Table of Contents

HYDROCARBONS, SATURATED
TOM
REEL		 BAG ITEM FRAMES

ALIPHATIC chemistry, laboratory rectification as an aid to, by Groll

71

662-677

“ hydrocarbons, aromatization of straight chained, from the Fischer-Tropsch synthesis, by Rottig

138

XXVIII

40’1-40 ‘8

“ hydrocarbons, preparation of high anti-knock isoparaffin motor fuels by the alkylation of, flow diagram

138

II

0 ‘2

“ hydrocarbons, preparation of high anti-knock isoparaffin motor fuels by the alkylation of, by Bohl

138

III

0 ‘3-0 ‘37

BUTANE, alkylate fuel from, cost estimations

14

1136-1149

“ , available, for the AT plant

71

162-164

“ and isobutane content of the gasification in splitting and aromatization over fullers’ earth catalysts

257

879-880

Translation T-308

257

880a-880b

Translation T-308

273

674-675

n-BUTANE and i-butane formation in hydro-genation, effect of different methods of operation on the total

174

89-94

i-BUTANE and butene yields at the different hydrogenation plants, calculated

214

20 ‘86-20 ‘92

n-BUTANE and n-pentane, isomerization of

168

481-489

BUTANE, catalytic dehydrogenation and H2SO4 alkylation

14

1251-1266

“ , catalytic dehydrogenation of

14

1180-1192

195

31190-31192

i-BUTANE, catalytic dehydrogenation of

14

1118-1119

n-BUTANE, catalytic isomerization

14

1273-1276

“ “ , constitution and distribution of production of sulfo-chlorination of

23

26..635-26..655

BUTANE (n-and i-), content of gas from splitting hydrogenation and aromatization

201

169-170

“ , dehydrogenation and alkylation of

14

1134-1135

“ , dehydrogenation, butylene concentration, isomerization, alkylation and polymerization, minutes of meeting on

56

617-639

“ dehydrogenation in 4 adiabatic steps

14

1158-1159

“ dehydrogenation in 5 liter pilot reactor

14

1122-1123

“ , dehydrogenation of,

56

12

992-1010

165

585

165

586-590

174

71-84

251

126-129

i-BUTANE, dehydrogenation of

29

13..668

n-BUTANE, dehydrogenation of, at atmospheric pressure with a catalyst from Oppau

168

496-500

“ “ , dehydrogenation of, with gas circulation at atmospheric pressure

168

490-495

174

55-61

“

62-64

“

65-70

BUTANE dehydrogenation, the selectivity of

174

53-54

“ dehydrogenation with gas recirculation

251

157

“ , flowsheet for the chlorination of, (fractionation with gas oil wash in HCl tower). Bruex, Kd 2005

28

2167

112

“ , flowsheet for the isomerization of, U 440-16

28

2167

114

“ , flowsheet T-52 - B-4 for alkylation of

177

2535-2536

“ for the aviation gasoline plant at Wesseling

71

156-159

i-BUTANE, history of the development of dehydrogenation of, isomerization and alkylation at Leuna

18

3042

11

10..44-10..46

BUTANE, hydrogenation of crotonic aldehyde to, Rodleben, 1941

55

512-516

i - “ , installation for the separation of

10

2743

4

40 ‘40-40 ‘43

n - “ , isomerization, dehydrogenation and alkylation, at Leuna

14

1279-1282

n - “ , and n-pentane, isomerization of

168

481-489

“ isomerization, Kd 1631

28

2167

99

“ , isomerization of

56

869-878

174

85-87

n- “ , isomerization of, with aluminum chloride, report by Drs. Pohl and and Nowotny

86

1304-1320

“ isomerization research

251

145-156

“ production, balance sheet for, Leuna, M 9405-2

195

31173

“ production, delivery agreement

“ between Brabag and Ammoniawerke

23

20..552-20..556

i - “ , research on the production of, by H. Hoshimiya, T. Otsuka, T. Shinoda and O. Miyata

