chemical physics of discharges - Argonne National Laboratory
chemical physics of discharges - Argonne National Laboratory chemical physics of discharges - Argonne National Laboratory
4 OL. ' , I. . TesCs. With.Coals .of Different Rank . . . In addition to the h,yab -coal, lignite, subbituminous, low-volatile bituminous, and anthracitc coals. coal char, and activated carbon were' tested as raw materials for producing hydrogen cyanide. It is thought that the volatile matter in.coa1 reacts with the ammonia to form hydrogen cyanide, therefore coals with higher volatile content should produce more hydrogen cyanide. The volatile-matter contents on a moisture-free basis of the various materials tested are as follows: Volatile matter, Tes t Identification of coal Source of coal percent C-123, 124,. Hvab, Pittsburgh seam Bruceton, Pa. 34.0 125, 198, 239, 241, 243 C -207 Activated carbon, Union Carbide an,d 2.0 Grade SXWC Carbon Corp. c -2 10 Anthracite Anthracite Research 7.6 Center, Schuylkill Haven, Pa. C -246 Subb, Laramie seam Erie, Colo. 38.5 C -249 Lvb, Pocahontas #3 seam Stepheson, W. Va. 17.5 C-252 Lignite, unnamed seam Beulah, N. Dak. 41.1 C-254 1/ Pretreated hvab,- Pittsburgh seam Bruceton, Pa. 32.6 - 1/ Treated with air at ZOOo C. Table 2 shows the results of these tests. Lignite with 41 percent volatile matter produced the most hydrogen cyanide, 0.4 cu ft per cubic foot of ammonia consumed; activated carbon, containing the least volatile matter (2.0 percent), produced the least hydrogen cyanide, 0.007 cu ft per cubic foot of ammonia consumed. The chemical nature of the volatile matter and the oxygen content of the coal may also affect the hydrogen cyanide yield. The ratio of H, to CO in the off gases varied from 2.3 to 1 for subb coal and 2.4 to 1 for lignite to 7 to 10 to 1 for hvab. The higher carbon monoxide values obtained uith subb coal and lignite are due to the higher oxygen contents of these coals, being 17.1 and 20.3 percent, respectively, compared with 8.0 percent for the hvab coal.
I b 1 I Table 2.- Data from Tests with Various Coals and Ammonia with Helium at 1.250" C I I Product gas, percent I Test HCNL' H2S & H2 02 N2 CO C02 Ct4 C2H4 C3H8 I ' C-246 Subb 5.4 0.0 0.0 64.2 0.0 4.9 28.0 0.5 2.4 0.0 0.0 , C-249 Lvb 4.2 .O .O 78.9 .1 14.2 3.6 .O 3.0 .2 tr. C-252 Lignite 6.4 tr. .O 64.6 .1 6.1 26.3 .5 2.4 .O .O C-254 Pretreated, hvab 3.8 .1 .O 72.3 .8 10.6 14.3 .O 1.9 .O .O j C-210 Anthracite 0.2 .o .o 73.4 .3 21.4 2.9 .4 1.5 .o .o C-207 Activated carbon .25 .O .O 70.0 .O 23.0 6.6 .1 0.3 .O .O 9 Feed i I He 9 cu ft/hr NH3 9 cu ft/hr Sol ids feed, lb/hr Total off gas He-free, cu ft/hr 'Length of run, min 1 C-246 Subb 0.91 1.00 0.42 6.88 30 C-249 Lvb .97 1.00 .47 3.92 30 C-252 Lignite 1.06 1.00 .37-.40 6.38 15 C-254 Pretreated, hvab 1.04 1.00 .35 5.80 30 C -210 Anthracite 1.02 1.15 -37-.40 4.15 15 f C-207 Activated carbon 1.06 1.15 .62 3.23 15 / Yield, cu ft 1 HCN/cu ft HCN/cu ft J HCN/lb coal feed consumed ,I C-246 Subb 0.88 0.37 0.37 C-249 Lvb / C-252 Lignite ! C-254 Pretreated, hvab C-210 Anthracite > C-207 Activated carbon .34 1.05 .63 .02l2/ .013- .16 .41 .22 .007 .007 .16 .41 .22 .007 .007 I ) L/ - 21 Wet-analytical method of analysis for HCN only; other components are the average of 2 chromatograph and 2 mass spectrometer analyses, HCN-free basis. Per pound of carbon. Tests were made to determine the effect that oxygen in the treating gas would have on the yield of hydrogen cyanide. It was thought that the heat for raising the temperature of the reactants to reaction temperature could be supplied by direct contact with a hot flue gas containing oxygen instead of by electric heating (table 3). In test C-125, a maximum yield of hydrogen cyanide was pro- duced for tests with air in the treating gas--0.12 cu ft of hydrogen cyanide per cubic foot of ammonia consumed, or 9.2 percent hydrogen cyanide in the product gas. When more than 0.5 percent. air was fed into the reactor, moisture condensed on the walls of the solids-collection flask; the yield of hydrogen cyanide de- creased. The moisture could have been absorbing the hydrogen cyanide since hydrogen cyanide is highly soluble in water. This approach was abandoned.
