Table of Contents

MANUFACTURE OF CATALYST

TOM
REEL
BAG ITEM FRAMES

ALUMINA-silica catalyst, methods of production

30

16..1020

AT catalyst, drying of, Leuna

177

2208-2210

“ “ plant at Heydebreck

1

2168

6

80 ‘42-80 ‘56

177

2162-2172

AT-244 catalyst plant according to Schklon

116

80 ‘94-80 ‘104

BROWN oxide catalyst plant for Frose

27

2169

8

8..70-8..80

BROWN oxide catalyst manufacture at Frose and Gapel, miscellaneous information on,

27

2169

14

14..92-14..97

“ oxide catalyst plant, operating description of,

27

2169

15

15..98-15..104

“ oxide catalyst W (Fe203 Cr203), preparation of,

30

16..1021-16..1050

CARRIER for the 7019 catalyst, preparation of,

202

39-43

“ for catalyst preparation

166

550-554

CATALYST 4046, preparation of,

119

50 ‘87

“ factory plans for U. S. 10 Am. Ka. 109)

90

20 ‘43-20 ‘46

“ plant, Brux. Leuna M 5504b-1

195

31503

“ cost

69

897-915

“ production in building 53, Welheim. Composition of catalysts. Manuscript supplied by Dr. E. Frese. T-291

273

577-595

COBALT and thorium in the catalyst plant, losses of,

42

452

“ catalyst plant

36

3454

9

10 ‘50-10 ‘52

“ catalyst plant, in English, flow sheet of,

48

403-409

“ catalyst, preparation - miscellaneous

43

3439

99

181-198

“ deliveries, 1943

39

3450

36

40 ‘91-40 ‘93

“ losses

42

966-969

67

220-242

“ “ costs, compositions, data for

43

2719

469-475

“ plant to an iron catalyst plant, conversion of,

37

3451

45

80 ‘36

“ procurement, 1943

33

3440

29

70 ‘81

“ situation, May 1943

35

3452

24

70 ‘44-70 ‘49

“ -thorium catalyst, raw material, receipts for

43

2719

477-479

“ stocks

134

0 ‘31-0 ‘33

134

0 ‘35-0 ‘37

193

23060-23061

COMPOSITION and preparation of 6434 catalysts

173

409

Translation T-482

279

236-237

CONSTRUCTION of catalyst plants in Germany (possibly with A.N.I.C.)

215

40 ‘127-40 ‘143

COOLING installation, enlarging and improving, for fused iron catalysts of the synol synthesis

