I.C. 7370
Report on the Investigation by Fuels and Lubricants Teams at the I.G. Farbenindustrie A.G. Leuna Works, Meresburg, Germany - 1946
Holroyd, R.1
Page | |||||
Section
1 1201kb |
Forward | i | |||
Introduction, by R. Holroyd | ii | ||||
Personnel of visiting teams | iii | ||||
I. | Gas production, by G.U. Hopton, R. J. Morley, L. L. Newman, and W. W. Odell | 1 | |||
Gas Production | 1 | ||||
Water-gas generators | 1 | ||||
Winkler generators | 2 | ||||
Slagging producers ("Abstichgeneratoren") | 5 | ||||
Pattenhausen generator | 6 | ||||
Oxygen plant | 6 | ||||
Section
2 1096kb |
Documents in connection with gas production | 7 | |||
H2S removal | 7 | ||||
Alkacid process | 7 | ||||
Active carbon process | 8 | ||||
Organic sulphur | 9 | ||||
CO conversion | 9 | ||||
II. | Ammonia synthesis, by R. J. Morley and W. W. Odell | 10 | |||
General | 10 | ||||
Staff interviewed | 10 | ||||
Compression | 10 | ||||
CO2 removal | 11 | ||||
CO removal | 12 | ||||
Final NH3 make-up gas purification | 12 | ||||
NH3 synthesis | 12 | ||||
Circulator | 13 | ||||
Catalyst | 13 | ||||
Converters | 14 | ||||
Section
3 1262kb |
III. | Methanol and higher alcohol synthesis, by R. J. Morley | 15 | ||
Methanol | 15 | ||||
Higher alcohols | 15 | ||||
IV. | Hydrogenation, by R. Holroyd and W. F. Faragher | 18 | |||
A. | General | 18 | |||
B. | Brown-coal hydrogenation | 18 | |||
(i) | Outline of present process | 18 | |||
(ii) | Consideration of process improvements made since the war | 20 | |||
Section
4 1100kb |
(iii) | Details of plant equipment | 22 | ||
C. | Brown-coal tar hydrogenation | 24 | |||
D. | Vapour-phase hydrogenation of middle oils | 25 | |||
(i) | process conditions and yields | 25 | |||
(ii) | Details of plant | 27 | |||
Section
5 1833kb |
E. | Vapour-phase splitting hydrogenation at 700 atmospheres pressure | 28 | ||
F. | Hydrogenation costs | 29 | |||
Section
6 986kb |
V. | D. H. D. (Dehydrierung - Hoch - Druck) process | 38 | ||
(i) | Description of process and Leuna operating results | 38 | |||
(ii) | Costs | 40 | |||
Section
7 920kb |
VI. | Hydroforming process, by E. Cotton and V. Haensel | 43 | ||
VII. | Arobin process, by D. A. Howes, J. G. Allen, and H. Schindler | 46 | |||
Charge to Arobin plant | 46 | ||||
Operating conditions | 46 | ||||
Yield and quality of the product | 47 | ||||
Preparation of the Arobin catalyst | 47 | ||||
Section
8 1227kb |
VIII. | Catalytic cracking, by E. Cotton and V. Haensel | 49 | ||
Introduction | 49 | ||||
Reaction conditions | 49 | ||||
Catalyst | 49 | ||||
Products | 50 | ||||
Catalyst life | 51 | ||||
Hydrogenation of product | 51 | ||||
Conclusions | 51 | ||||
IX. | Dehydrogenation of butane - alkylation, by D. A. Howes, J. G. Allen, and H. Schindler | 52 | |||
Introduction | 52 | ||||
Summary of operations | 52 | ||||
Dehydrogenation | 52 | ||||
Section
9 1051kb |
Catalyst regeneration | 54 | |||
Catalyst manufacture | 54 | ||||
Preparation of alkylation feed stock | 55 | ||||
