Reverse acid and hydrocarbon cascading in alkylation

Patent metadata

Field	Value
Publication number	US-10858299-B2
Application number	US-201916401595-A
Country	US
Kind code	B2
Filing date	May 2, 2019
Priority date	May 4, 2018
Publication date	Dec 8, 2020
Grant date	Dec 8, 2020

Abstract

A cascade reactor scheme with acid and hydrocarbon flowing in reverse directions. The systems and processes for alkylation of olefins herein may include providing a first olefin to a first alkylation zone, and a second olefin to a second alkylation zone. Isoparaffin may be provided to the first alkylation zone. The isoparaffin and first olefin may be contacted with a partially spent sulfuric acid in the first alkylation zone to form a spent acid phase and a first hydrocarbon phase including alkylate and unreacted isoparaffin. The first hydrocarbon phase and second olefin may be contacted with a sulfuric acid feed in the second alkylation zone to form a second hydrocarbon phase, also including alkylate and unreacted isoparaffin, and the partially spent sulfuric acid that is fed to the first alkylation zone. Further, the second hydrocarbon phase may be separated, recovering an isoparaffin fraction and an alkylate product fraction.

First claim

What is claimed:

1. A process for the alkylation of olefins, the process comprising:
providing a first olefin to a first alkylation zone;
providing a second olefin to a second alkylation zone, wherein the second olefin may be the same or different than the first olefin;
providing an isoparaffin to the first alkylation zone;
contacting the isoparaffin and the first olefin with a partially spent sulfuric acid in the first alkylation zone under alkylation conditions to form a spent acid phase and a first hydrocarbon phase comprising alkylate and unreacted isoparaffin;
contacting the first hydrocarbon phase and the second olefin with a sulfuric acid feed in the second alkylation zone under alkylation conditions to form a second hydrocarbon phase, comprising alkylate and unreacted isoparaffin, and the partially spent sulfuric acid fed to the first alkylation zone; and
separating the second hydrocarbon phase to recover an isoparaffin fraction and an alkylate product fraction.

2. The process of claim 1 , wherein an isoparaffin to olefin mole ratio in a total feed to the first reaction zone is greater than an isoparaffin to olefin mole ratio in a total feed to the second reaction zone.

3. The process of claim 1 , wherein an isoparaffin to olefin mole ratio in a total feed to the first reaction zone is at least 1.5 times an isoparaffin to olefin mole ratio in a total feed to the second reaction zone.

4. The process of claim 1 , wherein an isoparaffin to olefin mole ratio in a total feed to the first reaction zone is at least 1.75 times an isoparaffin to olefin mole ratio in a total feed to the second reaction zone.

5. The process of claim 1 , wherein an isoparaffin to olefin mole ratio in a total feed to the first reaction zone is at least 2 times an isoparaffin to olefin mole ratio in a total feed to the second reaction zone.

6. The process of claim 1 , wherein the alkylation conditions in the first and second alkylation zones include a reaction temperature of the first alkylation zone that is less than a reaction temperature of the second alkylation zone.

7. The process of claim 1 , wherein the first olefin comprises C3 and/or C4 and/or C5 olefins and wherein the second olefin comprises C3 and/or C4 and/or C5 olefins.

8. The process of claim 1 , further comprising feeding isoparaffin to the second alkylation zone.

9. The process of claim 1 , further comprising feeding sulfuric acid to the first alkylation zone directly.

10. A process for the alkylation of olefins, the process comprising:
providing a C5 olefin-containing feed to a first alkylation zone;
providing a C4 olefin-containing feed to a second alkylation zone;
providing a C3 olefin-containing feed to a third alkylation zone;
providing an isoparaffin to the first alkylation reactor;
contacting the isoparaffin and the C5 olefin with a second partially spent sulfuric acid in the first alkylation zone under alkylation conditions to form a spent acid phase and a first hydrocarbon phase comprising alkylate and unreacted isoparaffin;
contacting the first hydrocarbon phase and the C4 olefin with a first partially spent sulfuric acid in the second alkylation zone under alkylation conditions to form a second hydrocarbon phase, comprising alkylate and unreacted isoparaffin, and the second partially spent sulfuric acid fed to the first alkylation zone;
contacting the second hydrocarbon phase and the C3 olefin with a fresh sulfuric acid feed in the third alkylation zone under alkylation conditions to form a third hydrocarbon phase, comprising alkylate and unreacted isoparaffin, and the first partially spent sulfuric acid fed to the second alkylation zone; and
separating the third hydrocarbon phase to recover an isoparaffin fraction and an alkylate product fraction.

