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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, - 22. Table 3. Discharge pyrolysis of coal in the presence of Ar Volatile matter, percent Initial pressure of Ar, Irn Reaction time, min Product, 10-1 mmoles/g. coal E, Cb C?H2 C?Ha co c 02 H? 0 Total Gases, wt pct C gasificd,'percent C converted to gaseous liydrucarbons, percent Lignite hvab lvb Anthracite 44.0 5.1 5 86.8 2.1 10.4 0.6 79.5 8.6 7.5 33.5 19.4 4.5 39.2 5.1 20 9n.5 2.5 15.8 0.7 31.9 0.7 3.4 16.5 11.4 6.6 20.2 6.1 5.1 5.1 20 20 113 6/! .5 4.0 0.4 S.6 2.0 0.6 trace 10.8 4.2 0.2 trace 4.9 1.6 9.4 3.4 4.9 1.2 3.5 0.7 Tar -- Substantial amounts of tars were obtained from the hvab and the lvb coals in the discharge pyrolyses. The tars were compared by IR and UV analyses with the tar obtaincd from the thermal pyrolysis (at 700' C) of the hvab coal. All tne 1: spectra showed the presence of usual aliphatic C-H bands (2860-2940, cm-') and aromatic hands (740-860 ca-l) which are typical of pitch and coal. The tars obtained from the discharse pyrolyses, however, exhibited weaker aromatic bands and a stron:;cr carbonyl band (1710 cm-l) than the tar obtained from thermal pyrolysis. The UV spectra (of the tars extracted by benzene or ethanol) exhibited no distinct absorption band for the tar btained from the thermal pyrolysis, but exhibited bands at 3140, 3309, and 3470 1 (which could be attributed to derivatives of pyrene) for those obtained from the discharge pyrolyses. All the residual chars exhibited no distinct band over the entire IR spectrum. Effect of Cooling by Liquid Nitrogen , A. Hvab Coal -- When one end of an h-shaped reactor (vol. = 41 ml) was cooled with iiquid Nz while the other leg containing the hvab coal was subjected to the discharge pyrolysis, it was observed that the pressure reading of the reactor never exceeded 0.5 mm during ?he course of the decomposition. The end products consisted mainly of hydrocarbons and water, without significant amounts of H2 and CO. Acecyiene was the main hydrocarbon, but substantial amunts of other C2, C?, CI,, Cg and C6 hydrocarbons were also formed. Without liquid N2 cooling, the other C2 and Cj hydrocarbons were insignificant and the C4, C5 and c6 hydrocarbons were not measurable. The product analyses, except that for C4, C5 and c6 hydro- carbons whicii constitute less than 2 percent of the gases, are shown in Table 4. The extent 0: devolatilization and the hydrocarbon yield are significantly increased. I! \ \ I

.4 4 0 W 0 m .d m x .-( 0 x w M m s 0 .d -0 C a .d rl 0 0 C bc U U .r( C Q .d .d r( w 0 LI u 0) w U w 23. ".tal 004 NN.4 I-mm NNrn NN4 ... mom der- mmN ... 2: am- m.4e 4.44 m.om o o m ... ... m o m 0-40 ... r-wm 000 ... 'I-!? mmrl mom ... rlrlo ONN r-om *mm mmm 000 ... ... \o ma m . . OON d r-00 4N I 1 0 w 4J 4 C M cl .4 4 ,

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22.<br />

Table 3. Discharge pyrolysis of coal in the presence of Ar<br />

Volatile matter,<br />

percent<br />

Initial pressure of Ar,<br />

Irn<br />

Reaction time, min<br />

Product, 10-1 mmoles/g. coal<br />

E,<br />

Cb<br />

C?H2<br />

C?Ha<br />

co<br />

c 02<br />

H? 0<br />

Total Gases, wt pct<br />

C gasificd,'percent<br />

C converted to gaseous<br />

liydrucarbons, percent<br />

Lignite hvab lvb Anthracite<br />

44.0<br />

5.1<br />

5<br />

86.8<br />

2.1<br />

10.4<br />

0.6<br />

79.5<br />

8.6<br />

7.5<br />

33.5<br />

19.4<br />

4.5<br />

39.2<br />

5.1<br />

20<br />

9n.5<br />

2.5<br />

15.8<br />

0.7<br />

31.9<br />

0.7<br />

3.4<br />

16.5<br />

11.4<br />

6.6<br />

20.2 6.1<br />

5.1 5.1<br />

20 20<br />

113 6/! .5<br />

4.0 0.4<br />

S.6 2.0<br />

0.6 trace<br />

10.8 4.2<br />

0.2 trace<br />

4.9 1.6<br />

9.4 3.4<br />

4.9 1.2<br />

3.5 0.7<br />

Tar -- Substantial amounts of tars were obtained from the hvab <strong>and</strong> the lvb coals<br />

in the discharge pyrolyses. The tars were compared by IR <strong>and</strong> UV analyses <strong>with</strong><br />

the tar obtaincd from the thermal pyrolysis (at 700' C) of the hvab coal. All<br />

tne 1: spectra showed the presence of usual aliphatic C-H b<strong>and</strong>s (2860-2940, cm-')<br />

<strong>and</strong> aromatic h<strong>and</strong>s (740-860 ca-l) which are typical of pitch <strong>and</strong> coal. The tars<br />

obtained from the discharse pyrolyses, however, exhibited weaker aromatic b<strong>and</strong>s<br />

<strong>and</strong> a stron:;cr carbonyl b<strong>and</strong> (1710 cm-l) than the tar obtained from thermal<br />

pyrolysis. The UV spectra (of the tars extracted by benzene or ethanol) exhibited<br />

no distinct absorption b<strong>and</strong> for the tar btained from the thermal pyrolysis, but<br />

exhibited b<strong>and</strong>s at 3140, 3309, <strong>and</strong> 3470 1 (which could be attributed to derivatives<br />

of pyrene) for those obtained from the discharge pyrolyses.<br />

All the residual chars exhibited no distinct b<strong>and</strong> over the entire IR spectrum.<br />

Effect of Cooling by Liquid Nitrogen ,<br />

A. Hvab Coal -- When one end of an h-shaped reactor (vol. = 41 ml) was cooled<br />

<strong>with</strong> iiquid Nz while the other leg containing the hvab coal was subjected to the<br />

discharge pyrolysis, it was observed that the pressure reading of the reactor<br />

never exceeded 0.5 mm during ?he course of the decomposition. The end products<br />

consisted mainly of hydrocarbons <strong>and</strong> water, <strong>with</strong>out significant amounts of H2 <strong>and</strong><br />

CO. Acecyiene was the main hydrocarbon, but substantial amunts of other C2, C?,<br />

CI,, Cg <strong>and</strong> C6 hydrocarbons were also formed. Without liquid N2 cooling, the<br />

other C2 <strong>and</strong> Cj hydrocarbons were insignificant <strong>and</strong> the C4, C5 <strong>and</strong> c6 hydrocarbons<br />

were not measurable. The product analyses, except that for C4, C5 <strong>and</strong> c6 hydro-<br />

carbons whicii constitute less than 2 percent of the gases, are shown in Table 4.<br />

The extent 0: devolatilization <strong>and</strong> the hydrocarbon yield are significantly<br />

increased.<br />

I!<br />

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