Method for improving liquid yield during thermal cracking of hydrocarbons
View Patent ↗Metal additives to hydrocarbon feed streams give improved hydrocarbon liquid yield during thermal cracking thereof. Suitable additives include metal overbases and metal dispersions and the metals suitable include, but are not necessarily limited to, magnesium, calcium, aluminum, zinc, silicon, barium, cerium, and strontium overbases and dispersions. Coker feedstocks are a particular hydrocarbon feed stream to which the method can be advantageously applied, but the technique may be used on any hydrocarbon feed that is thermally cracked.
1. A method for improving liquid yield during thermal cracking of a refinery hydrocarbon comprising:
introducing a metal additive and a dispersant to a refinery hydrocarbon feed stream, where the metal additive is selected from the group consisting of a metal overbase and a metal dispersion, where the metal in the metal additive is selected from the group consisting of aluminum alone, and aluminum and magnesium together;
heating the refinery hydrocarbon feed stream to a thermal cracking temperature; and
recovering a hydrocarbon liquid product.
2. The method of claim 1 where the metal additive contains at least about 1 wt % metal.
3. The method of claim 1 where the thermal cracking temperature is between about 850° F. (454° F.) and about 1300° F. (704° C.).
4. The method of claim 1 where the amount of hydrocarbon liquid product is increased as compared with an identical method absent the overbase additive.
5. The method of claim 1 where the refinery hydrocarbon feed stream is a coker feed stream.
6. A method for improving liquid yield during thermal cracking of a refinery hydrocarbon comprising:
introducing a metal additive and a dispersant to a refinery hydrocarbon feed stream, where the metal additive is selected from the group consisting of a metal overbase and a metal dispersion, where the metal in the metal additive is selected from the group consisting of aluminum alone, and aluminum and magnesium together;
heating the refinery hydrocarbon feed stream to a thermal cracking temperature; and
recovering a hydrocarbon liquid product;
where the amount of hydrocarbon liquid product is increased as compared with an identical method absent the overbase additive.
7. The method of claim 6 where the thermal cracking temperature is between about 850° F. (454° C.) and about 1300° F. (704° C.).
8. A refinery process comprising a coking operation further comprising:
introducing a metal additive and a dispersant to a coker feed stream, where the metal additive is selected from the group consisting of a metal overbase and a metal dispersion, where the metal in the metal additive is selected from the group consisting of aluminum alone, and aluminum and magnesium together;
heating the coker feed stream to a thermal cracking temperature; and
recovering a hydrocarbon liquid product.
9. The refinery process of claim 8 where the overbase additive contains at least about 1 wt % metal.
10. The refinery process of claim 8 where the thermal cracking temperature is between about 850° F. (454° C.) and about 1300° F. (704° C.).
11. The refinery process of claim 8 where the amount of hydrocarbon liquid product is increased as compared with an identical method absent the overbase additive.