Ethylene oligomerization/trimerization/tetramerization reactor

Patent metadata

Field	Value
Publication number	US-11623900-B2
Application number	US-202117166214-A
Country	US
Kind code	B2
Filing date	Feb 3, 2021
Priority date	Sep 18, 2015
Publication date	Apr 11, 2023
Grant date	Apr 11, 2023

Abstract

A process includes periodically or continuously introducing an olefin monomer and periodically or continuously introducing a catalyst system or catalyst system components into a reaction mixture within a reaction system, oligomerizing the olefin monomer within the reaction mixture to form an oligomer product, and periodically or continuously discharging a reaction system effluent comprising the oligomer product from the reaction system. The reaction system includes a total reaction mixture volume and a heat exchanged portion of the reaction system comprising a heat exchanged reaction mixture volume and a total heat exchanged surface area providing indirect contact between the reaction mixture and a heat exchange medium. A ratio of the total heat exchanged surface area to the total reaction mixture volume within the reaction system is in a range from 0.75 in−1 to 5 in−1, and an oligomer product discharge rate from the reaction system is between 1.0 (lb)(hr−1)(gal−1) to 6.0 (lb)(hr−1)(gal−1).

First claim

I claim:

1. A reaction system for oligomerizing an olefin monomer, the reaction system comprising:
one or more reaction system inlets configured to periodically or continuously introduce an olefin monomer, a catalyst system or catalyst system components, or any combination thereof to a reaction mixture within the reaction system;
one or more reaction system reaction mixture outlets configured to periodically or continuously discharge a reaction system effluent comprising an oligomer product from the reaction system;
a total reaction mixture volume within the reaction system; and
a heat exchanged portion of the reaction system comprising a heat exchanged reaction mixture volume and a total heat exchanged surface area providing indirect thermal contact between the reaction mixture and a heat exchange medium;
wherein the reaction system is configured to have an oligomer product discharge rate between 1.5 lb/hr/gal to 6.0 lb/hr/gal; and
wherein a ratio of the total heat exchanged surface area to the total reaction mixture volume within the reaction system is in a range from 0.75 in −1 to 5 in −1 .

2. The reaction system of claim 1 , wherein the reaction system further comprises a non-heat exchanged portion of the reaction system comprising a non-heat exchanged reaction mixture volume and a total non-heat exchanged surface area that does not provide heat exchange between the reaction mixture and the heat exchange medium.

3. The reaction system of claim 2 , wherein an average temperature of the reaction mixture within the non-heat exchanged portion the reaction system is within 0.61% of an average temperature of the reaction mixture within the heat exchanged portion of the reaction system.

4. The reaction system of claim 1 , wherein an average temperature of the heat exchange medium is within 9.3% of the average temperature of the reaction mixture within the heat exchanged portion of the reaction system.

5. The reaction system of claim 1 , wherein a ratio of the heat exchanged reaction mixture volume to the total reaction mixture volume within the reaction system is in a range from 0.70 to 1.0.

6. The reaction system of claim 1 , wherein the reaction system comprises a reactor selected from the group consisting of a continuous stirred tank reactor, a plug flow reactor, or any combinations thereof.

7. The reaction system of claim 6 , wherein the reaction system comprises a continuous stirred tank reactor wherein the heat exchange medium is in indirect contact with the reaction mixture within a jacket around at least a portion of an outer wall of the continuous stirred tank reactor, within internal heat exchange coils, or any combination thereof.

8. The reaction system of claim 6 , wherein the reaction system comprises one or more plug flow reactors wherein the heat exchange medium is in indirect contact with the reaction mixture through a wall of at least a portion of the one or more one plug flow reactors.

9. The reaction system of claim 6 , wherein the reaction system comprises a reaction mixture path comprising the reactor and wherein a portion of the reaction mixture is recycled through the reactor and a ratio of a volumetric reaction mixture recycle flow rate to a volumetric discharge rate of the reaction system effluent is between 8 and 60.

