Table of Contents

NITROGEN FIXATION

 

 

 

 

 

TOM
Reel

Bag

Item

Frame

AMMONIA production, flow sheet

115

 

 

50 ‘7

 

117

 

 

60 ‘5-60 ‘7

     “         , pure, production of, from strong ammonia water

 215

 

 

10 ‘119-10 ‘121

 

 

 

 

20 ’61-20 ‘66

     “         synthesis, by R. L. Morley and W. W. Odell

197

 

 

60 ’61-60 ‘63

     “         synthesis, flow sheet, M 2720d-1

181

 

 

6339

 

207

 

 

154

     “         synthesis laboratory, work in

13

3043

2

30 ’77-30 ‘78

     “         utilization plant, Leuna

116

 

 

50 ‘2-50 ‘11

 

 

 

 

50 ’43-50 ‘46

     “         water, concentrated, flow sheet for preparation of, Leuna M 10811-2

 195

 

 

 31667, 31675

AMMONIUM sulfate plant, BK 922-8, Scholven, drawing

 89

 2747

 32

 0 ‘13

     “         sulfate production, flow sheet of

117

 

 

60 ’14-60 ‘15

     “         sulfate production, index of patentees

195

 

 

31661, 31665

CARBON monoxide removal from ammonia synthesis gas by absorption in copper solution

 17

 

 

25..479-25..559

CONVERTER stall installation, ammonia, Leuna, M 12714-2

 179

 

 

 4834

GAS amounts in ammonia synthesis, flow sheet of, Linz, W 3283-8

 195

 

 

 30926

GERMAN Association for sale of ammonia, authorized commercial activities

150

 

 

 588-593

HIBERNIA ammonia plant flow sheet

207

 

 

152

I. G. and Linde methods, flow sheet of ammonia production by

 195

 

 

 30927

LEUNA, I. G. Farbenindustrie A. G., nitrogen fixation plant, reported by R. M. Hunter

198

 

 

0 ’15-0 ‘19

LINDE and I. G. methods of ammonia production, flow sheet of

195

 

 

30927

RATE of formation of ammonia from synthesis gas

25

 

 

13..654-13..670

SCHOENHERR furnace, details of (electric arc nitric acid process)

155

 

 

 

466-469

SCIENTIFIC and technical foundation of high pressure synthesis of ammonia

29

 

 

26..789-28..1027

SPAIN, bid for installation of nitrogen plant in

118

 

 

0 ’10-0 ‘63

 

 

 

 

10 ‘1-10 ‘51

TERTRE, Societι Carbochimique, reported by H. J. Phelps

198

 

 

70 ‘3-70 ‘4

TOYAM, Japan, flow diagram of H2 – N2 plant for, 7288

99

 

 

10 –13

TWO thousand atm ammonia plant, installation of, Me 494, Leuna, M 4974a-2

195

 

 

31736

 

 

 

 

 

OIL CIRCULATION

 

 

 

 

 

 

 

 

 

ALCOHOL synthesis from carbon monoxide and hydrogen in oil circulation process

 

26

 

 

9..288-9..291

COMPARISON of Fischer, Winkler-Duftschmidt and Michael processes, synthesis of gasoline from CO + H2

117

 

 

90 ‘126-90 ‘130

COMPOSITION of synthesis products of gas and oil circulation processes

42

 

 

288-291

CONFERENCE on CO-H2 synthesis, Berlin, (oil circulation)

27

2169

 

31..167-32..170

     “         on CO-H2 synthesis, 1941, Michael and Duftschmidt processes

1

 

65

20 ’28-20 ‘31

                                    Translation by Atlantic Ref. Co.

143

 

 

0 ‘4-0 ‘8

CONVERSION of cobalt synthesis to iron catalyst synthesis according to experiments by Brabag, Koelbel, 1944

215

 

 

10 ‘1-0 ‘15

 

 

 

 

10 ’63-10 ‘75

DISCUSSIONS of various synthesis problems, brief, April 1942

180

 

 

6149-6161

DUFTSCHMID, notes and calculations on oil circulation process

219

 

 

10 ’18-10 ‘37

     “         , oil circulation process

170

 

 

234-240

 

 

 

 

250-258

 

174

 

 

33-39

DUFTSCHMID oil circulation process, three papers on

134

 

Ib-11 – Ib-13

40 ’26-40 ‘39

                                    Translation T-463

279

 

 

19-35

     “         oil circulation process, two short papers on

1

Sec. 65

3

20 ’32-20 ‘33

 

13

3043

2

30 ‘76

                                    Translation T-450

274

 

 

1558-1560

     “         process, estimate of plant for processing of 100,000 cbm/hr synthesis gas by

166

 

 

761-768

                                    Translation S-105

274

 

 

1790-1792

     “         process, installation cost estimate

166

 

 

762-768

     “         processes, Ludwigshafen preliminary experiments on Michael and

42

 

 

309-323

KOELBEL, hydrocarbon synthesis with iron catalyst, 1940

178

 

 

2627-2642

     “         process, Diesel fuel from synthesis products and tar oils

180

 

 

6062-6074

     “         , Dr., reports on middle pressure iron synthesis

26

 

 

303-314

 

 

 

 

315-316

                                    Translation S-6

274

 

 

1650-1651

LIQUID phase synthesis (largely illegible)

166

 

 

695-700

     “         phase, synthesis in, by Miss Gφring

256

 

 

174-179

                                    Translation T-433

256

 

 

179a-179g

                                                “              “

274

 

 

1446-1452

OIL circulation synthesis, preliminary report on, January 1939

42

 

 

298-308

    “          recycle process in hydrocarbon synthesis

190

 

 

24482-24483

     “         recycle process, report of Fouchers on CO + H2 synthesis, 1947, Sec. II of Part I, comments by L. W. Alberts

279

 

 

663-666

     “         requirements for wet synthesis

34

3440

57

40 ‘68

PARAFFIN wax, increasing proportion of, in existing synthesis plants, by Roelen

180

 

 

6244-6247

     “         wax, production of, in liquid phase synthesis

26

 

 

9..292-9..293

ROELEN, hydrocarbon synthesis with iron catalysts

178

 

 

2643-2669

SYNTHESIS process oil circulation

27

 

 

32169-32170

 

 

 

 

33171-33173

                                    Translation T-454

274

 

 

1593-1599

WET synthesis

42

 

 

934-940

WINKLER-Duftschmidt process of fuel production from CO + H2 under pressure

117

 

 

100 ‘1-100 ‘15