Separation of conjunct polymer from volatile regenerant for ionic liquid regeneration

Patent metadata

Field	Value
Publication number	US-9776877-B2
Application number	US-201414567913-A
Country	US
Kind code	B2
Filing date	Dec 11, 2014
Priority date	Dec 11, 2014
Publication date	Oct 3, 2017
Grant date	Oct 3, 2017

Abstract

Processes for separating conjunct polymer from an organic phase are described. A mixture comprising an ionic liquid phase and the organic phase into the ionic phase and an organic phase comprising the conjunct polymer and at least one silyl or boryl compound. The organic phase is separated in a fractionation column into an overhead fraction comprising unreacted silane or borane compound and a bottoms fraction comprising the conjunct polymer and the silyl or boryl compound. The bottoms fraction is passed through an adsorption zone, and the silyl or boryl compound is recovered. Alternatively, the organic phase is passed through an adsorption zone first to remove the conjunct polymer and then a fractionation zone to separate the unreacted silane or borane compound from the silyl or boryl compound.

First claim

What is claimed is:

1. A process for separating conjunct polymer from an organic phase comprising:
separating a mixture comprising an ionic liquid phase and the organic phase into the ionic phase comprising ionic liquid and the organic phase comprising the conjunct polymer and at least one silyl or boryl compound having an unreacted silane or borane compound; and
separating the organic phase in a first fractionation column into at least a first overhead fraction comprising unreacted silane or borane compound and a first bottoms fraction comprising the conjunct polymer and at least a portion of the at least one silyl or boryl compound wherein separating the organic phase in the first fractionation column into at least the first overhead fraction comprising unreacted silane or borane compound and the first bottoms fraction comprising the conjunct polymer and the at least the portion of the at least one silyl or boryl compound comprises separating the organic phase in the fractionation column into at least the first overhead fraction comprising unreacted silane or borane compound, the first bottoms fraction comprising the conjunct polymer and the at least the portion of the at least one silyl or boryl compound, and a fraction comprising at least a second portion of the at least one silyl or boryl compound; and either
passing the first bottoms fraction through a first adsorption zone;
recovering the at least the portion of the at least one silyl or boryl compound;
or
passing the organic phase through a second adsorption zone;
recovering a stream comprising unreacted silane or borane compound and the at least one silyl or boryl compound;
separating the stream comprising the unreacted silane or borane compound and the at least one silyl or boryl compound in a second fractionation column into at least a second overhead fraction comprising the unreacted silane or borane compound and a second bottoms fraction comprising the at least a portion of the at least one silyl or boryl compound.

2. The process of claim 1 wherein at least one of the first and second adsorption zones contains an adsorbent comprising alumina, silica, aluminosilicate, activated carbon, and combinations thereof.

3. The process of claim 1 wherein separating the mixture comprises:
separating the ionic liquid phase from the organic phase in a gravity separation zone into a first ionic liquid stream and a stream comprising the organic phase containing ionic liquid; and
separating the stream comprising the organic phase containing ionic liquid in a coalescer into a second ionic liquid stream and an organic stream; and
wherein separating the organic phase in the first fractionation column comprises separating the organic stream in the first fractionation column;
or
wherein passing the organic phase through the second adsorption zone comprises passing the organic stream through the second adsorption zone.

4. The process of claim 1 further comprising at least one of:
recycling the ionic liquid phase to a reaction zone; and
recycling the first or second overhead fraction to a regeneration zone.

5. The process of claim 1 further comprising:
controlling a composition of the first bottoms fraction by controlling a flow rate of the fraction comprising at least the second portion of the at least one silyl or boryl compound or a flow rate of the first bottoms fraction.

6. The process of claim 1 wherein the organic phase further comprises a solvent; and
either
wherein the first overhead fraction comprises the solvent; or
wherein the stream comprising unreacted silane or borane compound and the at least one silyl or boryl compound further comprises the solvent, and wherein the second overhead fraction comprises the solvent.

7. The process of claim 6 wherein the solvent comprises a normal paraffin, an isoparaffin, or a cyclic paraffin having up to 10 carbon atoms, an aromatic, or the at least one silane or borane compound.

8. The process of claim 1 further comprising:
desorbing the conjunct polymer from the first or second adsorption zone; and
recovering the conjunct polymer.

9. The process of claim 8 wherein desorbing the conjunct polymer from the first or second adsorption zone comprises at least one of:
introducing a desorbent into the first or second adsorption zone;
calcinating the adsorbent in air or presence of oxygen; and steam stripping the adsorbent.

10. The process of claim 1 further comprising:
replacing an adsorbent in the adsorption zone.

11. A process for separating conjunct polymer from an organic phase comprising:
separating a mixture comprising an ionic liquid phase comprising ionic liquid and the organic phase comprising the conjunct polymer and at least one silyl or boryl compound in a gravity separator into a first ionic liquid stream and a stream comprising the organic phase containing ionic liquid;
separating the stream comprising the organic phase containing ionic liquid in a coalescer into a second ionic liquid stream and an organic stream having an unreacted silane or borane compound; and
separating the organic stream in a fractionation column into at least a first overhead fraction comprising unreacted silane or borane compound and a bottoms fraction comprising the conjunct polymer and at least a portion of the at least one silyl or boryl compound wherein separating the organic stream in the fractionation column into at least the first overhead fraction comprising unreacted silane or borane compound and the bottoms fraction comprising the conjunct polymer and the at least the portion of the at least one silyl or boryl compound comprises separating the organic stream in the fractionation column into at least the first overhead fraction comprising unreacted silane or borane compound, the bottoms fraction comprising the conjunct polymer and the at least the portion of the at least one silyl or boryl compound, and a fraction comprising at least a second portion of the at least one silyl or boryl compound; and either
passing the bottoms fraction through a first adsorption zone containing an adsorbent comprising alumina, silica, aluminosilicate, activated carbon, and combinations thereof;
recovering the at least the portion of the at least one silyl or boryl compound;
or
passing the organic stream through a second adsorption zone containing an adsorbent comprising alumina, silica, aluminosilicate, activated carbon, and combinations thereof;
recovering a stream comprising unreacted silane or borane compound and the at least one silyl or boryl compound;
separating the stream comprising unreacted silane or borane compound and the at least one silyl or boryl compound in a fractionation column into at least a second overhead fraction comprising the unreacted silane or borane compound and a second bottoms fraction comprising the at least a portion of the at least one silyl or boryl compound.

12. The process of claim 11 further comprising at least one of:
recycling at least one of the first and second ionic liquid streams to a reaction zone; and
recycling the first or second overhead fraction to a regeneration zone.

13. The process of claim 11 further comprising:
controlling a composition of the first bottoms fraction by controlling a flow rate of the fraction comprising at least the second portion of the at least one silyl or boryl compound or a flow rate of the first bottoms fraction.

14. The process of claim 11 wherein the organic phase further comprises a solvent; and
either
wherein the first overhead fraction comprises the solvent; or
wherein the stream comprising unreacted silane or borane compound and th

Assignees

• Uop Llc

Inventors

• Wegerer David A
• Pham Trung

Classifications

• B01J31/4092

  involving a stripping step, with stripping gas or solvent · CPC title

• B01J38/50

  using organic liquids · CPC title

• B01J31/0274

  containing silicon (ligands in coordination complexes B01J31/1608) · CPC title

• B01J2531/98

  Phase-transfer catalysis in a mixed solvent system containing at least 2 immiscible solvents or solvent phases · CPC title

• B01J31/146

  of boron · CPC title