Process for desulfurization of naphtha using ionic liquids

Patent metadata

Field	Value
Publication number	US-9783747-B2
Application number	US-201313928578-A
Country	US
Kind code	B2
Filing date	Jun 27, 2013
Priority date	Jun 27, 2013
Publication date	Oct 10, 2017
Grant date	Oct 10, 2017

Abstract

A process has been developed in which some of the sulfur in a naphtha feed is removed using ionic liquids. The ionic liquid desulfurization step, which operates at low temperatures and pressures, is followed by a catalytic hydrodesulfurizaton step.

First claim

What is claimed is:

1. A method for desulfurization of naphtha comprising:
introducing a thermally or catalytically cracked naphtha stream containing sulfur compounds and a naphtha-immiscible ionic liquid into an ionic liquid desulfurization zone to remove a first portion of the sulfur compounds to provide an effluent comprising naphtha having reduced sulfur and a naphtha-immiscible ionic liquid containing the sulfur compounds; and
introducing the effluent comprising naphtha having reduced sulfur from the ionic liquid desulfurization zone and hydrogen into a catalytic hydrodesulfurization zone to remove a second portion of the sulfur compounds.

2. The method of claim 1 further comprising: separating an effluent from the catalytic hydrodesulfurization zone into a low sulfur liquid component and a sulfur containing gas component.

3. The method of claim 2 further comprising separating the low sulfur liquid component into a low sulfur naphtha stream and a low sulfur lights ends stream, and recovering the low sulfur naphtha stream.

4. The method of claim 2 further comprising removing sulfur from the sulfur containing gas component.

5. The method of claim 1 further comprising:
separating the effluent comprising naphtha from the ionic liquid desulfurization zone into a low sulfur naphtha overhead stream and a bottoms stream before introducing the effluent comprising naphtha from the ionic liquid desulfurization zone into the catalytic hydrodesulfurization zone, wherein introducing the effluent comprising naphtha from the ionic liquid desulfurization zone into the catalytic hydrodesulfurization zone comprises introducing the bottoms stream into the catalytic hydrodesulfurization zone;
separating an effluent from the catalytic hydrodesulfurization zone into a low sulfur liquid component and a sulfur containing gas component; and
recovering the low sulfur liquid component.

6. The method of claim 1 wherein the thermally or catalytically cracked naphtha stream contains diolefins, and further comprising introducing the thermally or catalytically cracked naphtha stream and hydrogen to a stabilization zone to saturate the diolefin compounds before the thermally or catalytically cracked naphtha stream is introduced into the ionic liquid desulfurization zone.

7. The method of claim 1 wherein the naphtha-immiscible ionic liquid comprises at least one of an imidazolium ionic liquid, a phosphonium ionic liquid, and a pyridinium ionic liquid.

8. The method of claim 1 wherein the naphtha-immiscible ionic liquid comprises at least one of 1-ethyl-3-methylimidazolium ethyl sulfate, 1-butyl-3-methylimidazolium hydrogen sulfate, 1-ethyl-3-methylimidazolium chloride, 1-butyl-3-methylimidazolium chloride, tetrabutylphosphonium methane sulfonate, pyridinium p-toluene sulfonate, tetrabutylphosphonium chloride, tetrabutylphosphonium bromide, tributyl(octyl)phosphonium chloride, and tributyl(ethyl)phosphonium diethylphosphate, 1-butyl-3-methylimidazolium trifluoromethanesulfonate, 1-butyl-4-methylpyridinium chloride, N-butyl-3-methylpyridinium methyl sulfate, trihexyl(tetradecyl)phosphonium chloride, trihexyl(tetradecyl)phosphonium bromide, tributyl(methyl)phosphonium bromide, tributyl(methyl)phosphonium chloride, tributyl(hexyl)phosphonium bromide, tributyl(hexyl)phosphonium chloride, tributyl(octyl)phosphonium bromide, tributyl(decyl)phosphonium bromide, tributyl(decyl)phosphonium chloride, triisobutyl(methyl)phosphonium tosylate, and tetrabutylphosphonium methanesulfonate.

9. The method of claim 1 further comprising regenerating the naphtha-immiscible ionic liquid stream containing the sulfur compounds.

