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.