13

3043

3

40 ‘30-40 ‘37

Translation T-452

274

1578-1586

COSTS of the tungsten catalysts at Ludwigshafen

163

38-40

DEHYDROGENATION catalyst, manufacture of, Leuna

18

1-15

DELIVERIES of catalyst for Fischer-Tropsch

70

811-820

DELIVERIES of catalyst from the Ludwigshafen plant

193

23056-23057

DEWAXING of spent Fischer-Tropsch catalyst

122

102431-102449

DRAWING of catalyst factory

27

2169

13..89-13..91

“ of Holten catalyst plant

67

640

EXTRACTION and drying of iron catalyst

36

3451

2

70 ‘89-70 ‘90

FLOW sheet of a catalyst plant

39

3450

31

40 ‘54

“ “ for manufacture of catalysts 6719 and 6434, Leuna M 7465-2

195

31497-31498

“ sheet M 7461a-2

195

31502

“ “ of catalyst plant II, Leuna, M3002-6

195

31504

“ sheet for catalyst manufacture and reduction plant Leuna, M 4628a -1

193

23449-23450

“ sheet for U. S. catalyst factory 10 Am. Ka 115

90

20 ‘47-20 ‘50

“ sheet of char (grude) catalyst plant, Leuna, M 4408-16

193

23470

“ sheet preparation of HF catalysts

195

31504

Translation, Sinclair

279

602-604

“ sheet of HF catalyst plant, Leuna, M 3789-16

193

23467-23468

“ sheet for the manufacture of the catalyst, Leuna M 7337-2

195

31505

“ sheet of manufacture of catalyst I, Me 971, Leuna

195

31508

“ sheet of production of catalyst II, Me 971, Leuna

195

31510

“ sheet of catalyst plant Me 22-b, 1937, Leuna 2089-16

195

31511

“ sheet of catalyst preparation, Leuna 0/7322

195

31512

“ sheet for rebuilding of tungsten oxide catalyst plant Me 22d Leuna M 4739-16

195

31513-31514

“ sheet of catalyst plant, Leuna M 8183-2

195

31515

“ sheet of HF catalyst plant, Leuna M 3513 e-1

195

31516

“ sheet of tungsten oxide catalyst production plant 0/1732-1

195

31517

31518

31519

“ sheet of catalyst plants Me 971-998, Leuna, M 9062-4

195

31521

“ sheet for enlarging the catalyst plant Me 882 Leuna M 7913-4

195

31522

“ sheet of catalyst plant Me 971, Leuna M 7821-4

195

31523-31524

“ sheet of the catalyst plant, Ruhrland. Braaunkohle-Benzin A. G. 2223-2

195

31527

FROSE catalyst plant, metal requirements for,

27

2169

12

12..87-12..88

FURNACE for heating catalysts, Zeitz plant. Mineraloel Baugesellschaft, 2075-2

195

31166

“ regenerator, for HF catalyst and its distributing mechanism, details of, Leuna M3411-1

194

30283

“ ignition, for catalysts, details of, OS 178

195

31520

“ with cooling ozone OFT/155 for catalyst reduction and oxidation, drawing of,

84

2..8

FUSED iron catalyst, production and reactivation at the Auschwitz synol plant

13

3043

3

70 ‘23-70 ‘24

“ iron catalysts in a 10,000 te/ann installation, reduction of,

134

80 ‘5-80 ‘14

HF catalyst treatment plant, Leuna, M3515-1

194

30278

HYDROGEN for reduction of catalyst

43

3439

93

32

HYDROGENATION catalyst, production and shipment of, 1928-1942

163

46

INDUSTRIAL production of catalyst 5058.

162

877-878

Translation T-143

237

80 ‘1-80 ‘2

IRON catalyst, preparation of detail drawing

62

40.243

“ catalyst, flow sheet for the production of,

39

3450

32

40 ‘55-40 ‘57

“ catalyst, testing and production of,

37

3451

45

80 ‘37-80 ‘39

“ synthesis catalyst reduction plant, M-6459, flow diagram of,

116

20 ‘14

134

80 ‘4

“ work of press stage (catalyst) 10 Am Ka 3.101

90

30 ‘26-30 ‘29

ITALIAN catalyst plant and correspondence in Novara, report on,

215

30 ‘133-30 ‘156

40 ‘1-40 ‘96

LAYOUT of catalyst plant, building 215, Leuna, 4882/210

195

31506

LEUNA catalyst plant expansion

116

80 ‘37-80 ‘69

“ proposed extension of existing catalyst plant, M 3916a-1

195

31500

“ ground plans of catalyst plant Me 971

195

31509

MANUFACTURE and recovery of catalysts, Sterkrade-Holton. Reported by A. Parker

197

10 ‘57-10 ‘63

“ and regeneration of catalysts at I. G. Farben Industrie, Ludwigshafen/Oppau. Reported by W. F. Faragher and W. A. Horne

199

60 ‘3-60 ‘12

“ and regeneration of catalysts for hydrocarbon synthesis

190

24472-24475

MONTHLY reports of the catalyst factory, Oberhausen Holten, 1942

68

617-836

M 3402-b-1 (marked “invalid”)

195

31501

NOBLE metals consumed in the fixed bed gasoline production, calculated to 100,000 te gasoline/ann

202

62-63

PLASTICS catalyst plant with catalyst reduction unit Me 971-I for 12 te/month. Leuna, M 4638 a-1, M 4628-1, flow sheet of,

195

31525-31526

“ manufacture, flow sheet for production of intermediates, Me 971-I Leuna M 4238-1

195

31528-31529

POLYMERIZATION catalysts (toka) in an industrial unit, description and drawings, production of,