11. The process of claim 10 , wherein an isoparaffin to olefin mole ratio in a total feed to the first reaction zone is greater than an isoparaffin to olefin mole ratio in a total feed to the second reaction zone, and wherein an isoparaffin to olefin mole ratio in a total feed to the second reaction zone is greater than an isoparaffin to olefin mole ratio in a total feed to the third reaction zone (I R1 :O R1 >I R2 :O R2 >I R3 :O R3 ).

12. The process of claim 10 , wherein the alkylation conditions in the first and second alkylation zones include a reaction temperature of the first alkylation zone that is less than a reaction temperature of the second alkylation zone, and wherein the alkylation conditions in the second and third alkylation zones include a reaction temperature of the second alkylation zone that is less than a reaction temperature of the third alkylation zone (T R1 >T R2 >T R3 ).

13. The process of claim 10 , further comprising feeding isoparaffin to the second alkylation zone and the third alkylation zone.

14. The process of claim 10 , further comprising feeding sulfuric acid to the first alkylation zone and/or the second alkylation zone directly.

15. The process of claim 10 , further comprising maintaining an acid strength for a total acid feed to the first alkylation zone less than an acid strength for a total acid feed to the third alkylation zone.

16. A process for the alkylation of olefins, the process comprising:
providing a C5 olefin-containing feed to a first alkylation zone;
providing a C4 olefin-containing feed to a second alkylation zone;
providing a C3 olefin-containing feed to a third alkylation zone;
providing an isoparaffin to the first alkylation reactor;
contacting the isoparaffin and the C5 olefin with a first partially spent sulfuric acid in the first alkylation zone under alkylation conditions to form a second partially spent acid phase and a first hydrocarbon phase comprising alkylate and unreacted isoparaffin;
contacting the first hydrocarbon phase and the C4 olefin with the second partially spent sulfuric acid in the second alkylation zone under alkylation conditions to form a second hydrocarbon phase, comprising alkylate and unreacted isoparaffin, and a spent sulfuric acid;
contacting the second hydrocarbon phase and the C3 olefin with a fresh sulfuric acid feed in the third alkylation zone under alkylation conditions to form a third hydrocarbon phase, comprising alkylate and unreacted isoparaffin, and the first partially spent sulfuric acid fed to the first alkylation zone; and
separating the third hydrocarbon phase to recover an isoparaffin fraction and an alkylate product fraction.

17. The process of claim 16 , wherein an isoparaffin to olefin mole ratio in the total feed to the first or second reaction zones is greater than an isoparaffin to olefin mole ratio in the total feed to the third reaction zone.

18. The process of claim 16 , wherein the alkylation conditions in the first, second, and third alkylation zones include a reaction temperature of the first or second alkylation zone that is less than a reaction temperature of the third alkylation zone.

19. The process of claim 16 , further comprising feeding isoparaffin to the second alkylation zone and/or the third alkylation zone.

20. The process of claim 16 , further comprising feeding acid to the first alkylation zone and/or the second alkylation zone directly.

21. A process for the alkylation of olefins, the process comprising:
providing a first olefin to a first alkylation zone;
providing a second olefin to a second alkylation zone, wherein the second olefin may be the same or different than the first olefin;
providing a third olefin to a third alkylation zone, wherein the th

Assignees

• Lummus Technology Inc

Inventors

• Liu Zan
• Loezos Peter
• Medina Jackeline
• Lemoine Romain

Classifications

• B01J2219/00245

  Avoiding undesirable reactions or side-effects · CPC title

• B01J2219/00164

  controlling the flow · CPC title

• B01J2219/00042

  Features relating to reactants and process fluids · CPC title

• B01J2219/00027

  Process aspects · CPC title

• B01J19/30

  Loose or shaped packing elements, e.g. Raschig rings or Berl saddles, for pouring into the apparatus for mass or heat transfer · CPC title