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Catalytic production

Shaped products used for adsorbent purposes are generally less sophisticated and therefore less expensive than catalytic products. In 1985, it was reported that 10,000 t/yr of activated alumina adsorbents were produced in the United States. North American producers of Bayer process-based activated aluminas include Alcoa, La Roche (formerly Kaiser Chemicals), Discovery, and Alcan. Gel-based activated aluminas are produced by La Roche, Vista, and several of the major catalyst manufacturers. In Europe, principal sources of supply are Rhc ne-Poulenc and Condea. [Pg.156]

CATALYTIC PRODUCTION AND PURIFICATION OF NANOTUBULES HAVING FULLERENE-SCALE DIAMETERS... [Pg.15]

A detailed discussion of CO as a ligand and the chemistry of metal carbonyls is on pp. 926-9. CO is a key intermediate in the catalytic production of a wide variety of organic compounds on an industrial scale. These include ... [Pg.309]

Co(TPP) has been demonstrated to act as a catalyst for the electrocarboxylation of benzyl chloride and butyl bromide with CO - to give PhCHiCfOiOCH Ph and Bu0C(0)C(0)0Bu, respectively. The propo.sed mechanism involved Co(TPP)R and [Co(TPP-N-R) as intermediates (the latter detected by spectroscopy) in the catalytic production of free R or R-, which then reacted directly with Co(TPP) precipitated on graphite foil has been successfully used for the determination of organic halides, including DDT and 1,2,3,4,5,6-hexachlorocyclohexane (lindane), to sub-ppm level in aqueous solution. Deoxygenation of the solutions is not required, and the technique is moderately insensitive to the ionic composition of the solution. ... [Pg.286]

The catalytic products for all the CNF catalysts include CjH, COx and frace amount of... [Pg.746]

It is generally accepted that oxo-Mn (V) is the catalytieally aetive speeies however, the reaction mechanism is currently under intensive debate sinee it strongly depends on the oxygen donor and the reaction conditions (6). On the other hand, low catalytic productivities are obtained due to oxidative degradation of the salen hgand (7). [Pg.480]

Figure 7.7 STM images of Pt(lll) at 300K (a) (75 x 75) A2, 20 mTorr cyclohexene plus 20mTorr H2 no catalytic products formed (b) (50x 50)A2, 200 mTorr H2, 20 mTorr of cyclohexene, disordered surface and cyclohexane formed (c) (90 x 90) A2, CO added, no catalytic activity. (Reproduced from Ref. 11). Figure 7.7 STM images of Pt(lll) at 300K (a) (75 x 75) A2, 20 mTorr cyclohexene plus 20mTorr H2 no catalytic products formed (b) (50x 50)A2, 200 mTorr H2, 20 mTorr of cyclohexene, disordered surface and cyclohexane formed (c) (90 x 90) A2, CO added, no catalytic activity. (Reproduced from Ref. 11).
Consequently, a crucial goal that still remains to be realized is the catalytic production of living polymers that increase the polymer/catalyst ratio and thus enhance catalyst productivity. The catalytic production of living polymers is feasible if we develop FI catalysts that incorporate monomers without termination, even in the presence of a chain transfer agent, and which only undergo chain transfer in the absence of a reacting monomer. [Pg.41]

In addition to the above achievements, researchers at Dow reported on the catalytic production of multiblock copolymers comprised of PE and amorphous pol y(cthylenc-co-1 -octene) segments, by a catalyst system comprised of Zr-FI catalyst 59, Hf complex 60 (Fig. 38), and Et2Zn [11, 90],... [Pg.41]

Fig. 36 Procedures for catalytic production of Zn-terminated PEs. Reproduced with permission from Nakayama et al. [76]. Copyright 2003, The Society of Synthetic Organic Chemistry, Japan... Fig. 36 Procedures for catalytic production of Zn-terminated PEs. Reproduced with permission from Nakayama et al. [76]. Copyright 2003, The Society of Synthetic Organic Chemistry, Japan...
Moisala, A. Nasibulin, A. G. Kauppinen, E. I. 2003. The role of metal nanoparticles in the catalytic production of single-walled carbon nanotubes—a review. J. Phys. Condens. Matter 15 S3011-3035. [Pg.342]

Autocatalysis is a special type of molecular catalysis in which one of the products of reaction acts as a catalyst for the reaction. As a consequence, the concentration of this product appears in the observed rate law with a positive exponent if a catalyst in the usual sense, or with a negative exponent if an inhibitor. A characteristic of an autocat-alytic reaction is that the rate increases initially as the concentration of catalytic product increases, but eventually goes through a maximum and decreases as reactant is used up. The initial behavior may be described as abnormal kinetics, and has important consequences for reactor selection for such reactions. [Pg.187]

Autocatalysis (i.e., catalysis by one of the products of the reaction), should also be considered. The impact of the accumulation of the catalytic product must be evaluated, and appropriate consideration given to runaway potential and prevention. [Pg.136]

An autocatalytic reaction may be able to proceed in. the absence of the catalyst. In some cases the catalytic product may be removed as it forms, by distillation, extraction, precipitation, or some other means. The process, A => B + P, may have the rate equation... [Pg.219]

The combination of Eqs. (13-16) implies that both reactions are catalytic under aerobic conditions, which, indeed, they are. The kinetics of catalytic product formation established that two different mechanisms operate. For aldehyde or ketone formation a rate law as in Eq. (18) has been established, whereas the 1,2-diol formation follows the rate law Eq. (19). [Pg.201]

The photocatalytic oxidation of organic and inorganic compounds and the photo-catalytic production of H202 occurs also at the surface of iron(III)(hydr)oxides. It has been proposed (e.g., Hoffmann, 1990 Faust and Hoffmann, 1986) that the oxidation of S(IV) by 02 in atmospheric water is catalyzed by iron(III)(hydr)oxide particles. It is assumed that the reductant (HSO3) is specifically adsorbed at the surface of an iron(III)(hydr)oxide, forming either a monodentate or a bidentate surface complex ... [Pg.354]

The production of H2 from some by-products of biomass conversion is also a possible option, which also requires the development of, new, more stable, more efficient catalysts that operate directly in the liquid phase. The catalytic production of hydrogen from more valuable products, such as bioethanol, should be reconsidered with appropriate economic assessments that take into account the alternative possible uses of these products. [Pg.400]


See other pages where Catalytic production is mentioned: [Pg.345]    [Pg.36]    [Pg.17]    [Pg.19]    [Pg.21]    [Pg.23]    [Pg.25]    [Pg.25]    [Pg.346]    [Pg.19]    [Pg.223]    [Pg.101]    [Pg.105]    [Pg.224]    [Pg.41]    [Pg.41]    [Pg.41]    [Pg.69]    [Pg.122]    [Pg.208]    [Pg.1352]    [Pg.17]    [Pg.366]    [Pg.120]    [Pg.73]    [Pg.232]    [Pg.69]   
See also in sourсe #XX -- [ Pg.2 ]




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