Method of manufacturing diesel fuel base stock and diesel fuel base stock thereof
Disclosed is a method of manufacturing a diesel fuel base stock improved in low-temperature flowability, including: fractionating in a first fractionator a synthetic oil obtained by Fisher-Tropsch synthesis into at least two fractions of a first middle fraction containing a component having a boiling range corresponding to diesel fuel oil, and a wax fraction containing a wax component heavier than the first middle fraction; hydroisomerizing the first middle fraction by bringing the first middle fraction into contact with a hydroisomerizing catalyst to produce a hydroisomerized middle fraction; hydrocracking the wax fraction by bringing the wax fraction into contact with a hydrocracking catalyst to produce a wax-decomposition component; and fractionating in a second fractionator a mixture of the produced hydroisomerized middle fraction and the produced wax-decomposition component, wherein rectification conditions in the first fractionator and/or rectification conditions in the second fractionator are adjusted to selectively reduce an n-paraffin having 19 or more carbon atoms in a heavy component contained in the diesel fuel base stock. Furthermore, disclosed is a diesel fuel base stock obtained by the manufacturing method.
1. A method of manufacturing a diesel fuel base stock improved in low-temperature flowability, comprising:
(i) fractionating in a first fractionator a synthetic oil obtained by Fisher-Tropsch synthesis into at least two fractions of
a first middle fraction containing a component having a boiling range corresponding to diesel fuel oil and containing a light wax component of n-paraffins having 20 to 25 carbon atoms, and
a wax fraction containing a wax component heavier than the first middle fraction;
(ii) hydroisomerizing the first middle fraction by bringing the first middle fraction into contact with a hydroisomerizing catalyst to produce a hydroisomerized middle fraction;
(iii) hydrocracking the wax fraction by bringing the wax fraction into contact with a hydrocracking catalyst to produce a wax-decomposition component; and
(iv) fractionating in a second fractionator a mixture of the produced hydroisomerized middle fraction and the produced wax-decomposition component,
wherein rectification conditions in the first fractionator and/or rectification conditions in the second fractionator are adjusted to reduce the content of n-paraffin having 19 or more carbon atoms in a heavy component contained in the diesel fuel base stock, and
wherein the fractionation is conducted where the 90% by volume distillation temperature of the first middle fraction, which is a feedstock for the hydroisomerization, is higher than the 90% by volume distillation temperature of the diesel fuel base stock by 20° C. or more as one of the rectification conditions in the first fractionator.
2. The method of manufacturing a diesel fuel base stock according to claim 1 , wherein: the 90% by volume distillation temperature of the first middle fraction, which is a feedstock for the hydroisomerization, is 360° C. or higher, and the 90% by volume distillation temperature of the diesel fuel base stock is 340° C. or less.
3. The method of manufacturing a diesel fuel base stock according to claim 1 , wherein:
when bringing the first middle fraction into contact with the hydroisomerizing catalyst, the reaction temperature is 180° C. to 400° C., the hydrogen partial pressure is 0.5 MPa to 12 MPa, and the liquid hourly space velocity is 0.1 h −1 to 10.0 h −1 ; and,
when bringing the wax fraction into contact with the hydrocracking catalyst, the reaction temperature is 180° C. to 400° C., the hydrogen partial pressure is 0.5 MPa to 12 MPa, and the liquid hourly space velocity is 0.1 h −1 to 10.0 h −1 .