ALCOHOLS

ALCOHOLS, by Giesen

205

565-579

“ and ethers, preparation of from Fischer LPG

40

3453

13

0 ‘55-0 ‘87

“ as aviation fuel, engine test of, by K. Sunoda

231

50 ‘109-50 ‘117

ALCOHOL distillation plant, flow sheet for, Leuna M 7872-2

195

31785

“ fermentation, research on, by T. Umemura, S. Nakamura, T. Fukuzake, Y. Noda, and M. Takahashe

231

50 ‘1-50 ‘22

“ from mixtures with hydrocarbons, separation of, by Geiseler, April 1943

134

70 ‘123-70 ‘124

“ fuel utility test as aero engine fuel, by T. Kondo and S. Soma

231

60 ‘1-60 ‘7

, hydrogenation of fatty acids to

119

80 ‘91-80 ‘94

“ , formation of in the aldehyde synthesis

42

662-663

Translation S-76

274

1737

“ plant, report on Kyushu regional fuel depart-ment, Shimabara, Kyushu

231

60 ‘8-60 ‘16

“ from Fischer LPG, preparation of ,

40

15

0 ‘55-0 ‘87

10 ‘3-10 ‘41

“ production costs

43

2719

641-644

122

40

102620-102645

“ , “ of

45

79

73-89

“ to fatty acids by caustic fusion

14

692-693

ALDEHYDES, hydrogenation of,

55

528-531

ALIPHATIC alcohols as plasticizers in the rubber industry

122

25

102374

“ “ , letter on,

55

86-87

“ “ , separation of, from associated hydro-carbons, with aqueous methanol

23

16..532-16..548

Do., by Meusel

134

70 ‘105-70 ‘117

Translation, Texaco Co.

244

30 ‘93-30 ‘107

ALLYL alcohol, flow sheet for the fractionation of, Kd 1926

28

2167

77

“ alcohol, separation from mixtures by wash distillation

55

719-721

“ alcohol manufactured from propargyl alcohol, proposed method of,

27

2077

23..169-23..17*

AMYL alcohol plant, flow diagrams, Leuna, M2121 a-2, M-4415-2, M-1675 a-2

116

20 ‘4-20 ‘7

20 ‘16

i-AMYL alcohol from acetopropionaldol

22

40..645-40..65*

ANALYSIS of synthetic alcohols

3

2168

13

10 ‘82

AVIATION fuel, studies on the utilization of alcohols for, by T. Yamamoto

231

50 ‘118-50 ‘121

BUTANOL, comparison of crotonaldehyde hydrogenation to, Dehvdag & J.T. methods of

55

520-524

“ , dehydration of, 800 mm, diam. reactor, N 4903-4

28

2167

22

BUTANOL, dehydration of, 1300 mm, diam. reactor, Kd 2209

28

2167

23

“ , dehydration of, flow sheet for, N-9722-2

28

2167

105

“ , dehydration of, polymerization of butylene and depolymerization of tri-butylene, N 2607-1

28

2167

21

“ , distillation of, handwritten notes, Schkopau

105

10686-10690

“ , studies on fermentation, by T. Umemora, S. Stakida, S. Shimada and M. Takahashe

231

50 ‘34-50 ‘62

“ , fractionation, instrument details I, BKOBS 1978-8

28

2167

16

“ , fractionation, instruments details II, BKOBS 1978-8

28

2167

17

“ , fractionation of, details column I, N-5321-8

28

2167

9

“ fractionation of, details column II, N 5322-8

28

2167

10

“ fractionation of, details column IIa, N 5323-8

28

2167

11

“ fractionation of, details column III, N 5324-8

28

2167

12

“ fractionation of, details column IV, N 5325-8

28

2167

13

“ fractionation of, details column V, N 5326-8

28

2167

14

“ fractionation of, details column VI, N 5327-8

28

2167

15

“ fractionation of, detail flow sheet for, part 1, N 2640-1

28

2167

6

“ fractionation of, detail flow sheet part 2, N 2641-1

28

2167

7

“ fractionation of, detail flow sheet for, part 3, N-2427e-1

28

2167

8

“ fractionation of raw, flow sheet for Kd 1848

28

2167

3

“ fractionation of raw, Ludwigshafen drawing, N 4186-4

28

2167

1 & 2

“ fractionation, N3989c-1

28

2167

104

“ “ , N5392-4

28

2167

5

“ products from, flow sheet

28

2167

103

“ working up

173

867-869

BUTANOL-crotanol mixtures, separation of,

55

724-732

BUTANOL, study of the use of the 200 te/mo crotyl alcohol plant for the manufacture of,

