Process for the controlled oligomerization of butenes

Patent metadata

Field	Value
Publication number	US-11312671-B2
Application number	US-202117362315-A
Country	US
Kind code	B2
Filing date	Jun 29, 2021
Priority date	Jun 29, 2020
Publication date	Apr 26, 2022
Grant date	Apr 26, 2022

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 olefins and/or isoolefins, the process comprising:
feeding an oxygenate reaction modifier and a mixed hydrocarbon feed to a fixed bed reactor containing an oligomerization catalyst, the mixed hydrocarbon feed comprising isobutene and optionally one or more of isobutane, n-butane, 1-butene, and 2-butene;
reacting isobutene in the fixed bed reactor at oligomerization conditions to form a reaction effluent comprising reaction modifier, isobutene dimers, unreacted isobutene, any oxygenate high-boiling reaction byproducts formed, as well as any unreacted isobutane, n-butane, 1-butene, and 2-butene;
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 reaction modifier, isobutene dimers, any oxygenate high-boiling reaction byproducts formed, as well as any unreacted isobutane, n-butane, 1-butene, and 2-butene;
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 any oxygenate high-boiling reaction byproducts, recovered as a bottoms fraction, from the isobutane, n-butane, and any unreacted isobutene, 1-butene, and 2-butene, recovered as an overheads fraction.

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, ethanol, propanol, isopropanol, and mixtures thereof.

4. The process of claim 1 , wherein the bottoms fraction further comprises 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.

5. The process of claim 4 wherein the side draw fraction comprises greater than 95 wt % isobutene dimers.

6. The process of claim 4 , 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 reaction modifier, the process further comprising:
recovering 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 modifier or oxygenated byproduct to one or more of the fixed bed reactor, the second fixed bed reactor, and the catalytic distillation reactor.

7. The process of claim 1 , further comprising:
feeding a C4 hydrocarbon mixture comprising isobutene, 1-butene, 2-butene, isobutane, and n-butane to a hydroisomerization reactor;
hydroismerizing the 1-butene in the C4 hydrocarbon mixture to form additional 2-butene;
fractionating the C4 hydrocarbon mixture to obtain an overheads fraction comprising the isobutene and isobutane and a bottoms fraction comprising 2-butene and n-butane; and
feeding the bottoms fraction comprising 2-butene and n-butane as the mixed hydrocarbon feed to the fixed bed reactor.

8. A process for the dimerization of olefins and/or isoolefins, the process comprising:
feeding an oxygenate reaction modifier and a mixed hydrocarbon feed to a fixed bed reactor containing an oligomerization catalyst, the mixed hydrocarbon feed comprising C4 hydrocarbons, C5 hydrocarbons, or a mixture of C4 and C5 hydrocarbons, the mixed hydrocarbons each respectively including isoolefins, n-olefins, isoparaffins and n-paraffins;
reacting isoolefins in the fixed bed reactor at oligomerization conditions to form a reaction effluent comprising reaction modifier, isoolefin dimers, unreacted isoolefin, any oxygenate high-boiling reaction byproducts formed, as well as any unreacted isoparaffins, n-paraffins, and n-olefins;
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 reaction modifier, isoolefin dimers, any oxygenate high-boiling reaction byproducts formed, as well as any unreacted isoparaffins, n-paraffins, and n-olefins;
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 any oxygenate high-boiling reaction byproducts, recovered as a bottoms fraction, from the isoparaffin, n-paraffin, and any unreacted isoolefin and n-olefin, recovered as an overheads fraction.

9. The process of claim 8 , 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.

10. The process of claim 8 , wherein the oxygenate reaction modifier is selected from the group consisting of methanol, ethanol, propanol, isopropanol, and mixtures thereof.

11. The process of claim 8 , wherein the bottoms fraction further comprises 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.

12. The process of claim 11 , wherein the side draw fraction comprises greater than 95 wt % isoolefin dimers.

13. The process of claim 11 , 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 reaction modifier, the process further comprising:
recovering 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 modifier or oxygenated byproduct to one or more of the fixed bed reactor, the second fixed bed reactor, and the catalytic distillation reactor.

14. A system for the selective dimerization of olefins and/or isoolefins, the system comprising:
a feed stream for conveying an oxygenate reaction modifier from an oxygenate reaction modifier supply system;
a feed stream for conveying a mixed hydrocarbon feed from a mixed hydrocarbon supply system, the mixed hydrocarbon feed comprising C4 hydrocarbons, C5 hydrocarbons, or a mixture of C4 and C5 hydrocarbons, the mixed hydrocarbons each respectively including isoolefins, n-olefins, isoparaffins and n-paraffins;
a fixed bed reactor containing an oligomerization catalyst, the fixed bed reactor being configured to receive the mixed h

Assignees

• Lummus Technology Inc

Inventors

• Barias Rosette
• Chen Liang
• Scott Michael Jon

Classifications

• Y02P20/10

  Process efficiency · CPC title

• B01D3/141

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

• C07C7/177 Primary

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

• B01D3/143

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

• B01D3/009 Primary

  in combination with chemical reactions · CPC title