| Vapor Phase Catalysts (Con't) | ||||
|
TOM REEL |
BAG | ITEM | FRAMES | |
|
CHLORINE in the vapor phase injection feed |
130 |
ref. t |
30 64-30 79 |
|
|
Translation, T-183 |
237 |
90 67-90 79 |
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|
CHROMIUM-aluminum spherical catalysts |
13 |
3043 |
3 |
50 70-50 76 |
|
Translation S-1 |
274 |
1632-1633 |
||
|
oxide catalysts containing activator for aromatization |
46 |
1027-1028 |
||
|
COMPOSITION of catalysts, catalyst production in building 53. Manuscript supplied by Dr. Frese, T-291 |
273 |
577-595 |
||
|
CLAY cracking catalysts, natural and synthetic |
146 |
350-352 |
||
|
CRACKING catalysts, effects of alkali on the cleavage |
141 |
135-136 |
||
|
catalyst, alumina-boric acid |
50 |
423-425 |
||
|
appraisal of, |
162 |
31-34 |
||
|
fluidized. Experiments with SiO2-Al2O3 catalysts |
162 |
35-71 |
||
|
catalysts, observation on, |
164 |
561-565 |
||
|
168 |
565-566 |
|||
|
and hydroforming, Leuna research on, |
125 |
311-313 |
||
|
3rd series |
||||
|
catalysts, exploratory search for, |
141 |
13-22 |
||
|
for the Moosbierbaum plant |
174 |
306-320 |
||
|
hydrogenation and dehydrogenation with Ni, Pt, Pd, Fe, Co and Cu |
168 |
525-530 |
||
|
catalyst, silica-magnesia, influence of conditions of precipitation on gasification |
141 |
65-68 |
||
|
with synthetic aluminum silicate |
126 |
1227-1239 |
||
|
catalytic, of synthesis LPG with aluminum hydrosilicate catalysts, 1944 |
47 |
1059-1168 |
||
|
catalytic catalysts, 1935 |
177 |
2247-2270 |
||
|
of middle oils with different catalysts |
147 |
170-175 |
||
|
catalytic with aromatization catalysts |
146 |
132-133 |
||
|
catalyst, preparation of synthetic |
146 |
53-68 |
||
|
146 |
137-138 |
|||
|
146 |
435-436 |
|||
|
162 |
283-284 |
|||
|
catalytic catalysts, directions for the preparation of |
65 |
9..71 |
||
|
catalyst, use of polymerization sludge for paraffin waxes |
60 |
713-727 |
||
|
and hydrocarbon conversion, observations on catalysts for, |
181 |
|||
|
Translation T-189 |
237 |
90 123-90 126 |
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|
catalyst, magnesium silicate |
146 |
537-538 |
||
|
moving |
167 |
260-264 |
||
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petroleum at 50 atm, experiments on catalyst for, |
147 |
155-162 |
||
|
catalytic, with Zn-containing catalysts |
141 |
222-224 |
||
|
catalysts, isomerizing action of, |
167 |
319-321 |
||
|
DEHYDROGENATION and aromatization, catalysts for, by Wiedemann |
71 |
937-939 |
||
|
catalysts |
14 |
1118-1119 |
||
|
14 |
1294-1301 |
|||
|
Translation |
143 |
30 49-30 55 |
||
|
DEHYDROGENATION catalysts, experiments with |
125 |
275-288 |
||
|
3rd series |
||||
|
169 |
442-449 |
|||
|
at 50 atm. catalyst tests, starting with NiW |
202 |
53-55 |
||
|
composition of Al2O3-MoO3 catalysts for, |
126 |
445-473 |
||
|
catalyst, development of alumina-molyb-denum-nickel |
164 |
729-751 |
||
|
hydrogenation, and cracking with Ni, Pt, Pd, Fe, Co, and Cu |
168 |
525-530 |
||
|
catalyst molybdenum and alumina, composition of, |
126 |
445-473 |
||
|
catalysts, preparation of specially active |
125 |
215 |
||
|
3rd series |
||||
|
catalysts, reworking of spent |
18 |
22..112-22..114 |
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|
testing of, |
125 |
236-244 |
||
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3rd. series |
||||
|
in 100 ml. converter, testing of, |
126 |
483-497 |
||
|
|
148 |
21-29 |
||
|
, preliminary comparison of catalyst 7612 with 7360 at 350° in, |