55

532-539

“ synthesis, use of off-gases of the

2

2168

10

50 ‘6-50 ‘9

i-BUTANOL

30

5..436-5..462

“ , distillation of,

2

2168

10

20 ’61-20 ‘70

“ “ discussion of crude, Jan. 1944

29

10..584-10..591

“ plant in Oppau, drawings of,

2

2168

10

10 ’92-10 ’109

“ production, 1936

54

152-168

“ , discussion of the productions of November 1943

134

90 ‘1-90 ‘6

“ , production of,

2

2168

10

0 ‘25-0 ‘41

“ , “ “, in Leuna

2

2168

10

20 ‘17-20 ‘24

“ “ , plans for, June 1944

29

10..591-10..632

“ , synthesis of from water gas, by S. Endo and T. Inoue

231

50 ‘105-50 ‘108

BUTANOL-tanol plant, installation of

165

578-584

BUTANOL, tert., separation from i-propanol

55

740-743

BUTOL 1-3, flow sheet for

31

2078

53..281

“ with its by-products, manufacturing process of,

105

10578-10588

BUTYL and methanol synthesis, materials of construction for,

65

Sect. III

44.00256-44.0026*

“ catalyst at low pressures, resistance measure-ments with

2

2168

10

10 ‘1-10 ‘8

“ circuit, increased CO content in the

2

2168

10

0 ‘41-0 ‘48

“ oil distilling column at Oppau

155

117-124

“ “ distillation, operating description of,

31

2078

86..337-86..339

“ synthesis, effect of pressure in the

2

2168

10

10 ‘14-10 ‘21

“ “ , methane formation in

2

2168

10

0 ‘40-0 ‘67

i-BUTYL oil, driving methanol out from crude

29

10..568-10..580

“ converter drawing, A.F.T. 2553

181

6333

“ vapor phase converter. Mineralol Baugesellschaft, 2341-1

179

4856

“ distillation, flow sheet of,

117

60 ‘18

“ plant, Leuna, M 10235-4

179

4840

“ oil and methanol distillation, 1939-1940, operation record for 1939

134

80 ‘82-80 ‘131

“ oil and methanol production flow sheet

193

23488

“ oil, compounds isolated from

29

10..637-10..63*

134

80 ’56-80 ‘58

“ “ with pentane, description of operations of preliminary extraction of,

29

10..632-10..63*

“ oil, determination and elimination of the non-alcoholic oxygenated constituents of, volatile with the methanol vapors

2

2168

10

10 ‘22-10 ‘30

“ oil distillation flow sheet

31

2078

87..340

i-BUTYL oil, distillation of,

2

2168

10

20 ‘1-20 ‘16

“ “ , “ “

2

2168

10

30 ‘1-30 ‘63

193

23478

“ “ , “ “ raw, January 1944

134

80 ‘59-80 ‘66

“ “ , gasoline from, by hydrogenation

173

861-863

“ “ plant, enlarging the existing, with brief description

116

40 ‘81-40 ‘88

“ “ production, economics of, 1943

115

40 ‘59-40 ‘108

“ “ , flow sheet of products from

117

60 ‘31

“ “ residues, working up of

173

858-860

193

23479-23480

CATALYTIC reduction of free fatty acids to the corresponding alcohols

32-I

160.1310-160.1314

COMPARISON of middle pressure and high pressure methanol synthesis method of the I.G.