10. The method of claim 9 wherein regenerating the naphtha-immiscible ionic liquid stream containing the sulfur compounds comprises:
contacting the naphtha-immiscible ionic liquid stream containing the sulfur compounds with a regeneration solvent; and
separating the naphtha-immiscible ionic liquid stream from the regeneration solvent to produce an extract stream comprising the sulfur compounds and a regenerated naphtha-immiscible ionic liquid stream.

11. The method of claim 9 wherein regenerating the naphtha-immiscible ionic liquid stream containing the sulfur compounds comprises separating the naphtha-immiscible ionic liquid stream by steam stripping to produce the extract stream comprising the sulfur compounds and the regenerated naphtha-immiscible ionic liquid stream.

12. A method for desulfurization of naphtha comprising:
introducing a thermally or catalytically cracked naphtha stream containing sulfur compounds and a naphtha-immiscible ionic liquid into an ionic liquid desulfurization zone to remove a first portion of the sulfur compounds to provide an effluent comprising naphtha having reduced sulfur and a naphtha-immiscible ionic liquid containing the sulfur compounds;
introducing the effluent comprising naphtha having reduced sulfur from the ionic liquid desulfurization zone and hydrogen into a catalytic hydrodesulfurization zone to remove a second portion of the sulfur compounds;
separating an effluent from the catalytic hydrodesulfurization zone into a low sulfur liquid component and a sulfur containing gas component; and
regenerating the naphtha-immiscible ionic liquid containing the sulfur compounds by steam stripping to produce the extract stream comprising the sulfur compounds and the regenerated naphtha-immiscible ionic liquid stream.

13. The method of claim 12 further comprising: separating the low sulfur liquid component into a low sulfur naphtha stream and a low sulfur lights ends stream.

14. The method of claim 12 further comprising:
separating the effluent from the ionic liquid desulfurization zone into a low sulfur naphtha overhead stream and a bottoms stream before introducing the effluent from the ionic liquid desulfurization zone into the catalytic hydrodesulfurization zone, wherein introducing the effluent from the ionic liquid desulfurization zone into the catalytic hydrodesulfurization zone comprises introducing the bottoms stream into the catalytic hydrodesulfurization zone;
separating an effluent from the catalytic hydrodesulfurization zone into a low sulfur liquid component and a sulfur containing gas component; and
recovering the low sulfur liquid component.

15. The method of claim 12 further comprising removing sulfur from the sulfur containing gas component.

16. The method of claim 12 wherein the thermally or catalytically cracked naphtha stream contains diolefins, and further comprising introducing the thermally or catalytically cracked naphtha stream and hydrogen to a stabilization zone to saturate the diolefin compounds before the thermally or catalytically cracked naphtha stream is introduced into the ionic liquid desulfurization zone.

17. The method of claim 12 wherein the naphtha-immiscible ionic liquid comprises at least one of an imidazolium ionic liquid, a phosphonium ionic liquid, and a pyridinium ionic liquid.

18. The method of claim 12 wherein the naphtha-immiscible ionic liquid comprises at least one of 1-ethyl-3-methylimidazolium ethyl sulfate, 1-butyl-3-methylimidazolium hydrogen sulfate, 1-ethyl-3-methylimidazolium chloride, 1-butyl-3-methylimidazolium chloride, tetrabutylphosphonium methane sulfonate, pyridinium p-toluene sulfonate, tetrabutylphosphonium chloride, tetrabutylphosphonium bromide, tributyl(octyl)phosphonium chloride, and tributyl(ethyl)phosphonium diethylphosphate, 1-butyl-3-methylimidazolium trifluoromethanesulfonate, 1-butyl-4-methylpyridinium chloride, N-butyl-3-methylpyridinium methyl sulfate, trihexy

Assignees

• Uop Llc

Inventors

• Gattupalli Rajeswar R
• Banerjee Soumendra M
• Nicholas Christopher P
• Bhatacharyya Alakananda

Classifications

• C10G67/04 Primary

  including solvent extraction as the refining step in the absence of hydrogen · CPC title

• C10G21/20

  Nitrogen-containing compounds · CPC title

• C10G2300/202

  Heteroatoms content, i.e. S, N, O, P · CPC title

• C10G45/04

  characterised by the catalyst used · CPC title

• C10G21/24

  Phosphorus-containing compounds · CPC title