초록 ▼

Disclosed are processes for producing deasphalted bitumen and heavy bitumen compositions from oil sands and processes for upgrading the bitumen compositions. The processes for producing the deasphalted bitumen and heavy bitumen compositions involve a Phase I and/or Phase II extraction solvent. Accor

Disclosed are processes for producing deasphalted bitumen and heavy bitumen compositions from oil sands and processes for upgrading the bitumen compositions. The processes for producing the deasphalted bitumen and heavy bitumen compositions involve a Phase I and/or Phase II extraction solvent. According to the Phase I process, a high quality oil sands-derived, deasphalted bitumen can be produced using a Phase I type solvent. According to the Phase II process, a substantial amount of the heavy bitumen on the oil sand can be extracted using a Phase II type solvent, while producing a relatively a tailings by-product that is non-harmful to the environment. The heavy bitumen from the Phase II type extraction process can be hydroprocessed for ready conversion into relatively high volumes of high quality transportation fuels.

대표청구항 ▼

1. A process for hydroprocessing a heavy bitumen composition derived from total oil sands bitumen, comprising: a) providing the heavy bitumen composition as a feedstock for the hydroprocessing, wherein the heavy bitumen composition is provided by treating oil sands containing the total oil sands bit

1. A process for hydroprocessing a heavy bitumen composition derived from total oil sands bitumen, comprising: a) providing the heavy bitumen composition as a feedstock for the hydroprocessing, wherein the heavy bitumen composition is provided by treating oil sands containing the total oil sands bitumen with a hydrocarbon solvent comprised of an admixture of: 1) a light solvent component comprised of from 95 wt % to 5 wt % of propane and 2) and from 5 wt % to 95 wt % of a deasphalted bitumen fraction of the total oil sands bitumen, having an asphaltene content of not greater than 10 wt % measured according to ATSM D6560, and has an asphaltene concentration by weight, measured according to ASTM D6560, greater than that of the total oil sands bitumen; andb) hydroprocessing the heavy bitumen composition by contacting the heavy bitumen composition with a hydroprocessing catalyst in the presence of hydrogen, wherein the hydroprocessing catalyst comprises at least one Group 6metal and at least one Group 8-10 metal. 2. The process of claim 1, wherein the heavy bitumen composition has an asphaltene content of greater than 10 wt %, measured according to ASTM D6560, and the hydrocarbon solvent has a Hansen hydrogen bonding blend parameter of at least 0.2 MPa1/2 and a Hansen polarity blend parameter of at least 0.2 MPa1/2. 3. The process of claim 1, wherein the heavy bitumen composition has an asphaltene content of greater than 10 wt %, measured according to ASTM D6560. 4. The process of claim 1, wherein the hydroprocessing catalyst is comprised of at least one Group 6 metal selected from the group consisting of Mo and W and at least one Group 8-10 metal selected from the group consisting of Co and Ni. 5. The process of claim 4, wherein the hydroprocessing catalyst has a pore diameter of from 30 Å to 1000 Å. 6. The process of claim 1, wherein the hydrocarbon solvent has a Hansen hydrogen bonding blend parameter of at least 0.2MPa1/2. 7. The process of claim 6, wherein the hydrocarbon solvent has a Hansen polarity blend parameter of at least 0.2 MPa1/2. 8. The process of claim 7, wherein the hydrocarbon solvent has a Hansen dispersion blend parameter of at least 14 MPa1/2. 9. A process for hydroprocessing a heavy bitumen fraction of total oil sands bitumen, comprising the steps of: a) treating oil sands comprised of the total oil sands bitumen with a hydrocarbon solvent comprised of an admixture of: 1) a light solvent component comprised of from 95 wt % to 5 wt % of propane and 2) and from 5 wt % to 95 wt % of a deasphalted bitumen fraction of the total oil sands bitumen, having an asphaltene content of not greater than 10 wt % measured according to ATSM D6560, to extract a heavy bitumen composition from the total oil sands bitumen present on the oil sands, wherein the heavy bitumen composition has an asphaltene concentration by weight, measured according to ASTM D6560, greater than that of the total oil sands bitumen; andb) hydroprocessing the heavy bitumen composition by contacting the heavy bitumen composition with a hydroprocessing catalyst in the presence of hydrogen, wherein the hydroprocessing catalyst comprises at least one Group 6 metal and at least one Group 8-10 metal. 10. The process of claim 9, wherein the heavy bitumen composition has an asphaltene content of greater than 10 wt %, measured according to ASTM D6560. 11. The process of claim 10, wherein the hydrocarbon solvent has a Hansen hydrogen bonding blend parameter of at least 0.2 MPa1/2. 12. The process of claim 11, wherein the hydrocarbon solvent has a Hansen polarity blend parameter of at least 0.2 MPa1/2. 13. The process of claim 12, wherein the hydrocarbon solvent has a Hansen dispersion blend parameter of at least 14 MPa1/2. 14. The process of claim 9, wherein the heavy bitumen fraction has an asphaltene content of greater than 10 wt %, measured according to ASTM D6560, and the hydrocarbon solvent is has a Hansen hydrogen bonding blend parameter of at least 0.2 MPa1/2 and a Hansen polarity blend parameter of at least 0.2 MPa1/2. 15. The process of claim 9, wherein the hydroprocessing catalyst is comprised of at least one Group 6 metal selected from the group consisting of Mo and W and at least one Group 8-10 metal selected from the group consisting of Co and Ni. 16. The process of claim 9, wherein the hydroprocessing catalyst has a pore diameter of from 30 Å to 1000 Å.