VAPOR PHASE CATALYSTS

ALKALI, effect of, on cleavage by cracking catalyst

141

135-136

ALUMINA, active as catalyst carrier

125

217-222

(3rd. series)

“ catalysts, discussion of, Oppau, July 1943

169

158-200

“ catalysts for prehydrogenation, effect of W, Ni, Co, and Fe

165

1-9

(Illegible)

21-29

202

442-459

“ fullers’ earth and synthetic silicate catalysts for aromatization

165

381-397

166

469-492

“ boric acid cracking catalyst

50

423-425

“ Mo catalyst for dehydrogenation, composition of,

126

445-472

“ fullers’ earths and synthetic silicates

165

281-297

“ Mo-Ni catalysts

165

191-198

“ molybdneum-nickel catalyst, development of dehydrogenation catalyst

164

729-751

“ Mo-Ni catalysts, further research in,

148

565-572

254

281-288

“ molybdenum-nickel and alumina-tungsten nickel prehydrogenation catalysts

164

235-237

169

16-21

“ saturation catalysts, action of W, V, Ni, Co and Fe as active components on,

254

449-457

“ terrana catalysts, aromatization

165

285-298

166

363-374

“ tungsten-nickel catalysts, activity of diffe-rently prepared

202

237-242

“ W-Ni catalysts for hydrogenation, activity of,

254

433-438

“ W-Ni catalyst for various products, use of,

165

30-54

165

98-132

165

144-149

“ nickel-tungsten catalysts, the effect of nickel content on the activity of,

202

243-244

“ and MoO3 catalyst for dehydrogenation, composition of,

126

445-473

“ W-Ni prehydrogenation catalyst 8376, (7846 W 250 for) various products, the use of,

148

383-394

ALUMINA-W-Ni catalyst, research to refine aviation gasoline and other products over,

253

928-936

“ W-Ni catalyst testing on various products

202

282-374

ALUMINUM chloride catalyst, partially hydrated

126

1267-1268

“ chloride, catalytic cracking of B middle oil, produced by,

126

1245-1248

“ hydro silicate catalyst, 1944, laboratory test on catalytic cracking of synthesis LPC with,

47

1059-1168

ANIC catalysts

173

418-420

454-460

507-512

513-516

519-525

526-528

254

243-245

255-265

424-426

“ “ 1941, discussions of,

173

529-537

“ experiments with fluoride treated catalysts

164

123-129

“ fluoride catalyst compared with 6434

254

418-423

AROMATIZATION catalysts

50

573

165

359-380

165

469-483

166

406-408

166

412-427

166

428-441

“ catalysts, development of,

165

259-280

“ catalysts on a lab scale

47

1006-1010

“ with alumina-terrana catalysts

165

285-298

166

363-374

“ catalyst, chromic fluoride as,

166

469-492

“ “ development of alumina fullers’ earth and synthetic silicate for

165

381-397

166

408a-4408c

“ catalyst 8688 at 250 atm. Preliminary results

148

185-187

“ catalysts for 600 atm from previously used 6434

164

8-16

“ catalyst, chromic fluoride as

166

408a-408c

“ “ containing chromic oxide as activator

46

1027-1028

“ catalysts, spent 6434 as source of,

181

6460-6468

“ catalysts of synthetic silicate, alumina and fullers’ earth

165

381-397

166

469-492

AROMATIZATION, testing of catalyst for,

165

337-341

342-356

“ catalysts by dehydrogenation testing of,

165

503-505

500-502

166

493-517

518-539

“ catalysts, use of UO2 in

165

492-499

“ “ recovery of spent chromium oxide

50

489-500

“ “ regeneration of,

49

35-39

“ and dehydrogenation catalysts, Wiedemann

71

937-939

“ catalyst, K-7360 and K7638, comparison of,

125

267-270

3rd series

“ effect of catalyst components on,

165

518-522

“ with fullers’ earth or silica base catalysts, quality of gasolines

181

6508-6510

“ of middle oil over catalyst 8688, influence of the partial pressure of the products on,

166

349-353

BUTADIENE production, dehydrogenating catalyst for,

14

1292-1293

Translation

143

30 ‘47-30 ‘48

BUTANE dehydrogenation, etc., catalyst discussion:

251

130-133

“ dehydrogenation catalysts, uniform testing methods for,

14

1128-1129

n-BUTANE, dehydrogenation catalyst for,

57

12-27

35-39

52-58

BUTANE and propane, dehydrogenation of,

28

2171

3..112-3..113

“ isomerization catalyst, tungsten sulfide for

168

475

205

811-812

BUTOL, dehydrogenation catalysts for, Huls

55

375-383

CATALYST 5058 activity peak

254

40

“ “ disintegration of,

75

884-901

“ “ diluting with ZNS to obtain prehydrogenation catalyst

164

130-132

“ 5058, effects of density and size of pellets on the splitting hydrogenation and prehydrogenation with,

201

368-381

“ 5058 in heating tests at normal pressure, the effect of temperature upon,

5

2747

27

60 ‘1-60 ‘9

“ 5058, influence of the size of pellets on the splitting activity of,

205

602-604

805-807

Translation T-264

273

386-387

808-810

CATALYST 5058, influence of grain or pellet size on the splitting activity, by Peters and Trofimoff.

