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Figure 7.16. A sketch of the magnetic field for the planar case. (a) [R, R] polarization case; see also Figure 7.12. (b) [ , ] polarization case; see also Figure 7.13.



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420 The samples proved to be very active and selective in the aromatization of C6+ alkanes (n-hexane and n-octane) From n-octane, as main products, only ethylbenzene and a-xylene were formed The catalysts have low acidity due to significant dehydration of the zirconia surface, and high surface area since the carbon matrix prevents sintering of the Zr02 particles A pore-size-regulated 5% ZnO-H-ZSM-5 catalyst was studied in the aromatization of C4-C 6 hydrocarbon stream at 500_540 c 421 Modification of the pore size was performed by chemical vapour deposition of (EtO)4Si to form Si02 A significant enhancement of p-xylene selectivity as high as 99% was achieved with this catalyst with the production of benzene and toluene remaining unaffected A new method has been described to obtain acid or bifunctional catalysts for aromatization by steaming the as-synthesized Ga-H[AI]-ZSM-5 at low temperature (530 C).





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Ignoring the desire to include the product pivot in the ongoing pivot query, the following subquery summarizes the order line information:

422,423 During the steaming process a profound and progressive demetalization (removal of Ga and AI) takes place The propane aromatization properties of these catalysts are similar to those prepared by means of direct calcination under dry air at higher temperature (> 700 C) or by conventional impregnation methods This method provides an alternative synthesis for aromatization catalysts without long and expensive conventional preparation Acidic solids loaded with bimetallic Pt alloys were also studied A synergistic effect was observed using Pt-Ga supported on H-ZSM-5 zeolite in the aromatization of n-butane 424 Enhanced aromatization activity, significant increase in aromatization selectivities, and suppressed side reactions (hydrogenolysis and hydrogenation) are the main improvements observed The Pt-Ge intermetallic compound was shown to form on the external surface of H-ZSM-5 during chemical vapor deposition of Ge(acachCI 2425 The catalyst exhibited lower dehydrogenation ability, a key step in aromatization, than that of Pt on H-ZSM-5.

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WA R N I N G When fitting polynomial trend curve to data points, be sure that the degree of the polynomial is much smaller than the number of data points. This reduces the likelihood of overfitting.

11.3 See Georgi and Glashow (1974). The group must be at least of rank 4 to allow an S U ( 3 ) x S U ( 2 ) x U(1) subgroup, and it must be simple so that there is only one coupling constant. There are many possibilities, but only SU( 5) survives the requirements of low-energy phenomenology that the unifying group have complex representations, and that it allow both fractimally and integrally charged particles. It can accommodate the known particles in anomaly-free representations (see Exercise 11.4)1 which satisfies the final criterion. 11.4 See Cheng and Li (1984), $14.1. Choose Ta = T b= T" = Q, where Q

This, however, is coupled with lower coke formation and, consequently, results in a longer catalyst life The activity of Pt-Ge on H-ZSM-5 is also lower for hydrogenolysis These catalytic properties make this sample a favorable catalyst for selective aromatization A systematic study of the aromatization of propane and butane resulted in the observation that ZSM-5 loaded with Pt and Re when presulfided gives high BTX selectivity, low methane and ethane selectivity, and low coke formation All of these are attractive features for a commercial process 426.

T I P Even a seemingly simple question such as how many customers are there can have different answers depending on specifics: how many customers have placed an order and how many households are in the database may have very different answers.

->Item[$i]->ItemAttributes->ListPrice ->FormattedPrice . ]]></price> ; $xml .= \t\t<thumb> . $xmlResponse->Items->Item[$i] ->SmallImage->URL . </thumb> ; $xml .= \t</book> ;

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