Residual base oil process
The present invention relates to a Fischer-Tropsch derived residual base oil having a kinematic viscosity at 100° C. according to ASTM D445 in the range of from 15 to 35 mm 2 /s, an average number of carbon atoms per molecule Fischer-Tropsch derived residual base oil according to 13 C-NMR in a range of from 25 to 50.
1. A process for preparing a clear and bright Fischer-Tropsch derived residual base oil at 0° C. having a kinematic viscosity at 100° C. in the range of from 15 to 35 mm 2 /s according to ASTM D445, a cloud point of below 0° C. as measured according to ASTM D2500, and an average number of carbon atoms per molecule of the Fischer-Tropsch derived residual base oil according to 13 C-NMR in a range of from 25 to 50, wherein the process comprises the steps of:
(a) providing a hydrocarbon feed which is derived from a Fischer-Tropsch process;
(b) subjecting the hydrocarbon feed of step (a) to a hydrocracking/hydroisomerisation step to obtain an at least partially isomerised product;
(c) separating at least part of the at least partially isomerised product as obtained in step (b) into one or more lower boiling fractions and a hydrowax residue fraction;
(d) catalytic dewaxing of the hydrowax residue fraction of step (c) to obtain a highly isomerised product;
(e) separating the highly isomerised product of step (d) into one or more light fractions and an isomerised residual fraction;
(f) mixing the isomerised residual fraction of step (e) with a diluent to obtain a diluted isomerised residual fraction;
(g) cooling the diluted isomerised residual fraction of step (f) to a temperature between 0° C. and −60° C.;
(h) subjecting the mixture of step (g) to a centrifuging step at a temperature between 0° C. and −60° C. to isolate the wax from the diluted isomerised residual fraction; and
(i) separating the diluent from the diluted isomerised residual fraction to obtain the clear and bright Fischer-Tropsch derived residual base oil.
2. The process according to claim 1 , wherein the clear and bright Fischer-Tropsch derived residual base oil has an average number of carbon atoms per molecule of the Fischer-Tropsch derived residual base oil according to 13 C-NMR of from 30 to 45 carbon atoms.
3. The process according to claim 1 , wherein the clear and bright Fischer-Tropsch derived residual base oil has an average number of carbon atoms per molecule of the Fischer-Tropsch derived residual base oil according to 13 C-NMR of from 31 to 45 carbon atoms.
4. The process according to claim 1 , wherein the clear and bright Fischer-Tropsch derived residual base oil has an average number of carbons in the non-branched segment according to 13 C-NMR of less than 14 carbon atoms.
5. The process according to claim 1 , wherein the clear and bright Fischer-Tropsch derived residual base oil has an average number of branches normalized for a molecule of 50 carbon atoms in according to 13 C-NMR of at least 3.5.
6. The process according to claim 1 , wherein the clear and bright Fischer-Tropsch derived residual base oil has an average number of branches normalized for a molecule of 50 carbon atoms in according to 13 C-NMR of at least 4.0.
7. The process according to claim 1 , wherein the clear and bright Fischer-Tropsch derived residual base oil has a T10 wt. % recovery point in the range of from 470 to 590° C., a T50 wt. % recovery point in the range of from 550 to 710° C., a T80 wt. % recovery point of at least 630° C. and a T90 wt. % recovery point of at least 700° C. as measured with ASTM D7169.
8. The process according to claim 1 , wherein the clear and bright Fischer-Tropsch derived residual base oil has a pour point of less than −10 as measured according to ASTM D97.
9. The process according to claim 1 , wherein the clear and bright Fischer-Tropsch derived residual base oil has a pour point of less than −20° C. as measured according to ASTM D97.