231

10 ‘62-10 ‘69

“ separation, aviation gasoline plant, drawing BK 301-8, Scholven

89

2243

25

60 ‘26

“ separation, flowsheet of, Leuna, M 6706e-2

181

6287

n- “ , separation of, from i-butane

1

2168

5

70 ‘28-70 ‘34

n- “ , studies on the dehydrogenation of, by M. Kumamoto

231

10 ‘49-10 ‘61

i- “ , sulfo-chlorination of

23

22..573-22..58*

“ treatment plant, sketch 0/981, Leuna

195

31154

M 9201

195

31159

BUTANOL-tanol plant, installation of

165

578-584

CONDENSATION products, process for

254

497-503

CYCLOHEPTANOL, synthesis of

32-II

2078

227.1713-227.17**

CYCLOHEXANE, discussion, October 1941

164

491-493

“ from benzene

173

703-710

“ , hydrogenation of benzene to

253

910-911

CYCLOPENTANE phenanthren derivatives, progress in the chemistry of

18

66..686-66..69*

ETHANE, flowsheet of the working up of, Leuna, M 2063-16

193

23465

“ , purification of, separation of ethane and ethylene

189

21431-21457

“ utilization, flowsheet

117

60 ‘19

FISCHER 1.p.g., I. G. process for utilization of, flowsheet

1

2168

13

10 ‘33

FOUR-cycle hydrocarbons, the stability of

24

1..27

i-HEPTANE, production of, from n-heptane at 50 atm over 5058 with HCl addition

201

164

HEPTANE plant drawing, Bamag

41

2744

6

30 ‘116-30 ‘118

“ plant , flowsheet of

41

2744

6

40 ‘1-40 ‘2

40 ‘7

1-10-di (p-HEPTYLPHENYL) decane, preparation of

79

2856-2857

80

2993-2996

HEXADACANES derived from sulfonates and sulfates, preparation, properties and comparative capillarity investigations with 8

23

27..669-27..685

28..687-28..706

HEXANES and pentanes, isomerization constants of

167

356-357

HEXATRIACONTANE, preparation of

79

2913-2915

2922-2923

HEYDEBRECK iso-octane (tanol) installation

26

15..568-15..684

HYDROCARBONS C2-C4 I.G. in the scheme of processes

1

2168

4

0 ‘31

“ , analysis and characteristics of paraffins

(1083

127

(1140-1145

and

(1174-1180

128

(1208-1215

(1279-1285

(1323-1325

“ , analysis of mixtures of aliphatic and cyclo-aliphatic, by Ebert

71

659-661

“ and phenols, nitration of

217

0 ‘29-0 ‘32

0 ‘35-0 ‘46

“ , branched aliphatic with a long side chain, preparation of

79

2951-2954

“ , classification of solid

43

3441

855

“ , effect of lead on the oxidation of, and experiments on the slow oxidation of some olefines and ketones, by L. v. Muffling

221

30 ‘33-30 ‘40

“ from hydrogenation plants, production and use of gaseous, (tables)

210

50’70-50 ‘81

“ , gaseous, by hydrogenation

221

90’23-90’24

“ gases by hydrogenation and DHD

221

90 ’11-90 ‘15

“ , ignition of

167

285-287

“ in diesel fuels, knock behaviour and pour points of individual

168

197-207

“ , information gathered for Dr. Pier on possibilities of making

117

100’49-100’76

“ in mixtures, new methods of isolation and identification of, by Stern

71

638-650

HYDROCARBONS, literature survey on treatment of various, with hydrogen

254

526-529

“ mixtures, analytical and preparative separation of, by Sterne

3

2168

13

10 ‘26-10 ‘67

“ mixtures, colloquium on analytical and preparative separation of, 1940

71

630-700

“ mixtures, determination of aniline point

127

679-682

699-702

“ mixtures, precision separation of, by Schultz

71

634-638

“ , preparation of anti-knock

167

303-318

“ , preparation of iso paraffin-free

73

608-617

“ , processes for high test pure

254

494-496

“ , properties of C10 and C11 of

68

427-486

“ recovery process from coke oven gas

207

17-32

“ , report on

259

346-354

“ , research on, May 13, 1945

82

4968-4973

Translation by Phill. Petr. Co.

