Vapor Phase Catalyst (Con't) | ||||
TOM REEL |
BAG | ITEM | FRAMES | |
SATURATION catalyst, action of W, V, Ni, Co and Fe on |
254 |
449-457 |
||
catalyst tests (January 1942) |
253 |
848-857 |
||
SILICA-alumina-iron catalyst behavior in hydrocarbon conversion |
126 |
1167-1169 |
||
SILICA-aluminum oxyhydrate, behavior in HF treated tungsten free catalysts |
170 |
713-720 |
||
SILICA-magnesia cracking catalyst, influence of the conditions of precipitation upon gasification |
141 |
65-68 |
||
SILICATE catalysts |
173 |
416-417 |
||
SPLITTING activity of various types of catalysts |
205 |
755 |
||
activity of catalyst K-6102 as compared to K-5058 under conditions of catalytic cracking |
126 |
1249-1251 |
||
activity of catalysts, numerical expression for, |
257 |
922-925 |
||
Translation T-345 |
257 |
925a-925d |
||
Translation T-345 |
273 |
845-848 |
||
catalyst |
50 |
951-966 |
||
new |
254 |
92-103 |
||
by Gunther |
181 |
6408-6817 |
||
for catalytic high pressure hydrogenation |
254 |
53-54 |
||
catalysts from iron sulfide on fullers earth |
254 |
405-409 |
||
catalysts with HF-treated alumina as carrier |
164 |
21-25 |
||
173 |
461 |
|||
and isomerization of i- and n-octane over catalyst 5058 |
205 |
768 |
||
catalyst, tungsten-free |
202 |
590-599 |
||
of gas oil over various catalysts |
205 |
787 |
||
SPLITTING catalysts, tungsten-free, of the type of silica-aluminum-iron hydrated oxide mixtures, treated with HF |
257 |
926-933 |
||
Translation T-347 |
257 |
933a-933h |
||
Translation T-347 |
273 |
853-858 |
||
of coal oils in the vapor phase, tests on the zinc sulfide catalyst for, by Kaufmann and Schrader |
7 |
2732 |
1 |
50 42-50 53 |
17 |
29..661-29..672 |
|||
hydrogenation catalysts, new |
173 |
421-439 |
||
173 |
471-482 |
|||
201 |
368-381 |
|||
202 |
526-530 |
|||
570-575 |
||||
hydrogenation catalysts, study of, |
201 |
44-48 |
||
117-121 |
||||
with Cr2O3-containing catalyst effect of sulfur addition on |
173 |
647-649 |
||
hydrogenation catalysts with HF treated alumina as carriers, by Roetter; tungsten-free splitting catalyst of the SiO2-Al2O3-Fe2O3 mixtures treated with HF, by Gunther: splitting hydrogenation of DHD residues, by Gieg and Simon |
173 |
483-488 |
||
401-408 |
||||
366-392 |
||||
Translation, brief summaries, T-475 |
279 |
193-199 |
||
hydrogenation catalysts from iron fluoride upon bleaching earth as carrier |
173 |
596-600 |
||
hydrogenation, terrana-zinc sulfide-tungsten and terrana-zinc sulfide-molybdenum catalysts for, by Peters and Gunther |
173 |
541-548 |
||
Translation T-480 |
279 |
231-235 |
||
hydrogenation catalysts, tungsten require-ments for, |
181 |
6446-6452 |
||
Translation S-111 |
274 |
1802 |
||
hydrogenation catalysts free from tungsten |
173 |
410-415 |
||
401-408 |
||||
hydrogenation catalyst of iron fluoride on fullers earth |
202 |
408-412 |
||
hydrogenation with terrana-ZnS catalysts |
173 |
554-557 |
||
STARTING the converters with fresh catalyst |
5 |
2747 |
27 |
50 96 |
162 |
529-530 |
|||
SULFIDE vapor phase catalysts, especially tungsten sulfide for industrial hydrogenation of coal, by M. Pier |
119 |
30 30-30 72 |
||
SULFIDE vapor phase catalysts, especially tungsten sulfide for industrial hydrogenation of coal, by M. Pier |
212 |
20 44-20 72 |
||
vapor phase catalysts, in particular tungsten sulfide, Ludwigshafe, 1943 |
54 |
313-345 |
||
130 |
30 80 30 111 |
|||
Translation T-184 |
237 |
90 80-90 95 |
||
SYNTHETIC silicate, alumina and fullers earth aromatization catalysts |
165 |
381-397 |
||
166 |
469-492 |
|||
silicates and alumina - fullers earth |
165 |
281-297 |
||
TERRANA-iron fluoride catalysts, effect of sulfur addition to the |
173 |
592-596 |
||
202 |
436-439 |
|||
254 |
131-134 |
|||
catalysts, comparison of variously treated, |
146 |
232-233 |
||
T-52 plant, catalysts for the, |
78 |
164 |
||
TUNGSTEN carbide as hydrogenation catalyst |
173 |
465-470 |
||
sulfide |
162 |
665-666 |
||
668-677 |
||||
678-686 |
||||
844-846 |
||||
896-897 |
||||
catalyst, analytical evaluation of, |
254 |
330-332 |
||
sulfide as an isomerization catalyst for butane |
168 |
475 |
||
205 |
811-812 |
|||
sulfide and molybdenum catalysts in hydrogenation |
205 |
863-871 |
||
and molybdenum as catalysts for pressure hydrogenation, use of, |
254 |
152-160 |
||
sulfide-nickel catalyst, development of diluted |
205 |
730-732 |
||
sulfides and molybdenum as catalysts in pressure hydrogenation, application of, by Goehre, May 1943 |
257 |
886-893 |
||
Translation T-359 |
257 |
893a-893f |
||
Translation T-359 |
273 |
915-920 |
||
sulfide, reduction of, |
254 |
305-306 |
||
requirements with various catalyst combinations |
169 |
22 |
||
catalysts, research results with, |
254 |
50-52 |
||
results of experiments with |
201 |
316-319 |
||
sulfide, the splitting effect of, |
201 |
275 |
||
VAPOR phase catalysts |
201 |
42-43 |
||
, in particular WS2 |
205 |
872-880 |
||
VAPOR phase hydrogenation, development of poison resisting catalyst in, |
24 |
3..212-3..218 |
||
163 |
31-37 |
|||
181 |
6495-6505 |
|||
phase catalyst, current status of, |
148 |
242-243 |
||
WELHEIM vapor phase catalyst K 536, an example of preparation of, |
181 |
6615 |
||
catalyst and catalyst 7019, comparison of, |
202 |
44-47 |
||
ZINC sulfide catalysts |
7 |
50 42-50 53 |
||
Translation, Dr. Baer |
225 |
10 70-10 78 |