134

90 ‘84

COMPUTATION of conversion in the ammonia, methanol and other synthesis from gas analytical data, 1933

192

22418-22428

CONVERSION of high molecular weight unsaturated hydrocarbons into alcohols

164

581-584

CONVERTER, 500 atm methanol, Leuna M 1370-1

181

6313

CROTYL alcohol butanol mixtures, separation of

55

724-732

CYCLOHEXANOL, description of manufacture and distillation of, with drawing M 6881-16 and M 6882-16

152

698-710

“ from phenol

119

80 ‘73 ’80 ‘74

“ , layout of plant for the production of 1350 te/mo. of, Leuna M 4733b-1

195

31673

“ plant, layout of, Leuna M-6459-2, M-5353-2

116

10 ‘51-10 ‘60

DIACETONE alcohol from acetone

72

689-718

“ “ , experiments on preparation of, (Pyranton A)

53

567-581

5-DIETHYL amino pentanol-2 by the Reppe process, preparation of, reported by J. D. Rose

227

20 ‘76-20 ‘82

DIPROPYLCARBINOL from butyric acid

32-II

2078

214..1655

DISTILLATION plant, the design of a simplified alcohol, by A. Sheome

231

50 ‘63-50 ‘68

“ unit, enlarging the methanol

116

50 ‘47-50 ‘59

ETHANOL fermentation, studies on, by T. Asia and K. Shibake

231

40 ‘108-40 ‘113

ETHYL alcohol, studies on, by O. Miyata

231

50 ‘95-50 ‘104

2-ETHYL hexanol, experimental preparation of,

154

264-271

FATTY acids to alcohols, hydrogenation of

119

80 ‘91-80 ‘94

“ alcohols, research problems on

42

970-971

FLOW sheet methanol production

117

60 ‘16-60 ‘17

GAS flow sheet of the methanol plant (East)

193

23439

HEPTYL alcohol to C₁₂ alcohols, preparation of from olefins

70

685

HEXANOL, dehydrogenation of, Schkopau and Leuna. Conclusions on constitution of hexanol from the butyl distillation

154

179-183

HIGHER alcohols and methanol synthesis, reported by R. L. Morley

197

60 ‘63-60 ‘65

“ “ from olefins, production of

134

100 ‘151-100 ‘276

“ “ , preparation of

70

692-693

“ “ , production of,

72

438-489

“ “ from cracked petroleum gases, studies on the production of, by T. Etakura

231

50 ‘86-50 ‘94

HYDROGENATION of a mixture of alcohol, butanol and water and its separation by continuous distillation

154

168-175

354-363

MATERIAL balance in Avenarius alcohol plant

71

330-334

METHANOL plant lay out, Leuna M 10199-4

179

4841

“ formaldehyde, 1943/44

54

672-673

“ , toluene and nitric acid situation, the German, by K. Mayer

205

480-482

“ production, changing the Fürstenberg ammonia plant to, 1944

55

678-679

“ , import duty on,

2

2168

10

20 ‘71-20 ‘72

“ and benzene, comparative test with, as fuels for Otto engines

106

28802-28826

“ as an engine fuel

106

28017-28029

109

9421-9452

112

1112-1130

“ , nitric acid and toluene production in Germany, state of

13

3043

2

30 ‘96-30 ‘100

METHYL ethyl carbinol and i-propanol, production of,

180

6052-6062

67

695-703

“ “ “ and iso propyl alcohol preparation of,

46

368-376

“ Translation by S. O. Co. (Indiana)

234

50 ‘36-50 ‘40

“ formate, continuous process of formation of, from methanol and carbon monoxide

134

90 ‘25-90 ‘59

“ formate from methanol and carbon monoxide, using CO-containing gases

134

90 ’74-90 ‘79

METHYL formate, hydrogenation of,

134

90 ‘22-90 ‘24

134

90 ’60-90 ‘73

“ “ to methanol, drawing, experimental tube for hydrogenation of

55

476

OCTADECYL alcohol from stearic acid

79

2864-2867

OXO alcohols and synol, processing of, with flow sheets

193

23355-23365

“ “ , the constitution of,

134

100 ’28-100 ‘29

Translation, Texaco

244

30 ‘115-30 ‘117

“ alcohols, viscosity of,

155

53-68

“ synthesis products, alcohol production from, costs, heat balance etc.