10. The reaction system of claim 9 , wherein the reaction mixture path includes a pump.

11. The reaction system of claim 1 , wherein the ratio of the total reaction system heat exchanged surface area to the total reaction mixture volume within the reaction system is in a range from a minimum value described by the equation [0.64*(oligomer product discharge rate from the reaction system)]−1.16 to a maximum value described by the equation [0.64*(oligomer product discharge rate from the reaction system)]+0.76.

12. The reaction system of claim 1 , wherein the olefin monomer consists essentially of ethylene.

13. The reaction system of claim 12 , wherein the catalyst system or catalyst system components comprise i) a chromium compound complexed to a heteroatomic ligand and a metal alkyl compound, or ii) a chromium compound, a heteroatomic ligand, and a metal alkyl compound.

14. The reaction system of claim 13 , wherein the heteroatomic ligand is selected from pyrrole compounds, diphosphinoaminyl compounds, N 2 -phosphinylamidine compounds, N 2 -phosphinylformamidine compounds, phosphinyl guanidine compounds, and combinations thereof.

15. The reaction system of claim 13 , wherein the oligomer product comprises at least 70 weight % hexenes, octenes, or any combination thereof.

16. The reaction system of claim 13 , wherein the catalyst system or catalyst system components comprise
a) a trialkylaluminum compound,
b) a nickel salt and an organophosphorus compound,
c) a nickel complex of an organophosphorus compound,
d) a zirconium halide and a metal compound,
e) a zirconium halide, alkoxide, or carboxylate, a Lewis base, and an alkylaluminum compound,
f) a transition metal complex comprising a transition metal compound complexed to a ligand comprising an α-diimine group and a metal alkyl compound,
g) a transition metal complex comprising a transition metal compound complexed to a ligand comprising a pyridine bisimine group and a metal alkyl compound, or
h) a transition metal compound, a ligand comprising a pyridine bisimine group, and a metal alkyl compound.

17. A reaction system for oligomerizing an olefin monomer, the reaction system comprising:
a reactor selected from the group consisting of a continuous stirred tank reactor, a plug flow reactor, or any combinations thereof;
a pump;
one or more reaction system inlets configured to periodically or continuously introduce an olefin monomer, a catalyst system or catalyst system components, or any combination thereof to a reaction mixture within the reaction system;
one or more reaction system reaction mixture outlets configured to periodically or continuously discharge a reaction system effluent comprising an oligomer product from the reaction system;
a total reaction mixture volume within the reaction system; and
a heat exchanged portion of the reaction system comprising a heat exchanged reaction mixture volume, and a total heat exchanged surface area providing indirect thermal contact between the reaction mixture and a heat exchange medium;
wherein a reaction mixture path comprises the pump and the reactor,
wherein the reaction system is configured to have an oligomer product discharge rate between 1.5 lb/hr/gal to 6.0 lb/hr/gal; and
wherein a ratio of the total heat exchanged surface area to the total reaction mixture volume within the reaction system is in a range from 1.25 in −1 to 3.5 in −1 .

18. The reaction system of claim 17 , wherein the reaction system comprises a reaction mixture path comprising the reactor and the pump, and wherein a portion of the reaction mixture is recycled through the reactor and a ratio of a volumetric reaction mixture recycle flow rate to a volumetric discharge rate of the reaction system effluent is between 8 and 60.

19. The reaction system of claim 17 , wherein the reaction system further comprises a non-heat exchanged portion of the reaction system comprising a non-heat exchanged reaction mixture volume and a total non-heat exchanged surface area that does not provide heat exchange between the reaction mixture and the heat exchange medium wherein a) an average temperature of the heat exchange medium is within 9.3% of the average temperature of the reaction mixture within the heat exchanged portion of th

Assignees

• Chevron Phillips Chemical Co Lp

Inventors

• Kreischer Bruce E

Classifications

• C07C2/32 Primary

  as complexes, e.g. acetyl-acetonates {(complexes of salts of acids of halogen C07C2/20)} · CPC title

• B01J19/1881

  externally, i.e. the mixture leaving the vessel and subsequently re-entering it · CPC title

• C07C2531/12

  containing organo-metallic compounds or metal hydrides · CPC title

• B01J2219/00056

  involving measured parameters · CPC title

• B01J2219/00108

  involving reactant vapours · CPC title