TOM
Reel

CARBON deposition on catalyst

45

105

254-255

     “         dioxide and methane production, high

44

3441

36

838-847

     “         dioxide content, influence on synthesis yield with Co-Th-Mg catalyst

 1

 2168

17

 10 ’44-10 ‘49

     “         dioxide, formation of, correction

45

93

210-212

     “         dioxide-hydrogen mixture, letter on gasoline synthesis from

 38

 3450

 15

 10 ’74-10 ‘75

CARBON dioxide removing, by refrigeration

44

3441

69

1140-1146

     “         monoxide conversion and temperature, connection between

 219

 20 ’66-20 ‘79

     “         monoxide conversion from accurate gas analyses

 72

 515-517

CASTROP-Bauxel, inspection of Fischer-Tropsch plant at, reported by C. C. Hall and A. H. Powell

 197

 20 ’27-20 ‘34

CATALYST, analysis of Fischer-Tropsch

122

35

2469

     “         bed, downward progress of reaction in

45

88

190-195

     “         , Kuhlmann (pure Co catalyst), conversion with

 20

 156.2512-156.2534

     “         , reactivation of

35

3440

86

20 ‘103-20 ‘108

43

3439

16-23

     “         removal

44

3441

32

814

     “         removal from synthesis units

44

3441

32

812-813

C₄ content of Fischer primary gasoline

35

3440

70

10 ‘101-10 ‘109

CIRCULATION gas pilot plant results, Hoesch, 1940

62

37..240-38..241

     “         method for gasoline over cobalt catalyst

35

3452

30

90 ‘104-90 ‘121

     “         synthesis reactors products, composition of

43

2719

490-494

COBALT catalyst loss in paraffin wax formed

37

3451

15 & 17

0 ’12-0’13

0 ’18-0 ‘19

     “         procurement, status of

219

10 ’80-10 ‘91

     “         purity requirements

170

III-5

371

     “         -thorium and iron synthesis, 1939-1943, research problems on

 42

 556-648

COMPARISON between iron and cobalt catalysts synthesis, January 31, 1941

 45

 265-271

                                    Translation

225

50 ’40-50 ‘42

     “         of conversion of synthesis gas and water gas with cobalt and iron catalyst

 39

 3450

 42

 60 ’39-60 ‘44

     “         of different gasoline synthesis plants, January 1939

 33

 3440

20

 40 ’36-40 ‘48

     “         of gasoline from stages I and II

44

46

950-952

     “         of gasolines of 1^st and 2^nd stages with activated carbon unit after 2^nd stage

 72

 568-578

     “         of gasoline plants of Rheinpreussen, Victor, Brabag and Schwarzheide, 1938

 33

 3440

 20

 40 ’49-40 ‘127

     “         of hydrogenation and synthesis methods of liquefaction of coal

 181

 6584-6588

COMPARISON of normal pressure and medium pressure synthesis with cobalt catalyst, by Schuff, 1940

 178

 2586-2603

     “         of recycling and direct synthesis

45

109

272-275

     “         of synthesis gas conversion with cobalt and iron catalyst

 36

 3454

 14

 10 ’98-10 ‘106

     “         of Winkler-Duftschmidt, Klemm, Wentzel-Scheuermann and Michael processes

 13

 3043

 3

 50 ’50-50 ‘56

COMPOSITION of liquid synthesis product of pressure synthesis under normal operations and with operations in circuit

37

3451

37

60 ‘127-60 ‘141

     “         of products with mixed cobalt catalyst, August 1942

33

3440

28

60 ’46-60 ‘53

     “         of synthesis product

35

3440

78

20 ’38-20 ‘39

68

318-321

CONDENSATE from synthesis gas, testing

33

3440

13

30 ’30-30 ‘40

     “         in synthesis gas, effects of, on activity of catalyst

33

3440

 13

30 ’54-30 ‘58

CONDITIONS, effect of synthesis, with cobalt catalyst, discussion of

36

3451

1

70 ’68-70 ‘75

CONFERENCE at synthesis works, Essen, October 3, 1941

45

124

430-510

72

173-254

     “         of managers of synthesis works, 1937-1944

46

3446

452-720

CONNECTING high and low pressure synthesis in series based on 65,000 cbm water gas

44

1116-1126

                                    Translation T-415

274

1153-1164

CONNECTION between carbon dioxide and methane formation during synthesis, is there direct?

37

3451

18

0 ’20-0 ‘22

CONSTANT operating conditions during synthesis, note on maintaining

33

3440

 11

 20 ‘104-20 ‘105

CONSTRUCTION program for 1941

68

340-342

CONTROL, laboratory directions for synthesis

71

703-792

CONVERSION and expansion, computation of, from gas analytical results

 72

518-519

     “         of CO, and yields in some reactors

72

76-122

     “         of synthesis products into lubricating oils and special gasolines, factors for calculation of

 36

 3454

 5

10 ’22-10 ‘23

CONVERTING coal and possible products therefrom, diagram showing methods of

 70

635

637

COOLING in gasoline synthesis, use of oil for

35

3452

3

40 ’79-40 ‘90

COURSE of synthesis, study of 1942

72

18-48

C₇ content, determination of, in primary products of Fischer synthesis

 50

702-737

C₃ and C₄ hydrocarbons, production of

14

1248