Method for the physical separation of refinery purge streams
The present invention relates to a method for the physical separation of solids and asphaltenes with a conversion degree higher than or equal to 90%, present in refinery purge streams. Said method provides for heating a refinery purge stream to a temperature higher than or equal to 185° C. and not exceeding 220° C. and, subsequently, subjecting said heated purge to sedimentation by progressively lowering the temperature in a controlled manner to a minimum temperature of 100° C., without stirring the purge, so as to form a light phase and a heavy phase defined in relation to the density.
1. A method for the physical separation of solids and asphaltenes present in a refinery purge stream, wherein the asphaltenes have a conversion degree higher than or equal to 90%, the method comprising:
heating the refinery purge stream to a temperature higher than or equal to 185° C. and not exceeding 220° C. to form a heated purge and, subsequently,
subjecting said heated purge to sedimentation by progressively lowering the temperature in a controlled manner to a minimum temperature of 100° C., without stirring the purge, so as to form a light phase and a heavy phase in relation to the density.
2. The method according to claim 1 , wherein the refinery purge stream comes from hydroconversion processes in slurry phase.
3. The method according to claim 1 , wherein the heated purge is cooled to a temperature that varies within the range of 100° C. to 170° C.
4. The method according to claim 3 , wherein the heated purge is cooled to a temperature ranging from 100° C. to 160° C.
5. The method according to claim 1 , wherein the formation of the heavy phase takes from 15 minutes to 2 hours.
6. The method according to claim 5 , wherein the formation of the heavy phase takes from 20 minutes to 1 hour.
7. The method according to claim 1 , wherein the sedimentation takes place at a rate ranging from 85 mm/hour to 150 mm/hour.