Alkylation | 55 | ||||
Alkylate quality | 56 | ||||
Alkylate production in Germany | 56 | ||||
Economics of Leuna operation | 57 | ||||
Section
10 1030kb |
X. | Isomerization of normal butane, by E. Cotton and V. Haensel | 59 | ||
XI. | Synthetic lubricating-oil manufacture - Leuna, by D. A. Howes, J. G. Allen, H. Schindler, C. C. Chaffee, and R. J. Ozol | 60 | |||
Summary of process | 60 | ||||
Process details | 60 | ||||
(1) | Thermal cracking of ethane | 60 | |||
(2) | Acetylene removal | 61 | |||
(3) | Oil absorption | 61 | |||
(4) | Activated-charcoal absorption | 61 | |||
(5) | Alkazid washer | 61 | |||
(6) | Caustic washer | 61 | |||
(7) | Linde low-temperature fractionation | 62 | |||
(8) | Polymerization of ethylene to lubricating oil | 62 | |||
(9) | Catalyst separation and disposal | 63 | |||
Section
11 1360kb |
(10) | Oil fractionation | 64 | ||
Operating requirements | 64 | ||||
Tests on products | 65 | ||||
Production data | 66 | ||||
Notes on catalysts and reaction conditions | 67 | ||||
(1) | Acetylene removal catalyst | 67 | |||
(2) | Ethylene purity required | 67 | |||
(3) | Polymerization catalyst | 68 | |||
Theory of lubrication | 68 | ||||
Sources of olefines | 71 | ||||
Hydrocarbon synthesis | 71 | ||||
Lubricating-oil additives and special products | 72 | ||||
I. | Additives | 72 | |||
Section
12 1348kb |
II. | Special lubricants | 75 | ||
Conclusions and recommendation | 77 | ||||
XII. | Synthetic lubrication oil - Schkopau, by P. K. Kuhne | 78 | |||
Introduction | 78 | ||||
Description of the process | 78 | ||||
Miscellaneous | 80 | ||||
Conclusions | 80 | ||||
XIIA. | Synthetic lubricating-oil manufacture at Stettin-Pölitz, by D. A. Howes, J. G. Allen, and H. Schindler | 81 | |||
Source of information | 81 | ||||
Summary | 81 | ||||
Description of process | 81 | ||||
Wax cracking | 81 | ||||
Polymerization | 82 | ||||
Refining of polymerized oil | 82 | ||||
Tests on products | 83 | ||||
Yields | 83 | ||||
XIII. | Aviation fuel manufacture and engine testing, by D. A. Howes, J. G. Allen, and H. Schindler | 84 | |||
Introduction | 84 | ||||
Octane number determination and specification | 84 | ||||
Section
13 1235kb |
B. M. W. 3-litre single-cylinder aero engine | 85 | |||
Aviation gasoline | 85 | ||||
Nomenclature of aviation fuels | 86 | ||||
XIV. | OXO process, by v. Haensel and J. P. Jones | 87 | |||
Introduction | 87 | ||||
Chemistry of the OXO process | 87 | ||||
Process conditions | 88 | ||||
Leuna operation | 88 | ||||
Catalyst preparation | 91 | ||||
Section
14 1326kb |
OXO processing of cracked middle oil | 92 | |||
XV. | Synol process, by V. Haensel, J. P. Jones, and W. A. Horne | 93 | |||
Synthesis gas | 93 | ||||
Scale of operations | 93 | ||||
Process conditions | 93 | ||||
Yields | 94 | ||||
Design of reactors | 95 | ||||
Catalyst preparation | 95 | ||||
Work-up of crude Synol product | 96 | ||||
Section
15 1215kb |
XVI. | Mersol process, by A. J. V. Underwood | 98 | ||
Scale of operation | 98 | ||||