- Page 360 and 361: 359 \ Frozen Compositior: Calcillat
- Page 362 and 363: I 1 \ 361 -. ne reaction proceecis
- Page 364 and 365: \ 36 3 ' h, I 26. H. Purnell, Gas C
- Page 366 and 367: In experiments on the direct conver
- Page 368 and 369: 367 used as blnders, with different
- Page 370 and 371: 369 ' i 1. REFERENCES Berber, John
- Page 372 and 373: Distribution and yield rates of pro
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- Page 376 and 377: 4 372 090- > E w - m c N O - 0 z :
- Page 378 and 379: A-Feed tank 6-Thermocracker GReceiv
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- Page 382 and 383: COAL DEASH& AND HIGH-PURITY COKE Wa
- Page 384 and 385: 3Pn _. -. - L -J:,J.-;~~~L, ):as se
- Page 386 and 387: S ~ l ~ o n~pg:ading r is the resul
- Page 388 and 389: The range ~f temperatures and gener
- Page 390 and 391: . .. 386 9 * - r. Y 2 .' d a f' r.
- Page 392 and 393: .) .L m 388 I
- Page 394 and 395: TABLE 4 390 DELAYED COKING OF DEASH
- Page 396 and 397: , ! I- on '---
- Page 398 and 399: 394 The present method is to keep t
- Page 400 and 401: 396 ‘c erperature, while the pres
- Page 402 and 403: 2, '! ! Proximate Analysis, wt $ Mo
- Page 404 and 405: 0 IS 0 14 LL 9 013 e \ 3 b- m *- 01
- Page 406 and 407: 402 HYDROGEN CYANIDE PRODUCED FROM
- Page 408 and 409: 404 Before startup, the system is p
- Page 412 and 413: Table 3.- Product Gas Analyses and
- Page 414 and 415: 410 BIBLIOGRAPHY 1. American Public
- Page 416 and 417: Figure 2. Enclosure surrounding hyd
- Page 418 and 419: 0 0 f v) C 0 u m I z 2 c 2 r d J w
- Page 420 and 421: 0. E c .4 7 .. .c . I ( - Low tempe
- Page 422 and 423: 418 cual. A mjor aa\;antage or' the
- Page 424 and 425: 420 Ir ?Y ? ? 9 9 9 pc rod n o c o
- Page 426 and 427: 422 Table 3. Room-texperature M'dss
- Page 428 and 429: 424 state, depending on the strengt
- Page 430 and 431: Table 4. Room-?;ergerature isomer s
- Page 432 and 433: I' 1.3 . /o 9 IO 9 6 a 425 F F 33 I
- Page 434 and 435: Brooks J.D. and Sternhell S. (1957)
- Page 436 and 437: (52) Gib3 T.C. and Greenwood N.N. (
- Page 438 and 439: 434 transducer vas then introduced
- Page 440 and 441: 436 yield is quite similar. The con
- Page 442 and 443: ?-!??? 0 mv, Uh\OhIe . . . . eirlrl
- Page 444 and 445: 4. 5. 6. 7. 8. 9. 10. 11. 12. 13. 4
- Page 446 and 447: 442 CHEMICAL REACTIONS IN A CORONA
- Page 448 and 449: helium 444 CORONA REACTOR SYSTEM Fi
- Page 450 and 451: 446 The ultraviolet spectrum. for t
- Page 452 and 453: Biphenyl Fraction 448 The low molec
- Page 454 and 455: LUd The actual structural definitio
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- Page 458 and 459: ’. 454 Mechanism I The available
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Table 2.- Data from Tests with Various Coals and Ammonia with Helium at 1.250" C<br />
