Section 1 534kb | Foreword | i |
Author's Preface | ii |
Contents | v |
List of Illustrations | ix |
List of Tables | xi |
Introduction | 15 |
Section 2 608kb | I. | Extraction by Solvents | 20 |
| (a) | The Yield of Oil by Extraction | 20 |
| (b) | Identification of Chemical Compounds in the Extracts | 20 |
II. | Production and Working-Up of Primary Tar | 22 |
| (a) | Methods of Destructive Distillation of Fuels | 22 |
| (b) | Special Laboratory Methods for the Production of Primary Tar | 24 |
| (c) | Yields of Primary Tar From Coal and Peat | 25 |
| (d) | Proximate Composition of Primary Tars | 27 |
| (e) | The Temperatures Required for the Production of Primary Tar | 28 |
Section 3 779kb | | (f) | Differentiation Between Various Primary Tars and Other Tars | 30 |
| (g) | The Chemical Compounds Found in Primary Tar and in Primary Benzines | 38 |
| (h) | The Liquor From Low-Temperature Carbonization | 43 |
| (i) | Composition and Application of Low-Temperature Carbonization Gas | 43 |
Section 4 865kb | | (k) | The Low-Temperature Benzine | 46 |
| (l) | The Position of Primary Tar Between Coke-Oven Tar and Petroleum | 49 |
| (m) | Semi-Coke | 50 |
| (n) | The Heat Balance of Low-Temperature Carbonization | 56 |
| (o) | The Development of Commercial Primary Tar Production | 58 |
| | 1. | Distillation Apparatus with External Heating | 59 |
| | | | Vertical Retorts | 60 |
Section 5 939kb | | | | | Horizontal Retorts | 64 |
| | | | Tunnel Kilns | 68 |
| | | | Rotary Retorts | 71 |
| | | | Retorts with Inner Lining | 76 |
| | 2. | Internal Heating | 76 |
| | | | Superheated Steam as Heating Agent | 76 |
| | | | Hot Producer Gas as Heating Medium | 78 |
| | | | Hot Coke-oven Gas as Heating Medium | 79 |
| | | | Carbonisation by means of Flue Gasses | 80 |
Section 6 1002kb | | | 3. | Combined Apparatus | 81 |
| | | | Hot-Run Generators fitted with Carbonising Retorts | 81 |
| | | | Retorts Combined with Low-Temperature Producers | 84 |
| | | | Preliminary Carbonization of Furnace Fuel | 87 |
| (p) | The Influence of Retort Design Upon the Composition of Primary Tars and Gas Benzines | 89 |
| (q) | The Influence of Coal Drying on the Oil Recovery | 91 |
| (r) | Utilisation and Working-Up of Primary Tar | 94 |
| | 1. | Direct Utilisation of Primary Tar | 94 |
| | 2. | Working-Up of Primary Tar by Distillation | 94 |
| | | | Chemical Changes on Distillation | 94 |
Section 7 544kb | | | | | Working-up by Distillation at Ordinary Pressure | 97 |
| | | | Distillation at Ordinary Pressure and Chemical Treatment | 99 |
| | | | Working-up of Primary Tar by means of Superheated Steam and Chemical Treatment | 100 |
| | | | Working-up in a High Vacuum | 104 |
| | 3. | Separation and Utilisation of Phenols | 106 |
| | | | The Disadvantages of Phenols and their Corrosion of Metals | 106 |
| | | | The Utilisation of Phenols | 108 |
| | | | Methods of Separation of Phenols hitherto in Use | 108 |
Section 8 292kb | | | | | The Recovery of the Phenols by means of Superheated Water | 110 |
Section 9 959kb | | | 4. | The Reduction of Phenols of Primary Coal Tar to Benzol and Toluol | 117 |
Section 10 605kb | | | 5. | Benzine by Destructive Distillation of Primary Tar from Bituminous or Brown Coal | 137 |
| | | | Benzine by Cracking of Primary Tar at Ordinary Pressure | 140 |
| | | | Benzine by Cracking under Pressure | 146 |
Section 11 705kb | | | | | Benzine by the Burton Process | 150 |
| | | | Benzine by Cracking and Simultaneous Hydrogenation under High Pressure | 151 |
| | 6. | The Hydrogenation of Primary Tars, Tar Oils and Phenols | 158 |
| | | | With Catalysts | 158 |
| | | | Without Catalysts | 159 |
