T.O.M. Microfilm Reel 254
(Original designation BM-40)
Table of Contents
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XXVI. Vapor phase – hydrogenation.
Item No.
20. Basis for evaluation of aromatization research. Frames 1-4
21. Troubles in vapor phase stalls. Frames 5-7
22. 45 atm. aromatization with deteriorating activity. Frames 8-11
23. Saturation with 7846 catalyst. Frame 12
24. H2S addition in vapor phase. Frames 13-16
25. Semi technical work on saturation of bituminous coal hydrogenation middle oil and gasoline over 7846W250. Frames 17-39
26. The activity peak with 5058. Frame 40
27. Data (descriptive) on different catalysts. Frames 41-47
28. Catalytic behavior of the system cilicic acid-alumina-iron during hydro-carbonization conversion reactions. Frames 48-49
29. Research results with tungsten catalysts. Frames 50-52
30. Splitting catalyst for catalytic high pressure hydrogenation. Frames 53-54
31. ANIC catalysts. Frames 55-56
32. Gasoline quality for the Japanese plant. Frames 57-59
33. About catalyst 7846W250. Frames 60-65
34. Aromatization at 250 atm. with alumina- fuller’s earth catalyst 8688. Frames 66-73
35. Operations with 7846 and 5058 catalysts. Frames 74-79
36. Effect of oil partial pressure, throughput and contact time on the results of saturation with 7846. Frames 80-91
37. New splitting catalysts. Frames 92-103
38. Translations from Russians – “Recovery of high octane gasoline by hydrogenation.” Frames 104-130
39. Influence of sulfur with fuller’s earth- iron fluoride catalysts. Frames 131-134
40. Production of hydrocarbon gases by hydrogenation. Frames 135-138
41. Crystal structure and X-ray investigations of tungsten sulfide structure. Frames 139-140
42. Reactions which do not alter the carbon skeleton. Frame 141
43. WS2 as technical catalyst and chemical compound (physical data). Frames 142-144
44. Electron-diffraction relations of WS2. Frames 145-146
45. On the question of the existence of an amorphous intermediate state in the production of WS2 catalyst from ammonia-sulfo-tungstate. Frames 147-148
46. Historical development of catalysts (chronology). Frames 149-151
47. Use of Mo and W sulfides as catalysts for pressure hydrogenation. Frames 152-160
48. Influence of added nitrogen compounds on the results when splitting petroleum gas oil over 6434. II. Frames 161-162
49. Testing new saturation catalysts. Frames 163-166
50. Testing of composite samples of 5058, 8376, 6434. Frames 167-169
51. The temperature-dependence of reactions which occur in the hydrogenation of bituminous coal liquefaction middle oil over 5058, 7846 and 8376 (7846W250). Frames 170-185
52. Exchange of experience on saturation catalyst 8376. Frames 186-206
53. Processing crude oil by pressure distillation and cracking at 50 atm. Frames 207-209
54. Tungsten carbide as a hydrogenation catalyst. Frames 210-212
55. Saturation of Leuna gasoline and middle oil with the new 7846 catalyst. Research in 200 cc. converter. Frames 213-225
56. Use of 8676 (7846W250) for various products. Frames 226-242
57. Position taken on the fluoride-patent of the ANIC catalyst. Frames 243-245
59. Politz problem of common processing of petroleum residues and bituminous coal tar-a-middle oil in the gas phase. Frames 253-268
60. Production of low endpoint (100°C.) gasoline (due to scarcity of iso-octane). Frames 269-274
61. Aromatization of middle oil from bituminous coal liquid phase. Frames 275-277
62. 600 atmospheres aromatization. Frames 278-280
63. Further research in the domain of alumina- Mo-Ni catalysts. Frames 281-288
64. Research to refine heavy benzol with alumina-Mo-Ni catalyst in 1 liter converter. Frames 289-297
66. Effect of temperature on yield with various concentrations of saturation catalysts. Frames 303-304
67. Reducing tungstic acid. Frames 305-306
68. How to make 6434 catalyst. Frames 307-308
69. Splitting and DHD treatment of bituminous coal middle oil over saturation catalyst 7846W250. Frames 309-326
70. Splitting and isomerization of iso-octane and N-heptane over 5058. Frame 327
71. Action of sulfur in high pressure hydrogenation. Frames 328-329
72. Analytical evaluation of WS2 catalyst. Frames 330-332
73. Leuna discussion of catalysts. Frames 333-338
74. Comparison of splitting of natural fuller’s earth and synthetic silicates at 250 and 600 atm. Frames 339-348
75. Aromatization of dephenolized middle oil (Scholven) over 7019. Frames 349-356
76. Tests of feed stocks of different origin for 7019. Frames 357-358
77. Comparison between natural fuller’s earth (6109) and synthetic aluminum silicate (6752) at 600 atm. Frames 359-363
78. Influence of temperature and throughput in the one step 600 atm. aromatization of bituminous coal liquefaction middle oil with fuller’s earth catalyst. Frames 364-371
79. Calculations on the question of 300 vs. 700 atm. Frames 372-374
80. High load gasoline from bituminous coal using DHD as final step. Frame 375
81. Crystal structure of WS2 catalyst. Frames 376-381
82. Effect of recycle rate on 250 atm. aromatization of middle oil from bituminous coal liquefaction over alumina-fuller’s earth catalyst 8688. Frames 382-390
83. Aromatization at 250 atm. with alumina-fuller’s earth catalyst of the 8688 type. Frames 391-404
84. Splitting catalysts from iron sulfide on fuller’s earth. Frames 405-409
85. Variation of knock rating with different distillation fraction in 250 atm. splitting over 6434 catalyst. Frames 410-417
86. The ANIC fluoride catalyst compared with 6434. Frames 418-423
87. Discussion on ANIC catalyst operations. Frames 424-426
88. Comparison of 6434 and 6752 in aromatization processes. Frames 427-432
89. Activity of various alumina-W-Ni catalysts for hydrogenation. Frames 433-438
90. 2-stage 300 atm. gas phase gasoline from various raw material and with various saturation catalyst. Frames 439-445
91. Sulfur addition in splitting over 6434. Frames 446-448
92. Action of W, V, Ni, Co, and Fe as active components on alumina saturation catalysts. Frames 449-457
93. Influence of the carrier on the results of 6434 splitting. Frames 458-461
94. Heavy oil splitting over fixed catalysts at 250-600 atm. Frames 462-473
95. Hydrogenation of crude wax. Frames 474-475
96. Catalyst test for the MoO2 operation of Ludwigshafen. Frames 476-477
97. Reasons for difference in quality of residue gasoline from aromatization. Frames 478-487
XXVII. Various organic processes.
1. Hydrogenative splitting of natural rubber and buna. Frames 489-490
2. Synthesis of branched hydrocarbons (tri-alkylcarbinol). Frames 491-493
3. Processes for high test pure hydrocarbons. Frames 494-496
4. Process for condensation products. Frames 497-503
5. Polybutylene rubber. Frames 504-511
6. Making alcohol from Michael Process products. By Bueren. February 3, 194. Frames 512-515. 4 pages.
7. WS2 for perhydrogenation of polynuclear aromatics. Frames 516-525
9. Ketone and hydrocarbon synthesis using AlCl3 and CaCl3. Frames 530-532
10. Hydrogenation of isobutyron over catalyst 7878. Frames 533-537