Process for the controlled oligomerization of butenes

Patent metadata

Field	Value
Publication number	US-11939289-B2
Application number	US-202218148103-A
Country	US
Kind code	B2
Filing date	Dec 29, 2022
Priority date	Jun 29, 2020
Publication date	Mar 26, 2024
Grant date	Mar 26, 2024

Abstract

The selective dimerization of isoolefins, such as isobutene or isopentane, or mixtures thereof, may be conducted in a system including a series of fixed bed reactors and a catalytic distillation reactor. The system may provide for conveyance of the fixed bed reactor effluents, without componential separation, to a downstream reactor. It has been found that a high selectivity to the dimer may be achieved even though intermediate separation of the desired product from unreacted components between reactors is not performed. Further, embodiments provide for use of a divided wall column for recovery of a high purity dimer product, reducing unit piece count and plot size.

First claim

What is claimed:

1. A process for the dimerization of isoolefins, the process comprising:
feeding an oxygenate reaction modifier and a hydrocarbon feed to a fixed bed reactor containing an oligomerization catalyst, the hydrocarbon feed comprising isobutene and a secondary feed comprising butanes;
reacting isobutene in the fixed bed reactor at oligomerization conditions to form a reaction effluent comprising the oxygenate reaction modifier, isobutene dimers, unreacted isobutene, any oxygenate reaction byproducts formed, as well as butanes;
without componential separation, feeding the reaction effluent to a second fixed bed reactor containing an oligomerization catalyst;
reacting the unreacted isobutene in the second fixed bed reactor at oligomerization conditions to form additional isobutene dimers, recovering a second reaction effluent comprising the oxygenate reaction modifier, isobutene dimers, any oxygenate reaction byproducts formed, as well as butanes;
without componential separation, feeding the second reaction effluent to a catalytic distillation reactor having a reactive distillation zone comprising an oligomerization catalyst;
concurrently within the catalytic distillation reactor:
reacting unreacted isobutene in the second reaction effluent to form additional isobutene dimers;
separating the dimers and the oxygenate reaction byproducts, recovered as a bottoms fraction, from the isobutane and n-butane, and any unreacted isobutene, recovered as an overheads fraction; and

recycling the overheads fraction to the hydrocarbon feed;
wherein the bottoms fraction further comprises the oxygenate reaction modifier and isobutene trimers, the process further comprising separating the bottoms fraction in a divided wall distillation column to recover an overheads fraction, a side draw fraction comprising the isobutene dimers, and a bottoms fraction comprising the isobutene trimers; and
wherein the side draw fraction comprises greater than 95 wt % isobutene dimers.

2. The process of claim 1 , wherein the oligomerization catalyst contained in each of the fixed bed reactor, second fixed bed reactor, and reactive distillation zone comprises a sulfonic acid catalyst.

3. The process of claim 1 , wherein the oxygenate reaction modifier is selected from the group consisting of methanol and ethanol, and mixtures thereof.

4. The process of claim 1 , wherein the secondary feed is fed to the reactor initially and the n-butane is recycled in a closed loop cycle.

5. A process for the dimerization of isoolefins, the process comprising:
feeding an oxygenate reaction modifier and a hydrocarbon feed to a fixed bed reactor containing an oligomerization catalyst, the hydrocarbon feed consisting of isoolefins and n-paraffins;
reacting isoolefins in the fixed bed reactor at oligomerization conditions to form a reaction effluent comprising the oxygenate reaction modifier, isoolefin dimers, unreacted isoolefin, any oxygenate reaction byproducts formed, as well as n-paraffins;
without componential separation, feeding the reaction effluent to a second fixed bed reactor containing an oligomerization catalyst;
reacting the unreacted isoolefins in the second fixed bed reactor at oligomerization conditions to form additional isoolefin dimers, recovering a second reaction effluent comprising the oxygenate reaction modifier, isoolefin dimers, any oxygenate reaction byproducts formed, as well as n-paraffins;
without componential separation, feeding the second reaction effluent to a catalytic distillation reactor having a reactive distillation zone comprising an oligomerization catalyst;
concurrently within the catalytic distillation reactor:
reacting unreacted isoolefins in the second reaction effluent to form additional isoolefin dimers;
separating the dimers and the oxygenate reaction byproducts, recovered as a bottoms fraction, from the n-paraffin, and any unreacted isoolefin, recovered as an overheads fraction;