245

70’ 70-70’ 72

“ , study of structure for the identification of solid

91

296-308

“ , synthesis of branched, (from tri-alkylcarbinol)

254

491-493

“ , synthesis of pure, by G. Verberg

79

2811-2812

2819-2823

2852-2858

2864-2867

2877-2879

2894-2895

2913-2915

2922-2923

2951-2954

2966-2967

Translation by Phill. Petr. Co.

245

60 ‘29-60’56

“ , synthesis of pure

127

745-749

822-824

899-901

940-941

990-992

1020-1021

128

1069-1072

1101-1102

1167-1170

1195-1196

1252-1254

1368-1369

1419-1423

1469-1470

METHANE, activation of, through high pressures

82

4974-5021

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

243

50 ‘105-50 ‘119

“ , conversion of, into acetylene, formaldehyde

47

981c

“ , cracking of

188

20499-20515

190

24496-24497

“ formation, experimental

1

2168

76

20 ‘58-20 ‘74

“ formation in the butyl synthesis

2

2168

10

0 ‘49-0 ‘67

“ , production of, in Blechhammer

1

2168

5

70 ‘35

“ production from coke oven gas and by CO + H2 synthesis

1

2168

57

20 ‘11-20 ‘15

“ , production of, from mine gases

1

2168

46-48

10 ‘90-10 ‘92

“ research suggestions

42

908-925

“ , splitting off of, from hydrocarbons

7

2732

2

70 ‘70-70 ‘72

“ Synthesis, correspondence

56

11

958-961

“ , utilization in Hόls

1

2168

44

10 ’88-10 ‘89

METHANIZATION

45

111

279

“ catalyst, orienting experiments with

28

2171

4..268-4..273

“ oal gas by Martin and Traenckner, reported by E. T. Wilkins

226

10 ‘1-10 ‘9

METHYL cyclopentane from benzene or cyclo-exane

162

816-819

205

813-816

253

818-820

NAPHTHENES-aromatics equilibrium

165

523-526

“ , calculation of hydrogenation of, by Dr. Donath, July 1938

Translation T-472

279

172-179

“ , octane numbers of

165

447-459

168

262-274

“ , the temperature dependence of

168

250

NEOHEXANE

28

2171

3..56-3..61

56

766-771

174

142-144

“ , discussions of development work in

13

3043

2

20 ’81-20 ‘85

“ (2,2 dimethyl-butane), production of

117

100 ’33-100 ‘39

NEOPENTANE (tetra methyl methane) and triptane (trimethyl butane), by Bueren

179

4308

OCTANE, alternate proposal for alkylation of Blechhammer stock. B.Sk 16

28

2167

102

i-OCTANE plant, construction of the Oppau

2

2168

10

10 ‘34-10 ‘37

OCTANE, dehydrochlorination of, proposed flowsheet of

28

2167

100

“ , detail flowsheet for the manufacture of, Part I, Kd 2034

28

2167

109

OCTANE, detail flowsheet for the manufacture of, Part III

28

2167

111

“ from mixed C4 hydrocarbons by chlorination, material balance for the manufacture of

28

2167

30

“ , general flowsheet for the manufacture of 20,000 tons per year of, Kd 2006b

28

2167

108

“ , hydrogenation of, over diluted catalyst and at lower pressures

251

134-139

“ , material balance for 4000 tons per year of

28

2167

18

“ , material balance for the manufacture of 50,000 tons per year of, Kd 539

28

2167

4

“ production, material balance, Kd 1615

28

2167

98

“ production, material balance, Kd 1616

28

2167

97

“ , production of, from butane, Leuna, M 1304-1

195

31164, 31165

“ production, proposed flowsheet for alkylation of Blechhammer stock, Kd 1617

28

2167

101

“ production, proposed tankage for, Kd 2226

28

2167

19

“ , summary flowsheet for the manufacture of, from isobutylalcohol, N5533-2

28

2167

20

i-OCTANE and methanol plant, starting the, in Waldenburg

2

2168

10

20 ’99-20 ‘107

PARAFFINS, chemical stability of

67

635

“ , chlorination of

81

4694-4702

i-PARAFFINS for aviation gasoline, production of pure

1

2168

5

80 ‘39-80 ‘41

“ , direct synthesis of, (first page missing)