205

802-807

Translation T-264

273

386-387

“ 5058, effect of density and size of pellets on splitting and saturation

257

867-878

Translation T-322

257

878a-878k

273

734-744

“ 5058, 100 atm experiments on gas oil over

205

792-799

“ 5058, notes on preparation for,

162

626-627

“ “ log of, Scholven, drawing

89

2747 (43 & 44)

0 ‘24-0 ‘25

“ “ regulation of the aromatics - naphthenes equilibrium over

205

781-786

“ 5058 samples of various densities, comparison of performance of,

205

800-801

“ 5058, splitting and isomerization of i - and n-octane over

205

768

“ 5058, substituted by other catalysts

126

756-761

“ “ testing from the Gelsenberg high pressure stall 304

5

2747

27

50 ‘83-50 ‘93

“ 5058 and 6434, comparative tests with run in Gelsenberg and Scholven

202

1-9

“ 5058 and 7846 and their combination, comparison of, Poelitz, 1943

130

40 ‘25-40 ‘48

“ 5058 and 7846, combination of,

210

382-384

“ “ 8376, 6434, testing of composite samples of,

254

167-169

“ 5058, 6619, and 7846 for prehydrogenation

126

1122-1124

“ 5058 and 7846, operations with

254

74-79

“ “ 7846 (Mo) and 8376 (7846 W 250) temperature dependence of reactions of middle oil hydrogenation with,

218

90 ‘80-90 ‘96

“ 5058 and 8376 for Fischer process product

162

687-691

“ 6108 and 6752 for catalytic cracking in 40 li converters

126

1125-1149

“ 6108

75

769-770

Translation, Phillips Petr. Co.

245

20 ‘38-20 ‘39

“ 6108, tests with on Iraq naphtha

126

716-728

“ 6109 (natural fullers’ earth) compared with catalyst 6752 (synthetic aluminum silicate, at 600 atm.

148

560-564

254

359-363

“ 6434, comparison with ANIC fluoride catalyst

254

418-423

“ 6434, comparison of gasolines from B middle oil with catalyst 6752 at 250 and 600 atm with,

147

95-101

“ 6434, composition and preparation of,

173

409

CATALYST 6434, curves of behavior of, during hydrogenation

181

6595-6602

“ 6434, damage to in the splitting unit feed by a temporary introduction of the dehydrogenation feed

75

816-819

“ 6434 the effect of sulfur addition on splitting hydrogenation

173

558-560

201

263-265

202

585-589

“ 6434, observations during operation of, on sulfurized middle oil, by Kuppinger

181

6777-6803

“ 6434, Poelitz experience with,

3

2745

18

70 ‘8

“ “ influence or organic nitrogen compounds on splitting with,

162

401-405

“ 6434 in recycle gas stream

75

791-813

Translation, Phillips Petr. Co.

245

20 ‘48-20 ‘58

181

6733-6777

Translation T-127

237

60 ‘125-60 ‘143

“ 6434, regeneration of,

5

2747

27

50 ’94-50 ‘95

75

814-815

“ “ replacing terrana with synthetic silicates

173

549-553

“ 6434, testing regenerated

202

66-69

393-395

440-441

“ “ and 5058, comparative tests with run in Gelsenberg and Scholven

202

1-9

“ 6434 and 6719, I. G., notes on,

23

3424

6

6..380-6..383

“ “ and 6752, comparison of,

254

427-432

“ “ and 7846, specific data on vapor phase

89

2747

38

0 ‘19

“ 6434, 5058, 8376, testing of composite samples of,

254

167-169

“ 6434 and 8797, comparison of sensitivity to nitrogen and to operational disturbances of,

173

563-564

“ 6612

75

580-582

Translation, Phillips Petr. Co.

245

20 ‘9-20 ‘10

“ 6619, 7846, and 5058 for prehydrogeneration

126

1122-1124

“ 6718 and 7360, comparison of treatment of heavy naphtha from coal, brown coal tar, mixed base petroleum (straight run) with,

126

657-662

“ 6719 and 6434, I.G., notes on,

23

3424

6

6..380-6..383

“ “ improving the Fe-W-Ni

169

209-217

“ “ Fe-W-Ni, improving

169

209-217

236-241

“ “ and 6434, I. G., notes on,

23

3424

6

6..380-6..383

CATALYST 6752, comparison of, with catalyst 6434

254

427-432

“ 6752, comparison of gasolines from B middle oil at 250 and 600 atm. with catalyst 6434

147

95-101

“ 6752 (synthetic aluminum silicate) compared with catalyst 6109 (natural fullers’ earth) at 600 atm