recycling the overheads fraction to the hydrocarbon feed;
wherein the bottoms fraction further comprises the oxygenate reaction modifier and isoolefin trimers, the process further comprising separating the bottoms fraction in a divided wall distillation column to recover an overheads fraction, a side draw fraction comprising the isoolefin dimers, and a bottoms fraction comprising the isoolefin trimers; and
wherein the side draw fraction comprises greater than 95 wt % isoolefin dimers.

6. The process of claim 5 , wherein the oligomerization catalyst contained in each of the fixed bed reactor, second fixed bed reactor, and reactive distillation zone comprises a sulfonic acid catalyst.

7. The process of claim 5 , wherein the oxygenate reaction modifier is selected from the group consisting of methanol and ethanol, and mixtures thereof.

8. The process of claim 5 , wherein one or both of the bottoms fraction from the divided wall distillation column and the overheads fraction from the divided wall distillation column comprise oxygenated byproducts or comprise the oxygenate reaction modifier, the process further comprising:
recovering the oxygenate reaction modifier or oxygenated byproducts from one or both of the bottoms fraction from the divided wall distillation column and the overheads fraction from the divided wall distillation column; and
recycling the recovered oxygenate reaction modifier or oxygenated byproducts to the fixed bed reactor, the second fixed bed reactor, the catalytic distillation reactor, or a combination thereof.

9. A process for the dimerization of isoolefins, the process comprising:
feeding an oxygenate reaction modifier and a hydrocarbon feed to a fixed bed reactor containing an oligomerization catalyst, the hydrocarbon feed comprising isobutene and a secondary feed comprising butanes;
reacting isobutene in the fixed bed reactor at oligomerization conditions to form a reaction effluent comprising the oxygenate reaction modifier, isobutene dimers, unreacted isobutene, any oxygenate reaction byproducts formed, as well as butanes;
without componential separation, feeding the reaction effluent to a second fixed bed reactor containing an oligomerization catalyst;
reacting the unreacted isobutene in the second fixed bed reactor at oligomerization conditions to form additional isobutene dimers, recovering a second reaction effluent comprising oxygenate reaction modifier, isobutene dimers, any oxygenate reaction byproducts formed, as well butanes;
without componential separation, feeding the second reaction effluent to a catalytic distillation reactor having a reactive distillation zone comprising an oligomerization catalyst;
concurrently within the catalytic distillation reactor:
reacting unreacted isobutene in the second reaction effluent to form additional isobutene dimers;
separating the dimers and the oxygenate reaction byproducts, recovered as a bottoms fraction, from the isobutane and n-butane, and any unreacted isobutene, recovered as an overheads fraction; and

recycling the overheads fraction to the hydrocarbon feed;
wherein the bottoms fraction further comprises the oxygenate reaction modifier and isobutene trimers, the process further comprising separating the bottoms fraction in a divided wall distillation column to recover an overheads fraction, a side draw fraction comprising the isobutene dimers, and a bottoms fraction comprising the isobutene trimers; and
wherein one or both of the bottoms fraction from the divided wall distillation column and the overheads fraction from the divided wall distillation column comprise oxygenated byproducts or comprise the oxygenate reaction modifier, the process further comprising:
recovering the oxygenate reaction modifier or oxygenated byproducts from one or both

Assignees

• Lummus Technology Inc

Inventors

• Barias Rosette
• Chen Liang
• Scott Michael Jon

Classifications

• C07C7/177 Primary

  by selective oligomerisation or polymerisation of at least one compound of the mixture · CPC title

• B01D3/009 Primary

  in combination with chemical reactions · CPC title

• B01D3/141

  where at least one distillation column contains at least one dividing wall · CPC title

• B01D3/143

  by two or more of a fractionation, separation or rectification step · CPC title

• B01J8/0419

  the beds being placed in separate reactors · CPC title