Recycle of olefinic naphthas by removing aromatics

1. A process for producing one or more olefins, comprising:

cracking a feed comprising 90% by weight or more C4 and higher hydrocarbons at conditions sufficient to provide an olefinic mixture comprising 90% by weight or more C1 to C3 hydrocarbons and an aromatic mixture comprising 90% by weight or more C4 and higher hydrocarbons and one or more aromatics;

contacting a first portion of the aromatic mixture with one or more solvents to provide an aromatic-rich mixture and an aromatic-lean mixture;

recycling at least a portion of the aromatic-lean mixture to the feed prior to cracking; and

separating a second portion of the aromatic mixture to provide a low aromatics mixture and gasoline.

2. The process of claim 1 , wherein the aromatic-rich mixture comprises 50% by weight or more of the one or more aromatics from the aromatic mixture.

3. The process of claim 1 , wherein the aromatic-rich mixture comprises 75% by weight or more of the one or more aromatics from the aromatic mixture.

4. The process of claim 1 , wherein the aromatic-rich mixture comprises 90% by weight or more of the one or more aromatics from the aromatic mixture.

5. The process of claim 1 , wherein the aromatic-rich mixture comprises 95% by weight or more of the one or more aromatics from the aromatic mixture.

6. The process of claim 1 , wherein the aromatic-lean mixture comprises 10% by weight or less aromatics.

7. The process of claim 1 , wherein the aromatic-lean mixture comprises 5% by weight or less aromatics.

8. The process of claim 1 , wherein the solvent comprises di-methyl sulfoxide, n-methyl pyrrolidone, alkyl carbonates, derivatives thereof, or mixtures thereof.

9. The process of claim 1 , wherein the feed comprises one or more untreated hydrocarbons, unrefined hydrocarbons, treated hydrocarbons, refined hydrocarbons, derivatives thereof, or mixtures thereof.

10. The process of claim 1 , further comprising saturating the recycled aromatic-lean mixture with hydrogen prior to mixing with the feed.

11. A process for producing one or more olefins, comprising:

cracking a feed comprising 90% by weight or more C4 and higher hydrocarbons into one or more cracked hydrocarbons comprising one or more linear olefins and aromatics;

selectively separating the cracked hydrocarbons to provide an olefinic mixture comprising 20% by weight or more olefins and an aromatic mixture comprising 80% by weight or more C4 and higher hydrocarbons and one or more aromatics;

contacting a first portion of the aromatic mixture with one or more solvents to selectively separate at least a portion of the one or more aromatics from the aromatic mixture into the one or more solvents providing an aromatic-lean mixture comprising 30% by weight or more olefins and 10% by weight or less aromatic hydrocarbons;

selectively separating at least a portion of the one or more aromatics from the solvent;

recycling at least a portion of the aromatic-lean mixture to the feed; and

separating a second portion of the aromatic mixture to provide a low aromatics mixture and gasoline.

12. The process of claim 11 , wherein the solvent comprises di-methyl sulfoxide, n-methylpyrrolidone, alkyl carbonates, derivatives thereof, or mixtures thereof.

13. The process of claim 11 , wherein separating the one or more aromatics from the solvent comprises extraction, distillation, gravity separation, centrifugation, or any combination thereof.

14. The process of claim 11 , wherein selectively separating the cracked hydrocarbons comprises:

fractionating the cracked hydrocarbons to provide a first mixture comprising heavy naphtha, light cycle oil, slurry oil, derivatives thereof, or mixtures thereof and a second mixture comprising two or more C2-C10 olefins;

treating the second mixture to remove oxygenates, acid gases, water, or any combination thereof to provide a treated mixture comprising two or more C2-C10 olefins; and

selectively separating the treated mixture to provide the olefinic mixture and the aromatic mixture.

15. The process of claim 14 , further comprising:

selectively separating the olefinic mixture to provide a first fraction comprising 30% by weight or more methane and a second fraction comprising 30% by weight or more C2 and C3 hydrocarbons; and

recycling at least a portion of the first fraction to the feed.

16. The process of claim 11 , further comprising:

selectively separating the aromatic mixture to provide a first fraction comprising 5% by weight or more benzene, toluene, xylene, or combinations thereof and a second fraction comprising C6 and higher linear hydrocarbons; and

recycling at least a portion of the first fraction to the feed.

17. The process of claim 16 further comprising selectively separating the second fraction to provide a C2-rich mixture comprising 50% by weight or more ethylene and a C3-rich mixture comprising 50% by weight or more propylene.

18. The process of claim 17 further comprising:

selectively separating the C2-rich mixture to provide an ethylene-rich product comprising 60% by weight or more ethylene and an ethane-rich product comprising 60% by weight or more ethane;

recycling at least a portion of the ethane-rich product to the feed; and

recovering at least a portion of the ethylene-rich product.

19. The process of claim 17 further comprising:

selectively separating the C3-rich mixture to provide a propylene-rich product comprising 60% by weight or more propylene and a propane-rich product comprising 60% by weight or more propane;

recycling at least a portion of the propane-rich product to the feed; and

recovering at least a portion of the propylene-rich product.

20. The process of claim 14 , further comprising:

cracking a refinery feed comprising gas oil, full range gas oil, resid, or any combination thereof to provide a cracked refinery feed comprising 5% by weight or more olefins; and

combining at least a portion of the cracked refinery feed with the cracked hydrocarbons.

21. A process for producing one or more olefins, comprising:

cracking a feed comprising 90% by weight or more C4 and higher hydrocarbons into one or more cracked hydrocarbons comprising one or more linear olefins and aromatics;

selectively separating the cracked hydrocarbons to provide an olefinic mixture comprising 20% by weight or more olefins and an aromatic mixture comprising 80% by weight or more C4 and higher hydrocarbons and one or more aromatics;

contacting a first portion of the aromatic mixture with a solvent comprising di-methyl sulfoxide, n-methylpyrrolidone, alkyl carbonates, derivatives thereof, or mixtures thereof to selectively separate at least a portion of the one or more aromatics from the aromatic mixture into the one or more solvents to provide an aromatic-lean mixture comprising 30% by weight or more olefins and 10% by weight or less aromatic hydrocarbons and an aromatic-rich mixture comprising aromatics and solvent;

selectively separating at least a portion of the one or more aromatics from the aromatic-rich mixture to provide an aromatic-rich mixture comprising 20% by weight or more benzene, toluene, xylene, or combinations thereof, and a solvent comprising the solvent with less than 20% by weight benzene, toluene, xylene, or combinations thereof;

recycling at least a portion of the aromatic-lean mixture to the feed;

recycling at least a portion of the aromatic-rich mixture to the feed; and

separating a second portion of the aromatic mixture to provide a low aromatics mixture and gasoline.