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Superactivity

Fig. 4. Activity vs polymerization time. Polymerization occurs in hexane at 343 K (70°C) and 0.7 MPa (7 bat) with a superactive third-generation catalyst... Fig. 4. Activity vs polymerization time. Polymerization occurs in hexane at 343 K (70°C) and 0.7 MPa (7 bat) with a superactive third-generation catalyst...
Fig. 6. Activity and isotacticity vs Al/donor ratio. Batch polymerisation occurs ia diluent hexane at 70°C and 0.7 MPa (7 bar) for 4 h with a superactive... Fig. 6. Activity and isotacticity vs Al/donor ratio. Batch polymerisation occurs ia diluent hexane at 70°C and 0.7 MPa (7 bar) for 4 h with a superactive...
Residual catalyst (expressed as ash content). The actual residues depend on the manufacturing process used and on the characteristics of the polymer. The so-called new generation HD-PE processes such as the Solvay process use superactive catalysts which produce polymers with a low ash content and, hence, low or negligible odor. Some narrow MWD (Molecular Weight Distribution) resins also have lower catalyst residues than their wide MWD counterparts. [Pg.65]

Heinze modified the technique by purifying the solvent by transferring it under high vacuum from the electrochemical cell to superactive alumina in a separate vessel [27, 28]. Such sophisticated methods made it possible to generate reversible polyanions up to octaanions of aromatic and olefinic hydrocarbons [27, 28, 30-33]. [Pg.96]

Later, Corey reported that the bulky superacid triflylimide (Tf2NH) protonates chiral oxazaborolidines to form superactive, stable, chiral acids 11a and 11b, which are highly effective catalysts for a wide variety of enantioselective Diels-Alder reactions that were beyond the reach of synthetic chemists (Scheme... [Pg.364]

The activity advantage of zeolite catalysts over amorphous silica-alumina has well been documented, Weisz and his associates [1] reported that faujasite Y zeolite showed 10 to 10 times greater activity for the cracking of n-hexane than silica-alumina. Wang and Lunsford et al. [2] also noted that acidic Y zeolites were active for the disproportionation of toluene while silica-alumina was inactive. The activity difference between zeolite and silica-alumina has been attributed to their acidic properties. It is, however, difficult to explain the superactivity of zeolite relative to silica-alumina on the basis of acidity, since the number of acid sites of Y-type zeolite is only about 10 times larger than that of silica-alumina. To account for it, Wang et al. [2] proposed that the microporous structure of zeolite enhanced the concentration of reactant molecules at the acid sites. The purpose of the present work is to show that such a microporous effect is valid for pillared clay catalysts. [Pg.377]

AOT/isooctane Trypsin, a-chymotryp-sinogen A Investigation on protein-protein interactions in RMs. Trypsin showed superactivity by a factor of 21.3 during activation of a-chymotrypsino-gen A to a-chymotrypsin [285]... [Pg.169]

Fig. 8.16. Electrochemical cell for voftammetric experiments under superdry conditions (a) Measuring cell with three-electrode arrangement, (b) Drying vessel with superactive aluminum. (Reprinted with permission from J. Heinze, Angwandte Chemie 23 831, copyright 1986, Wiley-VCH Verlag.)... Fig. 8.16. Electrochemical cell for voftammetric experiments under superdry conditions (a) Measuring cell with three-electrode arrangement, (b) Drying vessel with superactive aluminum. (Reprinted with permission from J. Heinze, Angwandte Chemie 23 831, copyright 1986, Wiley-VCH Verlag.)...
The superactivity of zeolite catalysts sometimes becomes a considerable disadvantage when it is responsible for undesirable side reactions. These may alter the selectivity or cause deactivation and aging. These problems have been reviewed (56). [Pg.452]

Current Processes. The development of superactive third-generation supported catalysts enabled the introduction of simplified processes, without sections for catalyst deactivation or removal of atactic polymer. By eliminating the waste streams associated with the neutralization of catalyst residues and purification of the recycled diluent and alcohol, these processes minimize any potential environmental impact. Investment costs arc reduced by approximately one-third over slurry process plants. Energy consumption is minimized by elimination of the distillation of recycled diluent and alcohol. The total plant cost for the production of polymer is less than 130% of the monomer price, when a modem process is used, compared to 175% for a slurry process. [Pg.1147]

Although the net effect of HIV infection is immunodeficiency, the infection generally results in the increased activation of the immune response but the overall impact of this immune hyperactivity is negative. The activated CD4+ cells play a pivotal role in the replication of the virus this activation of CD4+ cells enhances the secretion of various cytokines, some of which contribute to muscle wasting. A superactive humoral response against HIV impairs the body s ability to mount antibody response against other pathogens, and the activation of immune response... [Pg.176]

Fig. 9. Model of superactive Pd"+ site stabilized on y-alumina surface (143). Fig. 9. Model of superactive Pd"+ site stabilized on y-alumina surface (143).
Catalytic superactivity of electron-deficient Pd for neopentane conversion was recently verified for Pd/NaHY (157, 170). The reaction rate was positively correlated with the proton content of the catalyst. Samples that contained all the protons generated during H2 reduction of the catalysts were two orders of magnitude more active than silica-supported Pd. Samples prepared by reduction of Pd(NH3)2+NaY displayed on intermediate activity. It was suggested that Pd-proton adducts are highly active sites in neopentane conversion. With methylcyclopentane as a catalytic probe, all Pd/NaY samples deactivated rapidly and coke was deposited. Two types of coke were found (by temperature-programmed oxidation), one of... [Pg.75]

Therefore, adopting the solution of reactive distillation instead of separate reaction and separation units does not lead automatically to a more efficient process. Matching the conditions of separation and reaction in the same device requires careful design. The element with the highest impact is the chemical reaction. The key condition for an efficient and competitive process by reactive distillation is the availability of a superactive catalyst capable to compensate the loss in the driving force by phase equilibrium, but at the same time ensuring a good selectivity pattern. [Pg.196]

The above simple reactions involve, in practice, costly operations, such as neutralization, washing, liquid phase and solid separations. These can be substantially reduced or even suppressed if superactive heterogeneous catalysts are employed. [Pg.404]

Heber D, Odell WD (1978) Pituitary receptor binding activity of active, inactive, superactive and ihibitory analogs of gonadotropin-releasing hormone. Biochem Biophys Res Commun 82 67-73... [Pg.334]


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See also in sourсe #XX -- [ Pg.298 ]




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Phosphoribosylpyrophosphate synthetase superactivity

Superactive carbons

Superactive catalysts

Superactive initiator

Third generation superactive catalysts

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