42

1042-1044

“ catalyst production

50

405-406

PRECIPITATION and solution catalyst plant 10 Am. Ka 2.101

90

30 ‘9-30 ‘12

PREHYDROGENATION catalysts, report of catalyst factory on,

169

220-221

PREPARATION of catalyst

165

398-402

“ “ “ Reported by W. A. Horne and F. Faragher

197

70 ‘79-70 ‘80

80 ‘1-80 ‘3

“ of 5058 catalyst

209

80662-80663

“ and composition of 6434 catalyst

173

409

Translation T-482

279

236-237

“ of catalysts 5058, 6434, 8376 and 7935, brief directions for,

218

30 ‘70-30 ‘71

“ of clay, general layout of, Leuna M 2571-1

195

31023

PRICES of catalyst

218

0 ‘33-0 ‘42

0 ‘50-0 ‘75

“ of the tungsten catalyst, changes in,

193

23053-23055

PRODUCTION and testing of iron catalyst

37

3451

45

80 ‘37-80 ‘39

“ of catalyst, 6434

162

697-698

205

735-736

209

80664

254

307-308

Translation T-416

274

1165-1166

“ costs of catalysts 6434

181

6434-6445

Translation S-110

274

1800-1801

“ of toka (toluene) catalyst in a pilot plant

42

1037-1041

“ of 5058, continuous

195

31507

“ records 1938, Oberhausen-Holten

68

841-891

“ of catalyst 6434, plant for, Leuna, M 3461-2

195

31499

QUARTERLY reports on hydrogenation catalysts (6434)

214

90 ‘41-90 ‘50

REACTIVATION of catalysts

41

2744

40

60 ‘76-60 ‘78

180

6044

“ of catalysts, discussions

176

877-889

RECOVERY and manufacture of catalyst, Sterkrade-Holten. Reported by A. Parker

197

10 ‘57-10 ‘63

REDUCTION plant catalyst 10 Am. Ka. 7.101

90

30 ’13-30 ‘16

“ vat (catalyst preparation) 10 Am Ka 7.102

90

30 ‘36-30 ‘39

REGENERATION and manufacture of catalysts at I. G. Farben-Industrie, Ludwigshafen/Oppau. Reported by W. F. Faragher and W. A. Horne

199

60 ‘3-60 ‘12

“ and manufacture of catalyst for hydrocarbon synthesis

190

24472-24475

REGENERATOR furnace for catalyst, details of, drawing M 5070-1, M 5181-1

86

1031-1033

SHIPMENT and production of hydrogenation catalyst, 1928-1942

163

46

SOLUTION and precipitation catalyst plant 10 Am Ka 2.101

90

30 ‘9-30 ‘12

“ tank (catalyst preparation) 10 Am Ka 4.103

90

30 ‘35

“ tank (catalyst preparation) 10 Am Ka 4.101

90

30 ’30-30 ‘34

SPENT 6434 catalyst, recovery of,

214

70 ‘1-70 ‘3

SPRAYERS and washers in building Me 22d. # 0/142

195

31496

STARTING the toka (toluene) polymerization catalyst plant

42

2087-2093

STORAGE of catalysts

7

2732

1

50 ‘10-50 ‘12

78

566-570

SUPPLIES, catalyst, 1943

181

6506

SYNTHESIS catalyst production, plant of,

170

III-3

263-271

SYNTHETIC aluminum silicate catalyst, production of,

141

44-46

THORIUM and cobalt losses in the catalyst plant

42

452

“ solution and recovery plant 10 Am. La 0.110

90

30 ‘1-30 ‘4

TOKA installation (toluene catalyst)

50

541-554

561-568

TUNGSTIC acid at the Ludwigshafen catalyst plant, 1934-1942, receipts of,

163

45

TUNGSTEN disulfide, preparation of,

181

6420-6428

“ sulfide catalyst, by v. Funer, the preparation of,

257

881-882

Translation T-236

257

882a-882b

Translation T-236

273

226-227

TUNGSTEN sulfide, the preparation of catalytic-cally active

181

6429-6430

Translation S-107

274

1795-1796

“ recovery, Leuna, flow sheet M 4767-16

193

23469

“ requirements for catalysts

181

6446-6452

VAPOR phase catalyst deliveries

163

41-44

WASHERS and sprayers in building Me 22d # 0 /152

195

31496

WELHEIM vapor phase catalyst K 536, prepa-ration of,

209

80665