14

564-584

PLANT for production of 28 te/mo of methyl formate, corresponding to 15 te/mo of methanol, description of,

134

90 ‘80-90 ‘83

POLY alcohols from butadiene oil and raw butadiene gas

154

255-256

POLYSTYROL, description of plant and production of, Schkopau

151

975-977

PRODUCTION flow sheets, methanol and isobutyl oil

193

23488

“ , methanol in Waldenburg

2

2168

10

10 ‘58-10 ‘64

10 ’67-10 ‘76

“ flow sheet of pure and either-containing methanol, O. A. Sk 1

195

31672

“ of methanol in relation to the gas composition (chart)

13

3043

3

60 ‘24

“ of methanol, toluene, and nitric acid in Germany, state of

13

3043

2

30 ‘96-30 ‘100

i-PROPANOL and methyl-ethyl carbinol, preparation of,

46

368-376

Do., by Grimme

67

695-703

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

243

50 ‘36-50 ‘40

180

6052-6061

“ and secondary butyl alcohol specifications for,

122

35

102517

“ plant, Ruhrchemie

49

75-82

“ , separation from tert. Butanol

55

740-743

PROPANOL production from hydrogenation off-gases, Leuna, flow sheet of,

195

31749

PROPARGYL alcohol containing formic acid on iron, effect of aqueous

27

2077

21..167

“ alcohol liquor, distillation of

32-11

2078

192.1530-192.1535

“ “ , oxidation products of

32-11

2078

186.1511-187.1516

“ “ rust remover PL

27

2077

19..165-20..166

“ “ from formaldehyde by vacuum distillation, flow sheet for separation of,

27

2077

22..168

PROPARGYL alcohol and butenediol, reaction with alkalies

31

2078

16..156-16.161

REACTOR, methanol - 500 mm, with cooling gas line, Leuna M 1370-1

195

31742

“ stall for methanol, Leuna M 10234-4

179

4837

Do. M 10236-4

4839

RECOVERY of alcohols from the off-water of the activated charcoal unit, 1943

46

441-445

180

6082-6086

SECONDARY butyl alcohol and isopropyl alcohol, specifications for

122

35

102517

SEPARATION of methyl alcohol and butyraldehyde

31

2078

88..341

SORBITOL-glycerine

117

100 ‘48

STARTING the methanol and iso octane plants in Waldenburg

2

2168

10

20 ‘99-20 ‘107

STYROL, production of,

154

299a-302

“ , reactions of,

154

224-231

SYNOL and oxo alcohols, processing of with flow sheets

193

23355-23365

SYNTHESIS, alcohol, by gas recycle process

166

709-712

“ , alcohols from medium pressure

128

556-557

“ , alcohols to 1936

54

215-239

“ at Oppau, methanol, reported by J. Robell and Wm. L. E. Dewling

240

60 ‘1-60 ‘16

“ flow sheets, two, (methanol?)

193

23476-23477

“ , heat of reaction and thermodynamic equilibrium of methanol

192

22272-22279

“ , materials of construction for butyl and methanol

65

Sect. II

44..256-44..266

“ , methanol

42

930

55

2523

752-772

Translation, Texas Co.

243

30 ‘45-30 ‘57

“ , methanol and higher alcohols, reported by R. L. Morley

197

60 ‘63-60 ‘65

“ , methanol, and high pressure hydrogenation, Dr. Pier’s lecture 1942, on recent develop-ments in

174

337-379

“ of methanol, by S. Endo

231

50 ‘69-50 ‘85

“ “ “ and the catalytic high pressure hydrogenation from the ammonia synthesis, development of to the present stage

24

9..322-9..324

“ of methanol, experiments on

37

3451

33

55

427-466

“ “ “ from carbon monoxide and hydrogen

134

90 ‘7-90 ‘21

SYNTHESIS of methanol from water gas, formation of higher alcohols in the

55

410-426

“ of methanol middle pressure

55

467-469

134

90 ’85-90 ‘89

192

22245-22271

“ , methanol, monthly report, Nov. 1942

55

474-475

“ of methanol with ternary Zn-Mn-Cr catalyst (Mm2)

65

Sect. VIII

1.001-1.003

“ plant, sketch methanol, Leuna M 12741-2

179

4827

Do. Leuna, M 6283-1

4844-4845

“ products, alcohol from

166

814-815

“ “ , Michael, alcohols from (Illegible)

166

701-704

166

705-708

254

512-515

“ , semi-annual reports on methanol, 1943

55

470-473

SYNTHETIC higher aliphatic alcohols, equipment for production of,

122

26

102382-102385

TANK storage for methanol, Leuna, M 12718-2

179

4831

WOLFGANG methanol plant, description of,

55

477-479

WORKING up of alcohols (dimere alcohols)

15

2433-2435