Methods and systems for producing reduced resid and bottomless products from heavy hydrocarbon feedstocks

1. A method of producing an upgraded product from a heavy hydrocarbon feedstock, comprising:

a) upgrading a heavy hydrocarbon feedstock by a method comprising:

i) providing a particulate heat carrier into an upflow reactor;

ii) introducing the heavy hydrocarbon feedstock into the upflow reactor at least one location above that of the particulate heat carrier so that a loading ratio of the particulate heat carrier to the heavy hydrocarbon feedstock is from about 10:1 to about 200:1, wherein the upflow reactor is run at a temperature of from about 300° C. to about 700° C., and

iii) allowing the heavy hydrocarbon feedstock to interact with the particulate heat carrier with a residence time of less than about 20 seconds, to produce a product mixture comprising a product stream and the particulate heat carrier;

b) separating the product stream from the particulate heat carrier;

c) obtaining a gaseous product and a liquid product mixture from the product stream, the liquid product mixture comprising a light fraction and a heavy fraction;

d) obtaining an upgraded bottomless product from the liquid product mixture using a vacuum tower; and

e) recycling at least a portion of the heavy fraction of the liquid product mixture from the vacuum tower to the upflow reactor.

2. The method of claim 1 , wherein the recycled heavy fraction is mixed with the particulate heat carrier, wherein the particulate heat carrier is at a temperature at about, or above, that used in the step of upgrading (step a).

3. The method of claim 1 , wherein the method further includes mixing the heavy fraction with the particulate heat carrier, wherein the particulate heat carrier of the recycled pyrolysis run is at a temperature at about, or above, that used in the step of upgrading (step a).

4. The method of claim 1 , wherein the product stream is treated within a hot condenser prior to obtaining the light fraction and the heavy fraction.

5. The method of claim 1 , wherein the heavy hydrocarbon feedstock is either heavy oil or bitumen.

6. The method according to claim 1 , wherein the upflow reactor run at a temperature in the range from about 450° C. to about 600° C.

7. The method of claim 1 , wherein the reactor is run at a temperature in the range from about 480° C. to about 550° C.

8. The method of claim 1 , wherein in the step of introducing (step a)ii)), the loading ratio is from about 20:1 to about 30:1.

9. The method of claim 1 , wherein prior to the step of upgrading, the feedstock is introduced into a fractionation column that separates a volatile component of the feedstock from a liquid component of the feedstock, and the liquid component is subjected to upgrading (step a).

10. The method of claim 1 , wherein prior to the step of upgrading, the feedstock is introduced into a fractionation column that separates a volatile component of the feedstock from a liquid mixture derived from the feedstock, the liquid mixture comprising a light component and a heavy component, wherein the heavy component is subjected to the step of upgrading (step a), and the light component is combined with the light fraction derived from the vacuum tower following the step of obtaining (step c).

11. The method of claim 1 , wherein the bottomless product contains less than 5% of the heavy fraction present in the liquid product mixture.

12. The method of claim 1 , wherein the bottomless product contains less than 1% of the heavy fraction present in the liquid product mixture.