148

560-564

254

359-363

“ 6752 and 6108 for catalytic cracking in 40 li converters

126

1125-1149

“ 7019, vapor phase, summary of reports on experiments with, Ruhroel

7

60 ‘9-60 ‘23

Translation, Dr. Baer

225

10 ‘52-10 ‘69

“ 7019, comparison with Ruhroel catalysts

7

60 ‘28-60 ‘31

Translation, Dr. Baer

225

10 ‘51

“ 7019 in normal operations with coal lique-faction middle oil

169

45-51

“ 7019, detailed report on experiments with, at Ludwigshafen

7

2732

1

50 ‘18-50 ‘41

“ 7019 and the Welheim catalyst, comparison of,

202

44-47

“ 7019

166

463-468

“ “ at 300 atm with 346/349 at 600 atm, comparison of,

7

60 ’28-60 ‘31

Translation, Dr. Baer

225

10 ‘95-10 ‘96

“ 7019 (Scholven) by Urban

76

996-998

“ “ , replacing vanadium with ZnO - MoO3 or ZNO - MgWO4

169

23-30

“ 7019 for the bleaching

165

357-358

“ 7019-L-8, conversion of coal-liquefaction middle oil into aromatic gasoline with, by Simon and Sussenguth

75

687-735

“ 7360, data sheet on,

75

772

“ “ and 6718, comparison of treatment of heavy naphtha from coal, brown coal tar, mixed base petroleum (straight run) with

126

657-662

“ 7360, comparison of with catalyst 7638 as aromatization catalyst

125

267-270

3rd series

“ 7360 CH 6 (Ludwigshafen) and 7911 (Leuna) comparison of at elevated temperatures and pressures

126

538-551

148

647-658

169

652-64

“ 7360, 7646, 7525, 7673, refining

173

198-199

“ 7525, 7673, 7360, 7646, refining

173

198-199

CATALYST 7612, comparison with 7360 at 350° for dehydrogenation

169

67-69

“ 7638 and 7360, comparison of as aromatization catalysts

125

267-270

3rd series

“ 7646, 7525, 7673, 7360, refining

173

198-199

“ 7673, 7525, 7360, 7646, refining

173

198-199

“ 846 W 250 (8376) use in different processes

173

31-32

173

231-255

“ 7846 and 6434, specific data on vapor phase

89

2747

38

0 ‘19

“ 7846 and 5058 and their combination, comparison of, Poelitz, 1943

130

40 ‘25-40 ‘48

“ 7846 and 5058, combination of,

201

382-384

“ 7846, 6619, and 5058 for prehydrogenation

126

1122-1124

“ 7846 (Mo) 5058, and 8376 (7846 W 250) temperature dependence of reactions of middle oil hydrogenation with,

218

90 ‘80-90 ‘96

“ 7846 and 5058, operations with,

254

74-79

“ “ W 250

148

147-152

254

60-65

“ “ “ “ operation results with the,

57

1002-1036

“ “ for the prehydrogenation of Scholven middle oil

164

713-716

“ 7846 W 250 with 5058 and with combinations of the two, comparison of,

218

90 ‘61-90 ‘79

“ 7846 W 250-8376, use of for different processes

169

1-2

“ 7846 for prehydrogenation of coal middle oil

169

33-44

173

49-61

“ 7846 for the prehydrogenation of Scholven middle oil

181

6511-6530

202

155-174

“ 7846 W 250, discussion of,

3

2745

18

70 ‘9-70 ‘25

“ “ “ “

75

822-880

75

826-829

Translation, Phillips Co.

245

20 ‘60-20 ‘63

75

872-874

Translation, Phillips Co.

245

20 ‘66-20 ‘68

“ 7846, calibration of the vessel in Politz

75

820-821

“ 7911 (Leuna) and 7360 CH6 (Lu) at elevated temperatures and pressures, comparison of,

126

538-551

148

647-658

169

52-64

“ 7935 for hydrogenation, testing of in 100 ml converter

126

483-497

CATALYST 8376, 5058, 6434, testing of composite samples of,

254

167-169

“ 8376 (7846 W 250) 5058, 7846 (Mo), temperature dependence of reactions of middle oil hydrogenation with,

218

90 ‘80-90 ‘96

“ 8736 for hydrogenation of wax from Fischer synthesis

162

847-869

“ 8736, testing, for Politz and Ludwigshafen

202

515-519

“ 8376, exchange of experience on saturation

254

186-206

“ 8376, regeneration of,

75

881-883

“ “ and 5058 for Fischer process products

162

687-691

“ 8376 (7846 W 250), use of for various feed stocks

254

226-242

“ 8376, use of for brown coal middle oil, Leuna

173

154-162

“ 8376, use of for different products

181

6469-6474

6488-6494

“ 8376 and a comparison with 5058 and a combination of the two catalysts, operating experience with,

130

ref. W

40 ‘1-40 ‘24

Translation T-185

237

90 ‘96-90 ‘101

“ 8376 prehydrogenation catalyst for various feeds, the use of, by Gunther

173

320-328

Translation T-485

279

240-241

“ 8688 for aromatization at 250 atm., preliminary results

148

185-187

“ 8688, the influence of the partial pressure of the products on the aromatization of middle oil

166

349-353

“ 8736, experiments on prehydrogenation catalysts, especially with,

202

639-650

“ 8754 aromatization

170

VII-2

721-734b

“ 8797 and 6434, comparison of sensitivity towards nitrogen and production disturbances of,

173

563-564