HEAT and carbon balance, Fischer-Tropsch plant, 1938

 48

399-402

HIGH pressure experimental plant, Lurgi

66

1067-1099

     “         pressure synthesis plant of Ruhrchemie A. G., diagram of experimental, 2 FT/23

 84

 2..11

     “         pressure synthesis reactors, ratio of gas and liquid in concurrent flow of feed

 190

23776-23806

     “         sulfur values, effect of, upon synthesis, 1941

45

441-447

46

295-301

     “         temperature circuit with Co catalysts, experimental

 84

 19..56-19..60

HYDROCARBON synthesis by gas circulation process

26

10..565-10..576

     “         synthesis from carbon dioxide and hydrogen

39

3450

39

40 ’97-40 ‘98

     “         synthesis from carbon monoxide and hydrogen, by Breywisch and Geiseler

 55

2523

94

 964-965

                                    Translation by Texas Co.

243

40 ’98-40 ‘101

                Do.,

55

95

966-971

                                    Translation by Texas Co.

243

40 ‘102-40 ‘112

                Do.,

55

96

972-979

                                    Translation by Texas Co.

243

40 ‘113-40 ‘123

     “         synthesis from carbon monoxide and hydrogen (1940-1943)

 55

 963-1079

148

99-102

166

851-861

HYDROCARBON synthesis from mixtures of carbon monoxide and hydrogen, ICI report, December 1938, in English

19

152.1794-152.1963

20

153.1964-153.2032

     “         synthesis using carbon monoxide gas from electric iron furnaces, proposed

 36

 3452

 39

 0 ’45-0 ‘55

HYDROGEN sulfide, formation of, from sulfates of cooling water, by Feisst

 180

 6185-6194

     “         sulfide in residual gas

44

59

1102

IMPROVEMENTS in Fischer-Tropsch installation

33

3440

13

30 ’16-30 ‘20

IMPROVING gasolines of Fischer synthesis, preliminary report of experiments for

 37

 3451

 7

 60 ‘142-60 ‘144

IMPURITIES in synthesis gas, effects of, upon catalysts

 70

 742-762

INCREASING production, yield and catalyst life in synthesis works, suggestions for, by Loepmann

35

3452

24

70 ’50-70 ‘59

180

6..100-6..109

INERT content of synthesis gas on conversion and yield, effect of

 37

 3451

 19

 0 ’23, 0 ‘35

     “         in synthesis gas, effect of, on course of reaction and paraffin deposition

 35

 3440

 77

20 ’36-20 ‘37

INJECTION circuit in synthesis

67

108-113

INSPECTION of hydrogenation and Fischer-Tropsch plants in Western Germany during September, 1945, reported by T. E. Warren

199

50 ‘1-50 ‘17

i-GASOLS and aviation gasoline from synthesis products, preparation of

 67

 673-694

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

243

50 ’19-50 ‘35

i-PARAFFINS, developments of gasoline synthesis from carbon monoxide and hydrogen, in particular of direct synthesis of, KWI Mulheim

209

80814-80830

i-     “       , direct synthesis of, from carbon monoxide and hydrogen

183

8107-8123

i-SYNTHESIS

45

80

90-95

i-     “       , by H. Pichler and K. H. Ziesecke

279

789-931

KELLOGG, M. W., reports on Fischer-Tropsch, February 1939, in English

 20

154.2034-156.251*

KOPPERS drawings and description of proposed Moers synthesis plant, 1938

 70

548-554