Invention Grant
- Patent Title: Optimized method for producing middle distillates from a feedstock originating from the Fischer-Tropsch process containing a limited quantity of oxygenated compounds
- Patent Title (中): 从含有有限量的含氧化合物的费 - 托法的原料生产中间馏分的优化方法
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Application No.: US13860850Application Date: 2013-04-11
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Publication No.: US09353320B2Publication Date: 2016-05-31
- Inventor: Aline Grezaud , Jean Philippe Heraud , Hugues Dulot , Christophe Bouchy , Vincenzo Calemma
- Applicant: ENI S.p.A. , IFP Energies nouvelles
- Applicant Address: FR Rueil-Malmaison IT Rome
- Assignee: IFP Energies Nouvelles,ENI S.p.A.
- Current Assignee: IFP Energies Nouvelles,ENI S.p.A.
- Current Assignee Address: FR Rueil-Malmaison IT Rome
- Agency: Millen White Zelano and Branigan, PC
- Agent John Sopp; Anthony Zelano
- Priority: FR1201075 20120412
- Main IPC: C10G65/12
- IPC: C10G65/12 ; C07C1/04 ; C07C1/12 ; B01J21/12 ; B01J23/42 ; B01J23/44 ; B01J23/75 ; B01J23/755 ; B01J23/882 ; B01J23/883 ; B01J23/888 ; B01J35/00 ; B01J35/10 ; B01J37/00 ; B01J37/02 ; C10G65/02 ; C07C27/06 ; C07C27/08 ; C10G45/00 ; C10G45/02

Abstract:
A method for producing middle distillates from a feedstock produced by Fischer-Tropsch synthesis and containing oxygenated compounds, including: a) a step of bringing the feedstock into contact with a hydrotreating catalyst allowing the methanation of the CO and CO2 contained in the feedstock or originating from the decomposition of the oxygenated compounds present in the feedstock, b) a step of hydroisomerization/hydrocracking of at least a part of the liquid and gaseous effluent originating from step a), in the presence of a hydroisomerization/hydrocracking catalyst, c) a step of gas/liquid separation of the effluent originating from step b) into a gaseous fraction comprising predominantly hydrogen and a hydroisomerized/hydrocracked liquid fraction, d) a step of fractionation of the liquid fraction separated in step c) to obtain at least one fraction of middle distillate, in which the hydrogen in step a) is obtained from the gaseous fraction separated in step c).
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