169 |
67-69 |
||
|
and aromatization catalysts, by Wiedemann |
71 |
937-939 |
||
|
catalysts, report of tests of a drying oven for, |
177 |
2479-2485 |
||
|
DEVELOPMENT, historical, of catalysts (chronology) |
254 |
149-151 |
||
|
DHD catalysts |
75 |
779-789 |
||
|
damage to, by oxygen, nitrogen, sulfur compounds and by unsaturated compounds |
169 |
354-382 |
||
|
catalyst from dismantled stall |
75 |
778 |
||
|
testing of, in 1 li converter |
162 |
408-422 |
||
|
169 |
383-395 |
|||
|
251 |
964-978 |
|||
|
physical inspection of, |
251 |
1048-1052 |
||
|
10 mm. pills, new |
75 |
773-777 |
||
|
testing (from technical alumina) |
251 |
804-817 |
||
|
, note on the question of second heating of, after saturation with ammonium molybdate |
169 |
396 |
||
|
catalyst, alumina Op (k 7360) and alumina Zu (K-7935), tests of, |
126 |
475-480 |
||
|
catalyst, testing of, |
126 |
507-534 |
||
|
221 |
80 64-80 66 |
|||
|
90 75-90 100 |
||||
|
251 |
1030-1047 |
|||
|
1080-1087 |
||||
|
DHD catalysts, testing of activity of industrial in 100 ml reactors |
125 |
90-116 |
||
|
3rd series |
||||
|
169 |
257-266 |
|||
|
267-272 |
||||
|
277-291 |
||||
|
169 |
612-625 |
|||
|
162 |
935-942 |
|||
|
catalysts, testing of three |
125 |
207-213 |
||
|
3rd series |
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|
K 7360, evaluation of alumina with respect to activity, splitting and iodine number in conversion to, |
125 |
202-205 |
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|
3rd series |
||||
|
manufacturing and catalyst requirements |
23 |
2..19-33 |
||
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EQUILIBRIUM of aromatics-naphthenes, regulation of, over catalyst 5058 |
205 |
781-786 |
||
|
FLUORIDE catalysts |
173 |
462-464 |
||
|
tests with differently prepared |
173 |
440-441 |
||
|
173 |
538-540 |
|||
|
stability of, in the presence of H2S and H20 in view of their catalytic action |
253 |
276-278 |
||
|
FULLERS earth, activation of, |
50 |
420-422 |
||
|
146 |
648 |
|||
|
synthetic silicate, and alumina catalysts for aromatization |
165 |
381-397 |
||
|
166 |
469-492 |
|||
|
earth superfiltrol as compared to the Bavarian analogue terrana in catalytic cracking of gas oil |
126 |
1291-1293 |
||
|
HYDROFORMING catalysts |
56 |
20 |
216-219 |
|
|
and cracking catalysts, Leuna research on |
125 |
311-313 |
||
|
3rd series |
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|
HYDROGENATION, dehydrogenation and cracking with Ni, Pt, Pd, Fe, Co, and Cu |
168 |
525-530 |
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|
, use of Mo and W sulfide catalyst in, |
205 |
863-871 |
||
|
254 |
152-160 |
|||
|
, pressure, application of Mo and W sulfides as catalysts, by Goehre, May, 1943 |
257 |
886-893 |
||
|
Translation T-359 |
257 |
893a-893f |
||
|
273 |
916-920 |
|||
|
activity of various Al2O3-W-Ni catalysts for, |
254 |
433-438 |
||
|
IRON-W-Ni catalyst 6719, improving |
169 |
209-217 |
||
|
236-241 |
||||
|
ISOMERIZATION and splitting of i-and n- octane over catalyst 5058 |
205 |
768 |
||
|
LOSS of catalyst in middle oil operations |
165 |
419-425 |
||
|
MAGNESIUM silicate cracking catalysts |
146 |
537-538 |
||
|
catalysts -Co, examination of, |
162 |
271-278 |
||
|
silicate catalysts, types of, |
141 |
128-130 |
||
|
MOLYBDENUM dioxide operation of Ludwig-shafen, catalyst test for, |
254 |
476-477 |
||
|
and W sulfides as catalysts in pressure hydrogenation, by Goehre, May 1943 |
257 |
