|
CATALYSTS |
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|
TOM |
BAG |
ITEM |
FRAMES |
|
|
ACETONE by reaction of acetylene with steam, catalysts for production of |
32-II |
2078 |
183.1498-183.1503 |
|
|
ACTIVATION of catalysts for hydrogenation of carbon monoxide, R 686 |
37 |
3451 |
36 |
40 110-40 115 |
|
177 |
1493-1495 |
|||
|
ACTIVE masses, similar to fullers earth, production of, O.Z. 14,296 |
17 |
39..1141-39..1144 |
||
|
ALUMINA-chromium oxide catalysts, Wiedemann |
71 |
943-948 |
||
|
ALUMINUM oxide-chromium oxide catalysts, R 560 |
39 |
3453 |
1 |
80 52 |
|
AROMATIZATION or dehydrogenation catalysts, R 687 |
36 |
3454 |
20 |
20 56-20 62 |
|
37 |
3451 |
36 |
40 116-40 122 |
|
|
, process for production of catalysts of maximum activity for, R 440 |
41 |
2744 |
14 |
40 46-40 48 |
|
and dehydrogenation catalysts, Wiedemann |
71 |
937-939 |
||
|
Do., R 687 |
36 |
3454 |
20 |
20 56-20 62 |
|
37 |
3451 |
36 |
40 116-40 122 |
|
|
CATALYST residues produced in polymerization of olefins to lubricating oils by means of aluminum chloride, utilization of, R 683 |
37 |
3451 |
36 |
40 104-40 106 |
|
CATALYSTS, separation of from liquids and re-introduction with fresh starting material, O.Z. 13,955 |
17 |
40..1193-40..1196 |
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|
CHROMIUM oxide - alumina catalyst, Wiedemann |
71 |
943-948 |
||
|
CLAY-containing catalyst, production of, O.Z. 11,583 |
17 |
39..1087-39..109* |
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|
COBALT-magnesium catalyst, preparation of for conversion of carbon monoxide-hydrogen mixtures, R 360 |
37 |
3451 |
35 |
30 111-30 113 |
|
CRACKING catalyst, Al2O3-boric acid |
50 |
423-425 |
||
|
CUPRIC oxide - chromium oxide catalysts |
54 |
703-704 |
||
|
DEHYDROGENATION and aromatization, catalysts for, Wiedemann |
71 |
937-939 |
||
|
catalysts, production of active, R 700 |
37 |
3451 |
36 |
50 34-50 37 |
|
or aromatization catalysts, R 687 |
36 |
3454 |
20 |
20 56-20 62 |
|
37 |
3451 |
36 |
40 116-40 122 |
|
|
DHD catalyst, covering by Raschig rings |
76 |
830-831 |
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|
ELECTROLYTIC cobalt |
41 |
2744 |
30 |
50 130-50 132 |
|
EXTRACTION of deposits on catalyst, arrangement of extraction, especially of, Krupp, K 160 |
177 |
1769-1785 |
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|
GRANULAR catalyst, treating gases or vapors with |
17 |
40..1228-40..12** |
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|
GRINDING of fibrous masses, low-fines, in particular during preparation of catalysts, R 626 |
36 |
3454 |
36 |
60 49-60 53 |
|
177 |
1504-1508 |
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|
INTERFERENCE discussions on process for production of rigid catalyst from silica-containing materials |
8 |
2732 |
3 |
10 96-10 98 |
|
IRON catalysts for production of predominantly olefinic and oxygen-containing hydrocarbons in hydrogenation of carbon monoxide, R 667 |
36 |
3454 |
36 |
70 32-70 35 |
|
177 |
1485-1488 |
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|
synthesis catalyst, process for preparation of, W. Herbert, to Metallgesellschaft A.G. |
35 |
3440 |
64 |
0 13-0 19 |
|
IRON catalysts, high activity, for hydrogenation of carbon monoxide, production of |
177 |
1644 |
||
|
Do., R 469 |
1695-1703 |
|||
|
Do., R 490 |
1704-1708 |
|||
|
Do., R 506 |
1709-1714 |
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|
Do., R 581 |
1686-1694 |
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|
