Abstract: The present invention provides A process for preparing Fischer-Tropsch gasoil fraction, comprising: a) providing a Fischer-Tropsch-derived gasoil feedstock containing one or more contaminants; b) providing the Fischer-Tropsch-derived gasoil feedstock to a pretreatment zone to be pretreated to remove at least part of the one or more contaminants in the Fischer-Tropsch-derived gasoil feedstock; c) retrieving from the pretreatment zone a purified Fischer-Tropsch gasoil, which purified Fischer-Tropsch gasoil is contaminant-depleted with respect to the Fischer-Tropsch-derived gasoil feedstock; and d) providing the purified Fischer-Tropsch gasoil to fractionation zone and fractionating the purified Fischer-Tropsch gasoil into two or more high purity Fischer-Tropsch gasoil fractions. The invention further provides for the use of the purified Fischer-Tropsch gasoil fraction.

Abstract: The present invention provides a Fischer-Tropsch gasoil fraction having: (a) an initial boiling point of at least 220° C.; (b) a final boiling point of at most 360° C.; (c) a kinematic viscosity at 25° C. according to ASTM D445 of from 3.8 to 4.4 cSt; and (d) of a flash point according to ASTM D93 of at least 100° C. In another aspect the present invention provides a composition and the use of a Fischer-Tropsch gasoil fraction according to the invention.

Abstract: The present invention provides a Fischer-Tropsch gasoil fraction having an initial boiling point of at least 175° C. and a final boiling point of at most 285° C. In another aspect the present invention provides a fuel composition and the use of a Fischer-Tropsch gasoil fraction according to the invention.

Abstract: The present invention provides a Fischer-Tropsch gasoil fraction having: (a) an initial boiling point of at least 250° C.; (b) a final boiling point of at most 350° C.; (c) a kinematic viscosity at 25° C. according to ASTM D445 of from 4.0 to 4.6 cSt; and (d) a flash point according to ASTM D93 of at least 117° C. In another aspect the present invention provides a composition and the use of a Fischer-Tropsch gasoil fraction according to the invention.

Abstract: The present invention provides a Fischer-Tropsch gasoil fraction having an initial boiling point of at least 210° C. and a final boiling point of at most 320° C. In another aspect the present invention provides a composition and the use of a Fisc-her-Tropsch gasoil fraction according to the invention.

Abstract: The present invention provides a Fischer-Tropsch gasoil fraction having an initial boiling point of at least 165° C. and a final boiling point of at most 220° C. In another aspect the present invention provides a cleaning composition and the use of a Fischer-Tropsch gasoil fraction according to the invention.

Abstract: The present invention provides a Fischer-Tropsch gasoil fraction having an initial boiling point of at least 160° C. and a final boiling point of at most 215° C. In another aspect the present invention provides a composition and the use of a Fischer-Tropsch gasoil fraction according to the invention.

Abstract: The present invention provides a Fischer-Tropsch gasoil fraction having an initial boiling point of at least 200° C. and a final boiling point of at most 300° C. In another aspect the present invention provides a composition and the use of a Fisc- her-Tropsch gasoil fraction according to the invention.

Abstract: The present invention provides a process for preparing a high purity Fischer-Tropsch gasoil fraction, comprising: a) providing a Fischer-Tropsch-derived gasoil feedstock comprising one or more contaminants; b) providing the Fischer-Tropsch-derived gasoil feedstock to a fractionation zone and fractionating the Fischer-Tropsch-derived gasoil feedstock into two or more Fischer-Tropsch gasoil fractions having a different boiling point range, wherein at least one Fischer-Tropsch gasoil fraction is a contaminant-enriched Fischer-Tropsch gasoil fraction, which is enriched in one or more contaminants with respect to the feedstock; c) providing the contaminant-enriched Fischer-Tropsch gasoil fraction to an absorption zone comprising at least one absorbent material and contacting the contaminant-enriched Fischer-Tropsch gasoil fraction with the absorbent material to absorb at least part of contaminant; and d) retrieving from the absorption zone a purified Fischer-Tropsch gasoil fraction, which is contaminant-depleted.

