FIELD: methods of thermal pyrolysis of hydrocarbon raw materials in tubular furnaces; chemical and petrochemical industries.
SUBSTANCE: proposed method includes preliminary thermal pyrolysis of liquid hydrocarbon raw material at 820-835°C continued for 48-120 h at contact time of 0.4-0.6 s and mass ratio of water steam=1:0.40-0.65. Subsequent joint thermal pyrolysis of gaseous hydrocarbons and liquid hydrocarbon raw material is performed at content of 5-15 mass-%, temperature of 830-840°C, contact time of 0.4-0.5 s and mass ratio of water steam=1:0.60-0.65. Used as gaseous hydrocarbons is mixture of hydrocarbons C2-C4 of the following composition, mass-%: methane, 0.01-0.20; ethane, 0.85-1.25; propane, 60.00-97.00; sum of C4-1.50-30.00; used as liquid hydrocarbon raw material is directly-distilled gasoline fraction at boiling limits of 28-160°C. Proposed method ensures increased yield of lower olefins C2-C3 due to increased degree of conversion of light hydrocarbon alkanes C2-C4.
EFFECT: enhanced efficiency of thermal pyrolysis process.
2 cl, 1 tbl, 8 ex
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SU1616956A1 |
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METHOD OF OBTAINING LOWER OLEFINS C-C FROM RAW LIGHT HYDROCARBON MATERIAL | 2007 |
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BLOCK OF FURNACES OF HYDROCARBON RAW MATERIAL PYROLYSIS UNIT | 2023 |
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UNSATURATED HYDROCARBONS PRODUCTION PROCESS | 2006 |
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RU2318860C1 |
METHOD OF PRODUCING ETHYLENE FROM HYDROCARBON MATERIAL | 2014 |
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RU2548002C1 |
LOWER OLEFIN PRODUCTION PROCESS | 2002 |
|
RU2206598C1 |
PETROCHEMICAL CLUSTER | 2014 |
|
RU2550690C1 |
Authors
Dates
2005-12-10—Published
2004-08-10—Filed