886-893 |
||
|
Translation T-359 |
257 |
893a-893f |
||
|
Translation T-359 |
273 |
915-920 |
||
|
and tungsten sulfide catalysts in hydrogenation |
205 |
863-781 |
||
|
254 |
152-160 |
|||
|
NICKEL content on catalysts, effect of, |
167 |
526-527 |
||
|
NITROGEN content, effect of on splitting properties. Two papers |
257 |
934-936 |
||
|
257 |
937-947 |
|||
|
Translation T-353-1 |
257 |
936a-936d |
||
|
Translation T-353-2 |
257 |
947a-947j |
||
|
Translation T-353-1 |
273 |
880-884 |
||
|
Translation T-353-2 comparison of |
273 |
884-892 |
||
|
and production trouble,/sensitiveness to, of catalysts 8797 and 6434 |
173 |
563-564 |
||
|
sensitivity of catalysts, experiments to determine |
173 |
880-884 |
||
|
Translation T-197 |
237 |
100 49-100 51 |
||
|
sensitivity of terrana-tungsten sulfide catalysts to, |
173 |
650-654 |
||
|
POLYMERIZATION duration test on a repre-sentative sample of the H3PO4 catalyst |
48 |
819-827 |
||
|
Translation S. O. Co. (Indiana) |
243 |
30 33-30 35 |
||
|
PREHYDROGENATON, catalysts for, |
167 |
466-474 |
||
|
480-482 |
||||
|
483 |
||||
|
484-487 |
||||
|
499-503 |
||||
|
513-515 |
||||
|
516-525 |
||||
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532-542 |
||||
|
543-547 |
||||
|
548-550 |
||||
|
580-583 |
||||
|
584-587 |
||||
|
593-600 |
||||
|
624-645 |
||||
|
646-656 |
||||
|
657-664 |
||||
|
(Continued on Page 84) |
668-669 |
|||
|
PREHYDROGENATON, catalysts for, |
167 |
670 |
||
|
677-678 |
||||
|
696-697 |
||||
|
698-701 |
||||
|
706-708 |
||||
|
709-714 |
||||
|
719-725 |
||||
|
734-740 |
||||
|
760-763 |
||||
|
804-807 |
||||
|
812-826 |
||||
|
951-959 |
||||
|
1024-1033 |
||||
|
1034-1045 |
||||
|
catalysts, Al-Mo-Ni and Al-W-Ni |
164 |
235-237 |
||
|
169 |
16-21 |
|||
|
, development of, Ludwigshafen, 1940 |
7 |
2732 |
2 |
176-178 |
|
130 |
40 1-40 24 |
|||
|
165 |
199-221 |
|||
|
Translation T-140 |
237 |
70 114 |
||
|
Translation T-185 |
237 |
9096-90 101 |
||
|
catalysts, development of, to catalyst 7745 |
169 |
201-208 |
||
|
catalysts, experiments on, in particular 8376 |
202 |
639-650 |
||
|
of middle oil, catalysts for, |
165 |
171-190 |
||
|
165 |
225-241 |
|||
|
alumina catalysts, effects of W, Ni, Co, and Fe |
165 |
1-9 |
||
|
(Illegible) |
21-29 |
|||
|
Al203-W-Ni catalyst 8376 (7846 W 250) |
148 |
383-394 |
||
|
catalysts, new |
202 |
484-497 |
||
|
543 |
||||
|
catalyst, iron, tungsten, nickel, and cobalt, effects on |
201 |
77-85 |
||
|
catalysts, effects of W, Ni, Co, and Fe on, |
167 |
488-494 |
||
|
504-512 |
||||
|
201 |
77-85 |
|||
|
catalysts obtained by diluting 5058 catalysts with ZnS |
164 |
130-132 |
||
|
, present status of experiements on, |
169 |
224-225 |
||
|
catalysts, testing of, |
165 |
55-58 |
||
|
133-143 |
||||
|
202 |
273-281 |
|||
|
testing some |
201 |
250 |
||
|
in 50 ml lead bath converters |
202 |
404-407 |
||
|
REFERENCES, literature, to a lecture on catalysts |
168 |
550 |
||
|
REGENERATON of aromatization catalysts |
49 |
35-39 |
||
|
of cracking catalysts, tests and theory of, |
177 |
2293-2355 |
||
|
188 |
20111-20173 |
|||
|
of moving catalyst in catalytic cracking process |
190 |
23620-3681 |
||
|
REFINING catalyst for aviation gasoline and other products, Al2O3-W-Ni |
253 |
928-936 |
||
|
RUHROEL catalysts, comparison with 7019 |
7 |
60 28-60 31 |
||
|
Translation, Dr. Baer |
225 |
10 51 |
||
|
catalysts K413, preliminary notes on experiments with, in Leuna |
7 |
50 13-50 17 |
||
|
Translation, Dr. Baer |
225 |
10 91-10 94 |