TAIL gas analysis for calculation of conversion

37

3451

16

0 ’14-0 ‘17

     “         gas at Hoesch-Benzin, composition of

33

3440

14

30 ‘71

     “         gas of pressure synthesis, evaluation of

36

3452

36

0 ’16-0 ‘24

     “         gas, purification of

49

384-386

TEMPERATURE, effect of, on synthesis

43

2719

559-566

TESTS of synthesis products

13

3043

3

60 ’84-60 ‘90

THEORETICAL aspects of Fischer-Tropsch synthesis

66

1035-1066

THRUPUT, conversion with increased

43

2719

523-526

TOLUENE and aircraft fuel synthesis (Hungary)

46

766-778

50

522-540

TWO-STAGE hydrocarbon synthesis from water gas with iron + cobalt catalysts

 84

 24..129-24..132

UNSATURATED hydrocarbons during hydrogenation of carbon monoxide, formation of (data in literature)

 164

 278-283

UPPER Silesian synthesis plant

35

3452

33

100 ‘6-100 ‘12

UP running

44

3441

48

1049-1055

VAPOR pressures (saturation pressures) for Engler fractions of middle pressure synthesis

 36

 3454

 3

 10 ‘18

WASTE gases from electric smelting of iron, hydrocarbon synthesis from

 41

 2744

 15

 40 ‘112-40 ‘123

WATER gas gasoline

37

3451

37

60 ‘109-60 ‘113

     “         gas, hydrocarbon synthesis directly from, by Mohry

 67

 39-41

                                    Translation by  S. O. Co., (Ind.)

243

50 ‘7-50 ‘8

     “         gas pressure synthesis products, study of

24

9..326-9..352

     “         gas, proposed plant changes to operations on

37

3451

29

30 ’23-30 ‘27

     “         gas recirculation

44

3441

40

878-884

WAX, avoiding formation during synthesis

45

206

                                    Translation S-96

274

1764

     “         extraction from spent catalyst

44

812-814

     “         production for fatty acid synthesis

37

3451

32

30 ’43-30 ‘51

     “         recovery from used catalysts

70

771-780

WAXES, physical properties of

68

278-285

286-290

WINTERSHALL A. G., Lutzkendorf, reported by H. Hollings

 197

 50 ‘1-50 ‘22

YIELD, calculation of theoretical, from analysis of synthesis and residual gas

 44

1085-1086

                                    Translation T-413

274

1144-1150

     “         , deterioration of synthesis

43

2719

505-507

     “         estimate with H₂ addition to second stage

72

490-500

     “         , Fischer synthesis

1

2168

18-20

10 ’50-10 ‘52

     “         measurements in Ruhrbenzin and Rauxel, comparison of

 33

 3440

 19

40 ’29-40 ‘35

     “         of products in Rheinpreussen

33

3440

15

30 ’83-30 ‘84

YIELD relationships in 2-stage synthesis of gasoline

44

3441

27

764-765

     “         , synthesis, calculations of

34

3440

42

30 ’73-30 ‘78

41

2744

17

50 ’19-50 ‘21

42

984-1002

43

2719

544-550

     “         , synthesis, experimental

43

2719

498-499

     “         , synthesis, with low CO:H₂ ratios

43

2719

554-558

     “         , theoretical

45

102

236

     “         , theoretical, calculation of, from gas analysis

44

3441

55

1082-1093