101

20’11-20’21

PARAFFIN hydrocarbons, Bataafsche Petroleum Maatschappij research on analysis of

127

636-643

720-735

“ hydrocarbons, discussion of Koch and Billig’s article, Brennstoff-chemi, 1940, #14, on the study of

67

1221-1223

“ hydrocarbons, nitration of

56

7

933-940

“ hydrocarbons, production of oxidation products of high molecular weight

35

3440

92

30 ‘45-30 ‘57

“ , isomeric

253

389-402

“ , isomerization of, by Koch, 1943

138

XII

10 ‘29-10 ‘38

n- and i-PARAFFINS, kinetic investigations of the oxidation reaction of, (1942 Yearbook of the German Aviation Study)

94

421-431

PARAFFINS, mixtures of

43

3441

856

863-865

PARAFFIN mixtures, process of solidification of, thesis, W. Beier, 1938

134

20 ‘18-20 ‘64

“ , octane numbers of

165

427e-436

168

275-285

i-PARRAFINS, synthesis of, by S. Nishino

231

10 ’70 -10 ‘81

“ , the most important data and methods for the preparation of some, with particular regard to their use as motor fuel

168

229-237

n-PENTANE and n-butane, isomerization of

168

481-489

PENTANES and hexanes, isomerization constants

167

356-357

“ plant, off-gas flow diagram and, BK 263-8, Scholven

89

2243

19

60 ‘20

n-PENTATRIACONTANE, conversion of stearone into

79

2884-2895

“ , preparation of

79

2858

PENTRATRIACONTANE, preparation of

79

2966-2967

PEROPTANE, comparison of, with I-octane and triptane

219

0 ‘1-0 ‘15

PROPANE and propene mixtures, separation of

30

9..552-9..566

174

325-336

“ and propene, preparation of

29

19..743-19..746

“ , catalytic dehydrogenation of

14

1173-1175

“ dehydrogenation, material balance for, Kd 2007a

28

2167

119

“ , distribution of, between asphalt, gum and refined oil

57

153-161

“ removal, aviation gasoline, flow diagram, BK 303-8, Scholven

89

2243

13

60 ‘14

SLOW oxidation of hydrocarbons, studies of, by absorption spectra, by K. Nakata

231

40 ‘66-40 ‘83

TANOL plant (iso-octane)

2

2168

10

10 ‘38-10 ‘57

di- and TETRAHYDROPYRAN (II), derivatives of

22

57..749-57..752

2,2,3 TRIMETHYLBUTANE, preparation of, and other branched hydrocarbons by the hydro-genation of trimethylacetic acid

138

VII

0 ‘58-0 ‘61

168

324-326

TRIMETHYLBUTANE, the preparation of

138

VI

0 ‘53-0 ‘57

TRIMETHYLETHANE (P3), declaration of readiness for construction and brief description of processes

116

40 ‘41-40 ‘64

TRIMETHYLETHANE plant, flowsheet of, OS-182g

195

31747

“ production, flowsheet

193

23458

TRIOXYBUTANE plant in Rodleben

55

616-637

TRIPTANE

18

61..609

Translation

144

10 ‘23

30

3..316-3..317

“ and other alkylparaffins, experiments on the preparation of

168

330-338

“ and some other isoparaffins, experiments on the preparation of, by Bueren

174

117-125

178

3630-3638

“ from propylene and isobutane with HF and F compounds

14

1272

“ , knocking behavior of, in the I. G. test motor, by Witschakowski

179

4765-4768

“ (trimethylbutane) and neopentane (tetramethylbutane), by Bueren

179

4308