Abstract: The present invention provides a process for preparing a high purity Fischer-Tropsch gasoil fraction, comprising : a) providing a Fischer-Tropsch-derived gasoil feedstock comprising one or more contaminants; b) providing the Fischer-Tropsch-derived gasoil feedstock to a fractionation zone and fractionating the Fischer-Tropsch-derived gasoil feedstock into two or more Fischer-Tropsch gasoil fractions having a different boiling point range, wherein at least one Fischer-Tropsch gasoil fraction is a contaminant-containing Fischer- Tropsch gasoil fraction; c) providing the contaminant-containing Fischer-Tropsch gasoil fraction to an absorption zone comprising at least one absorbent material and contacting the contaminant-containing Fischer-Tropsch gasoil fraction with the absorbent material to absorb at least part of contaminant; and d) retrieving from the absorption zone a purified Fischer-Tropsch gasoil fraction, which is contaminant-depleted.

Abstract: The present invention provides a process for preparing a high purity Fischer-Tropsch gasoil fraction, comprising: a)fractionating a Fischer-Tropsch-derived gasoil feedstock into two or more Fischer-Tropsch gasoil fractions having a different boiling point range, wherein at least one Fischer-Tropsch gasoil fraction is a contaminant-enriched Fischer-Tropsch gasoil fraction, which is enriched in one or more contaminants with respect to the feedstock; b) providing the contaminant-enriched Fischer-Tropsch gasoil fraction to an absorption zone comprising at least one absorbent material and contacting the contaminant-enriched Fischer-Tropsch gasoil fraction with the absorbent material to absorb at least part of contaminant; and c) retrieving from the absorption zone a purified Fischer-Tropsch gasoil fraction as high purity Fischer-Tropsch gasoil fraction, which purified Fischer-Tropsch gasoil fraction is contaminant-depleted with respect to the Fischer-Tropsch-derived gasoil feedstock, and wherein at least part of t

Abstract: The present invention provides a Fischer-Tropsch derived gas oil having an initial boiling point of at least 175° C. and a final boiling point of at most 360° C. In another aspect the present invention provides a functional fluid formulation comprising a Fischer-Tropsch derived gas oil having an initial boiling point of at least 175° C. and a final boiling point of at most 360° C.

Abstract: The present invention provides a Fischer-Tropsch derived gas oil fraction having an initial boiling point of at least 300° C. and a final boiling point of at most 365° C. In another aspect the present invention provides a functional fluid formulation comprising a Fischer-Tropsch derived gas oil fraction having an initial boiling point of at least 300° C. and a final boiling point of at most 365° C.

Abstract: The present invention provides a Fischer-Tropsch derived gas oil fraction having an initial boiling point of at least 185° C. and a final boiling point of at most 225° C. In another aspect the present invention provides a functional fluid formulation comprising a Fischer-Tropsch derived gas oil fraction having an initial boiling point of at least 185° C. and a final boiling point of at most 225° C.

Abstract: The present invention provides a Fischer-Tropsch derived gas oil having an initial boiling point of at least 165° C. and a final boiling point of at most 360° C. In another aspect the present invention provides a functional fluid formulation comprising a Fischer-Tropsch derived gas oil having an initial boiling point of at least 165° C. and a final boiling point of at most 360° C.

Abstract: The present invention provides a Fischer-Tropsch derived gas oil fraction having an initial boiling point of at least 165° C. and a final boiling point of at most 200° C. In another aspect the present invention provides a functional fluid formulation comprising a Fischer-Tropsch derived gas oil fraction having an initial boiling point of at least 165° C. and a final boiling point of at most 200° C.

Abstract: The present invention provides a Fischer-Tropsch derived gas oil having an initial boiling point of at least 165° C. and a final boiling point of at most 360° C. In another aspect the present invention provides a functional fluid formulation comprising a Fischer-Tropsch derived gas oil having an initial boiling point of at least 165° C. and a final boiling point of at most 360° C.

Abstract: The present invention provides a Fischer-Tropsch derived gas oil fraction having an initial boiling point of at least 245° C. and a final boiling point of at most 275° C. In another aspect the present invention provides a functional fluid formulation comprising a Fischer-Tropsch derived gas oil fraction having an initial boiling point of at least 245° C. and a final boiling point of at most 275° C.

Abstract: The present invention provides a Fischer-Tropsch derived gas oil fraction having an initial boiling point of at least 270° C. and a final boiling point of at most 305° C. In another aspect the present invention provides a functional fluid formulation comprising a Fischer-Tropsch derived gas oil fraction having an initial boiling point of at least 270° C. and a final boiling point of at most 305° C.

Abstract: The present invention provides a Fischer-Tropsch derived gas oil fraction having an initial boiling point of at least 215° C. and a final boiling point of at most 250° C. In another aspect the present invention provides a functional fluid formulation comprising a Fischer-Tropsch derived gas oil fraction having an initial boiling point of at least 215° C. and a final boiling point of at most 250° C.