secondary cells with lithium anodes and immobilized fused_salt
secondary cells with lithium anodes and immobilized fused_salt
secondary cells with lithium anodes and immobilized fused_salt
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d (Sulfur]<br />
dt<br />
m i trogenj<br />
dt<br />
32.<br />
E ks (Sulfur)<br />
= kn (Nitrogen)<br />
where llkg,17 rcks,lr <strong>and</strong> trknlr are rate constants for gasoline formation<br />
<strong>and</strong> removal of sulfur <strong>and</strong> nitrogen respectively. There was no<br />
change in the concentration of hydrogen in thc system during the<br />
course of the reaction since the hydrogen p~ essure was maintained I<br />
, constant throughout llqdrogen atoms may be involved in the rate-<br />
determining step but %he ir concentration constitutes one of the<br />
constant factors in the rate constant term <strong>and</strong> does not show up in<br />
the rate equation. llowever. hydrogen actually takes part in the<br />
hydrocracking rex tinos dnd , hence, @\he redc tions are considered<br />
pseudo-f 1 I st order<br />
The hydrocrack irig reactions under study follow true Arrhenius<br />
temperature dependence (Figa~re 14) <strong>and</strong> the rate constants can be<br />
represented b> eq?lations 4 to 6.<br />
kg = 0 1567 x 106 e 17:600/RT hrs<br />
k, = c? 2134 x LO5 e 14 500/RT hrs -1<br />
(4 1<br />
(5)<br />
hn I 0 47jE x lo5 E 15.900/RT hrs..l<br />
(6)<br />
The following values c,f enthalpies <strong>and</strong> entropies of activation were<br />
calculated by tht Eyri ng equatiorl plotbng log k’/T versus T (Figure<br />
15)<br />
AHg = 16,200 c al /mole, asg = 43 5 e.u.<br />
Alls = 12,200 c al /mole, ASs = -44.9 e.u<br />
411, = 14,QOO cal /mole, ASn = 45 9 e-u.<br />
,<br />
Linear relationship was found between kg, ks, <strong>and</strong> kn (Figure 16)<br />
<strong>and</strong> can be represerited by equations 7 to 9<br />
A major part of tile gasol iiie is expected to be formed by the crack-<br />
ing of hydrocarbons, but a minor part comes from the decomposition<br />
of some of tllt slilfur, oxygen. <strong>and</strong> nitrogen compounds. The yield<br />
of gasoline thus tle.peritls, to some extent, on the removal of sulfur<br />
<strong>and</strong> nitrogen <strong>and</strong> this may result in some sort of interrelationship<br />
between kg, ks, <strong>and</strong> kll. The dissociation energies of the C-C, C-S,<br />
<strong>and</strong> C-.X bonds may also have some influence on the above relation-<br />
ship, especiall>- between k, <strong>and</strong> kn. However, the results presented<br />
in this paper do not throw muc.li light on the effect of other tem-<br />
perature <strong>and</strong> pressure conditions <strong>and</strong> equations 7 to 9 are not con-<br />
sidered to be having much quantitative significance at this stage.<br />
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