Process conditions | 98 | ||||
XVII. | Methylamine, by R. J. Morley | 100 | |||
Isobutylamine manufacture | 100 | ||||
Schiff's base | 101 | ||||
XVIII. | Manufacture of carboxylic acids, by D. A. Howes, J. G. Allen, and H. Schindler | 102 | |||
XIX. | Polymerization of C6 and C7 olefines, by D. A. Howes, J. G. Allen, and H. Schindler | 103 | |||
XX. | Fertilizers and nitric acid, by R. J. Morley | 104 | |||
Ammonium sulphate | 104 | ||||
Nitric acid | 105 | ||||
Concentrated nitric acid | 105 | ||||
Ammonium nitrate | 105 | ||||
Calcium nitrate (Kalksalpeter) | 106 | ||||
Phosphate fertilizers | 106 | ||||
Leuna saltpeter (ammonium sulphate and nitrate) | 106 | ||||
Ammonium chloride fertilizers | 106 | ||||
Section
16 1106kb |
XXI. | Synthesis of toluene from benzene and methanol, by R. Holroyd and C. C. Chaffee | 107 | ||
Introduction | 107 | ||||
General process data | 107 | ||||
Plant operation | 108 | ||||
Development work on related processes | 109 | ||||
XXII. | Catalyst preparation, by W. A. Horne and W. F. Faragher | 110 | |||
Catalyst 616 | 110 | ||||
Catalyst 1132 | 111 | ||||
Catalyst 1750 | 111 | ||||
Catalyst 2493 | 111 | ||||
Catalyst 2730 | 112 | ||||
Catalyst 3076 | 112 | ||||
Catalyst 3390 | 112 | ||||
Catalyst 3510 | 113 | ||||
Catalyst 4577 | 113 | ||||
Catalyst 4788 | 114 | ||||
Catalyst 4821 | 114 | ||||
Catalyst 5058 | 114 | ||||
Catalyst 5436 | 115 | ||||
Catalyst 5623 | 115 | ||||
Section
17 1588kb |
Catalyst 5633 | 116 | |||
Catalyst 5780 | 116 | ||||
Catalyst 6067 | 116 | ||||
Catalyst 6069 | 117 | ||||
Catalyst 6448 | 117 | ||||
Catalyst 6523 | 117 | ||||
Catalyst 6853 | 117 | ||||
Catalyst 7187 | 118 | ||||
Catalyst 10927 | 118 | ||||
Ammonia-catalyst (no number) | 118 | ||||
XXIII. | Metallurgy, by J. F. Ellis | 119 | |||
I. G. experience with hydrogen-resistant steels | 119 | ||||
Enamelling of preheater bends | 120 | ||||
Chromium-plated injector rams | 120 | ||||
Material for butane dehydrogenation reactor tubes | 121 | ||||
Material for catalytic cracking regenerators | 121 | ||||
XXIV. | Bleohhammer, by r. Holroyd and W. F. Faragher | 122 | |||
Introduction | 122 | ||||
Details of coal hydrogenation to give excess heavy oil | 124 | ||||
Phenol extraction | 126 | ||||
Treatment of hydrocarbon bases | 127 | ||||
Costs | 127 | ||||
Section
18 1897kb |
XXV. | Brüx, by R. Holroyd and W. F. Faragher | 128 | ||
Introduction | 128 | ||||
General outline of the Brüx factory | 128 | ||||
(a) | Brown-coal carbonization | 128 | |||
(b) | Hydrogen production | 128 | |||
(c) | Hydrogenation plant | 129 | |||
(d) | Phenol extractions | 129 | |||
Operation of the hydrogenation units | 129 | ||||
Costs | 130 | ||||
Present condition of Brüx plant | 130 | ||||
Underground hydrogenation plant | 130 | ||||
XXVI. | German oil production, by R. Holroyd | 133 | |||
XXVII. | Use of bottled propane and butane for road vehicles, by R. Holroyd and J. F. Ellis | 135 |
1 British Ministry of Fuel and Power.