M. El Asser, eds., Correlationof the extent of chain branching with reactor conditions for emulsion polymerization of n-butyl acrylate ACS Symposium Series, k Polymer Latexes-Preparation, Characterization and Applications, Vol. 492 ACS Washington, D.C., 1992, pp. 188-202... [Pg.1273]

Daniels, T.C. and Al-Jumaily, F.K. (1975). Investigations of the factors affecting the performance of a rotating heat pipe. Int. J. Heat and Mass Transfer, Vol. 18, pp. 961-973. Goebel, P. (1977). Polymerisation reactor with gilled-tube radiator and axial agitator. US Patent 4029143, 14 June. [Pg.20]


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See also in sourсe #XX -- [ Pg.2 ]




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