Apparatus and method for superheated vapor contacting and vaporization of feedstocks containing high boiling point and unvaporizable foulants in an olefins furnace
View Patent ↗A contactor/separator is formed from a vessel; an inlet for receiving a vapor/liquid mixture; an inlet for receiving a superheated vapor; a hub located within the vessel, the hub including a plurality of vanes for imparting a centrifugal motion to the vapor/liquid mixture or the superheated vapor; an outlet in a bottom of the vessel for removing liquid; and an outlet for removing vapor from the vessel. A method is also provided for heating and separating liquid and vapor from a hydrocarbon feedstock comprising introducing a hydrocarbon feedstock into a contactor/separator: introducing a superheated vapor into the contactor/separator such that it contacts and vaporizes a portion of the feedstock within the contactor/separator; separating unvaporized feedstock from vaporized feedstock in the contactor/separator; removing the vaporized feedstock and the superheated vapor through a first outlet; and removing the unvaporized feedstock through a second outlet.
1. A method of heating and separating liquid and vapor from a hydrocarbon feedstock comprising:
introducing a hydrocarbon feedstock into a contactor/separator through a first inlet:
introducing a superheated vapor into the contactor/separator such that it contacts and vaporizes a portion of the feedstock within the contactor/separator through a second inlet;
separating unvaporized feedstock from vaporized feedstock in the contactor/separator using centrifugal forces in a separation zone;
removing the vaporized feedstock and the superheated vapor through a first outlet positioned below the separation zone; and
removing the unvaporized feedstock through a second outlet.
2. A method of heating and separating liquid and vapor from a hydrocarbon feedstock as defined in claim 1 wherein the superheated vapor comprises steam.
3. A method of heating and separating liquid and vapor from a hydrocarbon feedstock as defined in claim 1 wherein the superheated vapor comprises a steam and hydrocarbon mixture.
4. A method of heating and separating liquid and vapor from a hydrocarbon feedstock as defined in claim 1 wherein the feedstock is heated and partially vaporized before being introduced into the contactor/separator.
5. A method of heating and separating liquid and vapor from a hydrocarbon feedstock as defined in claim 1 wherein the hydrocarbon feedstock is vaporized at a temperature greater than 750° F. (400° C.).
6. A method of heating and separating liquid and vapor from a hydrocarbon feedstock as defined in claim 1 wherein the hydrocarbon feedstock is vaporized at a temperature between 760 and 950° F. (404° C. and 520° C.).
7. A method of heating and separating liquid and vapor from a hydrocarbon feedstock as defined in claim 1 wherein the hydrocarbon feedstock comprises crude oil, crude oil fractions, heavy hydrocarbon feeds, gas to liquid process heavy ends, Shell Middle Distillate Synthesis heavy ends, deasphalted oil, oils derived from tar sands, oil shale and coal, Fischer Tropsch products, or hydrocrackate.
8. A method of heating and separating liquid and vapor from a hydrocarbon feedstock as defined in claim 1 wherein at least 2 vol. % of the feedstock remains as liquid.
9. A method of heating and separating liquid and vapor from a hydrocarbon feedstock as defined in claim 1 wherein sufficient feedstock remains as liquid to wet the interior surfaces of the contactor/separator to prevent or reduce coking.
10. A method of heating and separating liquid and vapor from a hydrocarbon feedstock as defined in claim 1 wherein the separated vaporized feedstock and superheated vapor are fed to a pyrolysis furnace.
11. A method of heating and separating liquid and vapor from a hydrocarbon feedstock as defined in claim 1 wherein the temperature in the contactor/separator is controlled by adjusting the temperature of the superheated vapor.
12. A method of heating and separating liquid and vapor from a hydrocarbon feedstock as defined in claim 1 the temperature in the contactor/separator is controlled by adjusting the amount of superheated vapor fed to the contactor/separator.
13. A method of heating and separating liquid and vapor from a hydrocarbon feedstock as defined in claim 1 wherein the temperature in the contactor/separator is controlled by adjusting the temperature of the hydrocarbon feed fed to the contactor/separator.
14. A method of heating a feed to a pyrolysis furnace comprising:
preheating a hydrocarbon feed in a convection section of a pyrolysis furnace to form a pre-heated feed;
heating the pre-heated feed with a superheated vapor in a contactor/separator and separating the feed into a vapor fraction and a liquid fraction using centrifugal forces in a separation zone;
removing the vapor fraction through an outlet positioned below the separation zone; and
further heating the vapor fraction in the convection section of the furnace.
15. The method of claim 14 wherein the hydrocarbon feed includes pitch.
16. The method of claim 15 further comprising removing the pitch from the contactor/separator.
17. A method of cracking a hydrocarbon feed containing pitch comprising:
preheating a hydrocarbon feed containing pitch in a convection section of a furnace;
heating the pre-heated feed with a superheated vapor in a contactor/separator and separating the feed into a vapor fraction and a liquid fraction using centrifugal forces in a separation zone;
removing the vapor fraction through an outlet positioned below the separation zone;
removing the liquid fraction from the contactor/separator; and
cracking the vapor fraction in a radiant section of the furnace.