I<br />
I Product gas, percent<br />
I Test HCNL' H2S & H2 02 N2 CO C02 Ct4 C2H4 C3H8<br />
I<br />
' C-246 Subb 5.4 0.0 0.0 64.2 0.0 4.9 28.0 0.5 2.4 0.0 0.0<br />
, C-249 Lvb 4.2 .O .O 78.9 .1 14.2 3.6 .O 3.0 .2 tr.<br />
C-252 Lignite 6.4 tr. .O 64.6 .1 6.1 26.3 .5 2.4 .O .O<br />
C-254 Pretreated, hvab 3.8 .1 .O 72.3 .8 10.6 14.3 .O 1.9 .O .O<br />
j C-210 Anthracite 0.2 .o .o 73.4 .3 21.4 2.9 .4 1.5 .o .o<br />
C-207 Activated carbon .25 .O .O 70.0 .O 23.0 6.6 .1 0.3 .O .O<br />
9 Feed<br />
i<br />
I<br />
He 9<br />
cu ft/hr<br />
NH3 9<br />
cu ft/hr<br />
Sol ids<br />
feed,<br />
lb/hr<br />
Total<br />
<strong>of</strong>f gas<br />
He-free,<br />
cu ft/hr<br />
'Length<br />
<strong>of</strong> run,<br />
min<br />
1 C-246 Subb 0.91 1.00 0.42 6.88 30<br />
C-249 Lvb .97 1.00 .47 3.92 30<br />
C-252 Lignite 1.06 1.00 .37-.40 6.38 15<br />
C-254 Pretreated, hvab 1.04 1.00 .35 5.80 30<br />
C -210 Anthracite 1.02 1.15 -37-.40 4.15 15<br />
f C-207 Activated carbon 1.06 1.15 .62 3.23 15<br />
/ Yield, cu ft<br />
1 HCN/cu ft HCN/cu ft<br />
J HCN/lb coal feed consumed<br />
,I C-246 Subb 0.88 0.37 0.37<br />
C-249 Lvb<br />
/ C-252 Lignite<br />
! C-254 Pretreated, hvab<br />
C-210 Anthracite > C-207 Activated carbon<br />
.34<br />
1.05<br />
.63<br />
.02l2/<br />
.013-<br />
.16<br />
.41<br />
.22<br />
.007<br />
.007<br />
.16<br />
.41<br />
.22<br />
.007<br />
.007<br />
I<br />
)<br />
L/<br />
- 21<br />
Wet-analytical method <strong>of</strong> analysis for HCN only; other components are the<br />
average <strong>of</strong> 2 chromatograph and 2 mass spectrometer analyses, HCN-free basis.<br />
Per pound <strong>of</strong> carbon.<br />
Tests were made to determine the effect that oxygen in the treating gas<br />
would have on the yield <strong>of</strong> hydrogen cyanide. It was thought that the heat for<br />
raising the temperature <strong>of</strong> the reactants to reaction temperature could be supplied<br />
by direct contact with a hot flue gas containing oxygen instead <strong>of</strong> by electric<br />
heating (table 3). In test C-125, a maximum yield <strong>of</strong> hydrogen cyanide was pro-<br />
duced for tests with air in the treating gas--0.12 cu ft <strong>of</strong> hydrogen cyanide per<br />
cubic foot <strong>of</strong> ammonia consumed, or 9.2 percent hydrogen cyanide in the product<br />
gas. When more than 0.5 percent. air was fed into the reactor, moisture condensed<br />
on the walls <strong>of</strong> the solids-collection flask; the yield <strong>of</strong> hydrogen cyanide de-<br />
creased. The moisture could have been absorbing the hydrogen cyanide since<br />
hydrogen cyanide is highly soluble in water. This approach was abandoned.