Wax flow viscosity for fuels
Marine fuel compositions that are low sulfur and have improved wax flow viscosity are disclosed. An example marine fuel composition may have the following enumerated properties: a sulfur content of about 0.50% or less by weight of the marine fuel composition; a density at 15° C. of about 0.86 g/cm 3 to about 1.01 g/cm 3 ; a kinematic viscosity at 50° C. of about 1 centistoke to about 700 centistokes; and a ratio of kinematic viscosity to wax flow viscosity of greater than 1, wherein the wax flow viscosity is determined using a minimum operating viscosity of about 8 centistokes at 50° C.
1. A marine fuel composition having low sulfur content, the marine fuel composition having the following enumerated properties:
a sulfur content of about 0.50% or less by weight of the marine fuel composition;
a density at 15° C. of about 0.86 g/cm 3 to about 1.01 g/cm 3 ;
a kinematic viscosity at 50° C. of about 10 centistokes to about 80 centistokes;
a wax endpoint temperature of about 35° C. to about 130° C., and
wherein the marine fuel composition comprises a heavy gas oil and a lighter gas oil, wherein at least 50 vol. % of the heavy gas oil boils at about 500° C. to about 750° C., and wherein at least 50 vol. % of the lighter gas oil boils at about 200° C. to about 550° C.
2. The marine fuel composition of claim 1 , wherein the sulfur content is about 0.40 wt. % to about 0.49 wt. %.
3. The marine fuel composition of claim 1 , wherein the density is about 0.86 g/cm 3 to about 0.95 g/cm 3 .
4. The marine fuel composition of claim 1 , wherein the heavy gas oil has a sulfur content of about 0.50 wt. % to about 3 wt. %, and wherein the lighter gas oil has a sulfur content of about 0.0001 wt. % to about 0.05 wt. %.
5. The marine fuel composition of claim 1 , wherein the heavy gas oil has a kinematic viscosity at 50° C. of about 30 centistokes or greater, and wherein the lighter gas oil has a kinematic viscosity at 50° C. of about 1 centistoke to about 30 centistokes.
6. The marine fuel composition of claim 1 , wherein the heavy gas oil is present in an amount of about 1 vol. % to about 60 vol. %, and wherein the lighter gas oil is present in an amount of about 40 vol. % to about 99 vol. %.
7. The marine fuel composition of claim 1 , wherein the heavy gas oil comprises a residual hydrocarbon fraction.
8. The marine fuel composition of claim 1 , wherein the marine fuel composition comprises:
a heavy gas oil having a sulfur content of about 0.50 wt. % to about 3 wt. % and a kinematic viscosity at 50° C. of about 200 centistokes or greater, wherein at least 50 vol. % of the heavy gas oil boils at about 500° C. to about 700° C.; and
a lighter gas oil having a sulfur content of about 0.0001 wt. % to about 0.05 wt. % and a kinematic viscosity at 50° C. of about 1 centistoke to about 30 centistokes, wherein at least 50 vol. % of the lighter gas oil boils at about 300° C. to about 450° C.
9. The marine fuel composition of claim 1 , wherein the marine fuel composition is a distillate marine fuel.
10. The marine fuel composition of claim 1 , wherein the marine fuel composition is a residual marine fuel.
11. A method of blending marine fuel compositions, comprising:
blending two or more hydrocarbon components to prepare a liquid fuel, wherein the liquid fuel has the following enumerated properties:
a sulfur content of about 0.50% or less by weight of the marine fuel composition;
a density at 15° C. of about 0.86 g/cm 3 to about 1.01 g/cm 3 ;
a kinematic viscosity at 50° C. of about 10 centistokes to about 80 centistokes;
a wax endpoint temperature of about 35° C. to about 130° C., and
wherein the two or more hydrocarbon components comprise a heavy gas oil and a lighter gas oil, wherein at least 50 wt. % of the heavy gas oil boils at about 500° C. to about 750° C., and wherein at least 50 wt. % of the lighter gas oil boils at about 200° C. to about 550° C.
12. The marine fuel composition of claim 11 , wherein the heavy gas oil has a sulfur content of about 0.50 wt. % to about 3 wt. %, wherein the lighter gas oil has a sulfur content of about 0.0001 wt. % to about 0.05 wt. %, wherein the heavy gas oil as a kinematic viscosity at 50° C. of about 30 centistokes or greater, wherein the lighter gas oil has a kinematic viscosity at 50° C. of about 1 centistokes to about 30 centistokes, wherein the heavy gas oil is present in an amount of about 1 vol. % to about 60 vol. %, and wherein the lighter gas oil is present in an amount of about 40 vol. % to about 99 vol. %.