| | 7. | Summary of the Recovery of Light Motor Spirits From Primary Tars | 160 |
| | 8. | Purification of Primary Tar Oils by Oxidation Under Pressure | 164 |
Section 12 414kb | | | 9. | Formation of resins and Asphalt from Primary Tar by Oxidation under Pressure | 166 |
| | 10. | Fatty Acids from Crude Paraffin Wax by Oxidation under Pressure | 166 |
| (s) | Conversion of Low-Temperature Carbonisation Tar into Coke-oven Tar | 166 |
| (t) | Conversion of Brown Coal Tar into Aromatic Tar | 169 |
| (u) | Liquid Motor Fuels by Hydrogenation of Coal Tar, and Especially by Naphthalene | 170 |
| (v) | Importance of Primary Tar as Raw Material | 173 |
Section 13 568kb | II. | Hydrogenation of Coal | 174 |
| (a) | By Means of Hydriodic Acid Under Pressure According to Berthelot | 174 |
| (b) | Comparative Hydrogenation of Different Coals with Hydriodic | 177 |
| (c) | Hydrogenation by Means of Sodium Formate | 179 |
Section 14 626kb | | (d) | Hydrogenation by Means of Carbon Monoxide and Water | 187 |
| (e) | Hydrogenation with Sodium Carbonate and Hydrogen | 195 |
| (f) | Destructive Distillation of Bituminous Coal at Higher Hydrogen Pressures | 197 |
| (g) | Hydrogenation of Coal According to Bergius at High Hydrogen Pressure | 198 |
Section 15 569kb | IV. | Synthetic Processes | 202 |
| (a) | The Action of Electric Discharges | 202 |
| (b) | Catalytic Experiments at Ordinary Pressure | 203 |
| (c) | Liquid Hydrocarbons from Carbon Monoxide and Hydrogen Under Pressure | 206 |
| (d) | Alcohols and Formaldehyde from Carbon Monoxide and Hydrogen Under Pressure | 210 |
| (e) | Methyl Alcohol and Oils by Decomposition of Formates | 211 |
Section 16 610kb | | (f) | Synthol From Carbon Monoxide and Water Vapour Under Pressure | 213 |
| (g) | Catalytic Experiments in the Presence of Nitrogen | 219 |
| (h) | Catalytic Experiments with Carbon Dioxide and Hydrogen under Pressure | 221 |
| (i) | Synthol from Water Gas Under Pressure | 221 |
| | 1. | On the Need of a Metallic Hydrogen Carrier in the Contact Material | 221 |
| | 2. | Influence of the Form and Length by the Contact Material | 223 |
| | 3. | Influence of Bases and their Quantity upon the Oil Yield | 224 |
Section 17 646kb | | | 4. | Experiments with Hydrogen Carriers other than Iron | 227 |
| | 5. | Influence of the Composition of Water Gas | 229 |
| | 6. | Influence of Impurities in Water Gas | 232 |
| | 7. | Influence of Temperature, Pressure and Gas Velocity | 232 |
| | 8. | Determination of Yields in the Circulation Apparatus | 234 |
| (k) | Carbon Dioxide and Hydrogen in the Circulation Apparatus | 240 |
| (l) | Carbon Dioxide and Methane in the Circulation Apparatus | 241 |
Section 18 641kb | | (m) | Carbon Monoxide and Methane in the Circulation Apparatus | 241 |
| (n) | Examination of Products of Reaction | 246 |
| (o) | Road Tests of Synthol | 248 |
| (p) | Conversion of Synthol into Synthin | 248 |
| (q) | Formation of Petroleum from Water Gas | 248 |
| (r) | Attempt at an Explanation of the Synthol Process | 250 |
Section 19 664kb | | (s) | Industrial Applicability of the Synthol Process | 255 |
V. | Hydrocarbons from Carbides | 258 |
| (a) | Carbides which Directly Yield Liquid Hydrocarbons | 258 |
| (b) | Carbides Giving Hydrocarbons which can be Converted inot Liquids | 261 |
Appendix (Editor's Notes) | 263 |
| (a) | Recent Developments in Low-Temperature Carbonisation | 263 |
| | | Parker Plant | 263 |
| | | Maclaurin | 266 |
Section 20 825kb | | (b) | Lessing Process for the Separation of Oils and Pitch from Tar | 269 |
| (c) | Hydrogenation of Coal in the Absence of Oil | 271 |
Bibliography | 274 |
Index | 279 |