synthesis catalysts, preparation of, patent application and correspondence |
100 |
70 34-70 77 |
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|
LIQUID phase catalyst, O.Z. 14,226 |
28 |
2171 |
5..345-5..346 |
|
|
LOW temperature iron catalysts, production of, R 670 |
36 |
3454 |
36 |
70 44-70 47 |
|
177 |
1489-1492 |
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|
MAGNESIA, pure, suitable for manufacture of catalysts, preparation of, R 641 |
36 |
3454 |
36 |
60 97-60 99 |
|
177 |
1478-1480 |
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|
MAGNESIUM-containing catalyst for gasoline synthesis, R 306 |
37 |
3451 |
35 |
30 85-30 87 |
|
MASSES for use as catalyst or adsorbents, method of preparation of, O.Z. 13,149 |
28 |
2171 |
5..319-5..320 |
|
|
METALS in catalytic processes, recovery of, O.Z. 14,850 |
32-II |
2078 |
216.1661-216.1664 |
|
|
MIXED iron synthesis catalyst, patent application on and correspondence |
100 |
20 77-20 83 |
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|
20 96-20 100 |
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|
70 13-70 33 |
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|
PHOSPHATIC catalysts, method of preparation of, O.Z. 13,385 |
28 |
2171 |
5..331-5..333 |
|
|
PHOSPHORIC acid catalysts, preparation of, O.Z. 12,413 |
17 |
39..1128-39..1132 |
||
|
20 |
159.2578-159.2582 |
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|
POLYMERIZATION of unsaturated compounds, process for preparation of active catalyst for |
8 |
2732 |
3 |
0 59-0 60 |
|
PRODUCTION of surface-active materials, in particular catalytically active materials, O.Z. 14,345 |
17 |
39..1118-39..1121 |
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|
20 |
164.2638-164.2641 |
|||
|
REACTIVATION of catalysts, O.Z. 13,565 |
17 |
32..890-32..893 |
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|
Do., O.Z. 13,723 |
39..1109-39..1117 |
|||
|
54 |
848-849 |
|||
|
18 |
||||
|
Translation |
144 |
10 97-10 98 |
||
|
REACTIVATION of catalyst for gasoline synthesis, R 373 |
37 |
3451 |
35 |
30 122-30 123 |
|
of catalyst for hydrogenation of carbon monoxide, R 416 |
37 |
3451 |
35 |
40 50-40 52 |
|
of catalyst with oxygen-containing gases, O.Z. 13,255 |
17 |
39..1103-39..110* |
||
|
20 |
152.2588-152.259* |
|||
|
of thorium for catalyst manufacture from iron-thorium sludges, R 725 |
37 |
3451 |
36 |
50 118-50 121 |
|
REACTIVE TiO2, preparation of, O.Z. 13,069 |
28 |
2171 |
5..309-5..310 |
|
|
REDUCTION of catalyst, R 407 |
37 |
3451 |
35 |
40 32-40 33 |
|
of iron-containing catalysts |
134 |
70 125-70 127 |
||
|
of powdered catalysts, O.Z. 13,542 |
134 |
100 70 100-75 |
||
|
RIGID catalyst from silica-containing materials, preparation of |
8 |
2732 |
3 |
20 17-20 23 |
|
SEPARATION of catalysts from liquid and their re-introduction with fresh starting material, O.Z. 13,955 |
17 |
40..1193-40..119* |
||
|
SHAPED catalysts or adsorption materials, manufacture of, O.Z. 13,043 |
20 |
151.2583-151.258* |
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|
SYNTHESIS of liquid and solid hydrocarbons, catalysts for, by W. Gross to Metallgesellschaft A.G. |
35 |
3440 |
64 |
0 53-0 61 |
|
THORIUM, recovery of, R 408 |
37 |
3451 |
35 |
40 34-40 36 |
|
Do., R 413 |
40 37-40 42 |
|||
|
WASTE products of alumina manufacture, production of catalysts of high activity from, R 548 |
177 |
1645 |
||
|
1714-1721 |
||||
|
1752-1759 |
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|
ZINC oxide catalysts for dehydration of secondary alcohols, Wiedemann |
71 |
985-989 |