Table of Contents

HYDROGEN

 

 

 

 

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NITRIC oxide, removal of, from coke oven gas to be used for production of hydrogen, by Riese.  Article in Brennstoff-Chemie, August 1939, pp. 301-316

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2746

1

0 ‘67-0 ‘74

OPERATING age of hydrogen plant

37

3451

43

80 ‘23-80 ‘26

PARTIAL combustion processes, comparison of Rohrenofen and, for production of hydrogen from natural gas

65

Sec. III

20..114-20..11*

PRODUCTION at Louisiana, Mo. plant, Dr. O. Hubmann’s recommendations about hydrogen

 238

 

 

 40 ‘12-40 ‘16

     “         for hydrogenation plants, most economical hydrogen and fuel gas

 214

 

 

 30 ‘41-30 ‘64

     “         , hydrogen at Brabag Works at Troglitz-Zeitz, reported by J. F. Ellis and R. J. Morely

 226

 

 

 0 ‘61-0 ‘70

     “         , hydrogen, 1938, Bottrop

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2733

5

50 ‘64-50 ‘65

     “         , hydrogen, Wesseling synthetic fuel plant, reported by L. H. Mulit and R. C. Aldrich

 198

 

 

 30 ‘3-30 ‘21

     “         , methods of hydrogen

188

 

 

20655-20656

     “         of hydrogen and methane from coke oven gas at I.G. Farbenindustrie A.G., Hoechst/Main, reported by F. H. Reid

228

 

 

0 ‘3-0 ‘69

     “         of hydrogen, booklet describing, Linde

233

 

 

65-73

     “         of hydrogen, flowsheet for, Ruhroel

150

 

 

334

     “         of hydrogen, Scholven III

11

2247

12

40 ‘75-40 ‘79

 

 

 

 

40 ‘90-40 ‘10*

     “         records, hydrogen, 1941 and 1940

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2747

3

30 ‘73-30 ‘93

     “         unit, hydrogen, Linde

176

 

 

222-223

PURIFICATION, hydrogen

117

 

 

60 ‘4

     “         , hydrogen, flowsheet for

31

2078

 

59..288

 

117

 

 

50 ‘86-50 ‘87

     “         , hydrogen, in Oppau in 1941, report on

17

 

 

22..420-22..4**

     “         of hydrogen, notes on

116

 

 

40 ‘66-40 ‘70

RECOVERY of hydrogen by Linde-Frδnkl and cuprous salt scrubbing, comparison of

 1

 2168

 15

10 ‘37-10 ‘42

     “         of hydrogen in Linde liquefaction process

176

 

 

225

                                Translation T-261

273

 

 

382

REFRIGERATION, drying of reaction hydrogen and separation of gasoline by

 50

 

 

569-572

REQUIREMENTS, pure hydrogen, in Baehrheim

215

 

 

30 ‘8-30 ‘16

ROHRENOFEN and partial combustion processes, comparison of, for production of hydrogen

65

Sec. III

20..114-20..118

SHIFT reaction for water gas

71

 

 

140-155

     “         reaction, oxygen, Bamag

1

2168

25-28

10 ‘59-10 ‘61

     “         reaction, steam consumption in        

57

 

 

528-588

SOLUBILITY, hydrogen, in liquid hydrocarbons

167

 

 

296-298

STARTING hydrogen plant in Lutzkendorf

1

2168

194

40 ‘70-40 ‘87

SUPPLY, hydrogen, at Ludwigshafen and Oppau

32-I

 

 

165.1345-165.1354

     “         , hydrogen, for high pressure plant

1

2168

101-105

30 ‘66-30 ‘70

TAIL gas, hydrogen from

11

2247

12

50 ‘2

TRANSFER of hydrogen production plant from Leuna to Lutzkendorf

1

 2168

 196

40 ‘92-40 ‘95

 

 

 

197

40 ‘96-40 ‘98

USE of hydrogen in combustion motors

222

 

 

3625-3631