GAS, amount of converted, required to raise CO:H₂ ratio in second stage to 1:1.95

 72

 541-546

     “         balance computations from average analytical data, April 1940

 67

 138-139

     “         consumption during synthesis

43

2719

516-519

     “         contraction in combined 1^st stage reactors

72

52-54

     “         contraction in combined 2^nd stage reactors, comparison to total construction in system

 72

49-51

GAS, distribution, in different synthesis reactor

43

2719

500-503

     “         , distribution, in synthesis

43

2719

529-530

     “         flow, effect of changing direction of

37

3451

14

0 ‘3-0 ‘11

     “         flow, effect of velocity of, on pressure synthesis

 44

 3441

 35

 819-837

     “         flow, effect of velocity of, on production of olefins and fatty acids

 72

 794-821

     “         for stage 2, enriching

44

3441

56

1094-1096

     “         formation with Eirichkorn mixed catalysts

44

3441

51

1068-1071

     “         loads, synthesis reactor

43

2719

582-586

     “         oil obtained from CO₂-enriched end gases of gasoline synthesis, production and properties of

44

3441

28

766-784

     “         passing through reactor after long shutdown

43

2719

504

     “         supply in first stage converters

43

2719

576-579

     “         utilization and course of synthesis, calculations of, by O. Roelen, (1944 Storkrade-Holten)

49

470-532

                                    Translation T-420

274

1205-1270

                                                “       T-421 

1271-1282

GASOL calculations for 10-day period, example of, January 1943

72

501-508

     “         , I. G. process for utilization of Fischer, flow sheet

1

2168

 13

 10 ‘33

     “         synthesis

34

3440

58

40 ‘69

GASOLINE, aviation, and toluene from synthesis gasoline

 50

 522-540

     “         , aviation, from Fischer-Tropsch synthesis

50

433-462

     “         , circulation

36

3454

33

40 ’77-40 ‘90

     “         , circulation, over cobalt catalysts

36

3454

33

40 ’46-40 ‘75

     “         from tar oil-synthesis oil mixtures

43

2719

650-652

     “         in tail gas

35

3440

67

10 ’81-10 ‘93

     “         , odorless, from Fischer synthesis

24

6..285-6..289

     “         , production of aviation

46

823-838

     “         , production of Fischer, from natural gas

65

Sec. VII

5..45-5..47

     “         , properties of normal pressure synthesis

48

410-413

     “         synthesis

44

3441

29

785-793

     “         synthesis according to Franz Fischer, researches on, by Meisenheimer

 15

2505-2520

GASOLINE synthesis, circulation process

35

3452

2

40 ’61-40 ‘78

     “         synthesis, Franz Fischer’s, according to investigations of Dr. Lorenz, unreadable

 278

 0 ‘1-0 ‘16

     “         synthesis, ideal gas utilization in

33

3440

21

50 ‘1-50 ‘3

     “         synthesis, K. W. I. examination of fractions of

33

3440

29

90 ’14-90 ‘24

     “         synthesis, 1937 report on Fischer

42

1056-1061

     “         synthesis plant, Rheinpreussen

43

2719

332-337

     “         , synthetic, from natural gas; from article of P. C. Keith, Chem. Ind., Vol. 7, 1946, pp. 58-63, Kislorod 1947, No. 2, pp. 29-33, in Russian

258

50 ’57-50 ‘58

     “         , tests of various

68

291-317

GENERAL problems of synthesis

44

3441

57

1099-1101

                                    Translation T-414

274

1151-1152

GUM forming material, effect of, in synthesis gas

44

3441

37

848-849