Method of operating crude treatment system
View Patent ↗Crude containing a comparatively large content of nickel, vanadium, or carbon residue is treated so as to supply a raw material to a downstream catalytic cracking process. A primary distillation tower fractionates first crude into a residue fraction partly used as raw oil of a catalytic cracking process and other fractions. A secondary distillation tower fractionates second crude containing a larger content of a catalytic poison with respect to catalysts used in the catalytic cracking process than the first crude into a light fraction included in a distillation temperature range of the other fractions and a heavy fraction as a rest thereof. A light fraction supply line supplies the light fraction to the primary distillation tower so as to be treated in the primary distillation tower.
1. A method for operating a crude treatment system comprising:
supplying first crude from a supply line to a primary distillation tower;
fractionating the first crude by the primary distillation tower into a residue fraction and other fractions, the residue fraction being partly or entirely used as raw oil of a catalytic cracking process;
supplying second crude containing a larger content of a catalytic poison with respect to catalysts used in the catalytic cracking process than the first crude from a second crude supply line to a secondary distillation tower;
fractionating the second crude by the secondary distillation tower into a light fraction and a heavy fraction as a rest thereof, the light fraction having a distillation temperature range within a distillation temperature range of the other fractions fractionated in the primary distillation tower;
supplying the light fraction from a light fraction supply line to the primary distillation tower so as to be treated; and
wherein the second crude includes crude selected from a crude group consisting of Mayan crude, Orinoco tar, and oil sand/bitumen.
2. The method of operating the crude treatment system according to claim 1 , further comprising:
supplying the heavy fraction from the secondary distillation tower via a heavy fraction supply line to the vacuum distillation tower so as to be treated; and
distilling the heavy fraction in a vacuum condition by a vacuum distillation tower so as to obtain a vacuum gas oil fraction used as raw oil of the catalytic cracking process and other vacuum residue fractions.
3. The method of operating he crude treatment system according to claim 2 , further comprising: supplying the residue fraction from the primary distillation tower to the vacuum distillation tower via a residue fraction supply line.
4. The method of operating the crude treatment system according to claim 2 , further comprising mixing the residue fraction fractionated from the primary distillation tower with the vacuum gas oil fraction fractionated from the vacuum distillation tower so as to be used as raw oil of the catalytic cracking process.
5. The method of operating the crude treatment system according to claim 1 , wherein the catalytic poison is selected from a catalytic poison group consisted of nickel, vanadium, and carbon residue.
6. A method for operating a crude treatment system comprising:
supplying first crude from a supply line to a primary distillation tower;
fractionating the first crude by the primary distillation tower into a residue fraction and other fractions, the residue fraction being partly or entirely used as raw oil of a catalytic cracking process;
supplying second crude containing a larger content of a catalytic poison with respect to catalysts used in the catalytic cracking process than the first crude from a second crude supply line to a secondary distillation tower;
fractionating the second crude by the secondary distillation tower into a light fraction and a heavy fraction as a rest thereof, the light fraction having a content of the poison equal to or less than a predetermined value;
supplying the light fraction from a light fraction supply line to the primary distillation tower so as to be treated; and
wherein the second crude includes crude selected from a crude group consisting of Mayan crude, Orinoco tar, and oil sand/bitumen.
7. The method of operating the crude treatment system according to claim 6 , further comprising:
supplying the heavy fraction from the secondary distillation tower via a heavy fraction supply line to the vacuum distillation tower so as to be treated; and
distilling the heavy fraction in a vacuum condition by a vacuum distillation tower so as to obtain a vacuum gas oil fraction used as raw oil of the catalytic cracking process and other vacuum residue fractions.
8. The method of operating the crude treatment system according to claim 7 , further comprising: supplying the residue fraction from the primary distillation tower to the vacuum distillation tower via a residue fraction supply line.
9. The method of operating the crude treatment system according to claim 7 , further comprising mixing the residue fraction fractionated from the primary distillation tower with the vacuum gas oil fraction fractionated from the vacuum distillation tower so as to be used as raw oil of the catalytic cracking process.
10. The method of operating the crude treatment system according to claim 6 , wherein the catalytic poison is selected from a catalytic poison group consisting of nickel, vanadium, and carbon residue.