发明名称 Verfahren zum selektiven Kracken von n-Paraffinkohlenwasserstoffen
摘要 Hydrocarbons are cracked at elevated temperature and pressure in the presence of hydrogen with a catalyst comprising a crystalline synthetic mondenite having pore openings at least 5</>rA in diameter, which has been decationized by direct treatment with mineral acid to a metal cation content not exceeding 2% weight, and a hydrogenating component selected from metals, on oxides thereof, of Group VI on VIII. Preferably the feedstock is a petroleum fraction containing over 50% volume of material boiling above 250 DEG C., e.g. a wax distillate fraction boiling between 370 DEG and 600 DEG C. Suitable hydrocracking conditions are: temp. 450-950 DEG F., pressure 250-3000 p.s.i.g., space velocity 0.2-20 v/v/hour, gas rate 1000-20,000 SCF/B.ALSO:A hydrocarbon conversion catalyst comprises a synthetic crystalline monderite having pore diameters of at least 5 which has been decationised by direct treatment with mineral acid to a metal cation content of up to 2% wt., and a Group VI or VIII metal or an oxide thereof. Specified Group VI and VIII components are Mo, W, Ni, Co, Fe, Pt and Pd.
申请公布号 DE1545257(A1) 申请公布日期 1969.10.02
申请号 DE1966B090391 申请日期 1966.12.20
申请人 THE BRITISH PETROLEUM COMPANY LTD. 发明人 ANTHONY LAWRENCE,PAUL;WILLIAM AITKEN,ROBERT;NEIL BENNET,ROBERT
分类号 B01J29/18;B01J29/22;B01J29/26;C07C4/06;C07C5/02;C07C5/22;C07C5/27;C07C6/00;C07C6/12;C10G45/64;C10G47/16;C10G47/20 主分类号 B01J29/18
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