Process for the regeneration of an alkaline solution utilized in a process for the extraction of sulphur-containing compounds comprising a washing step

Patent metadata

Field	Value
Publication number	US-10808182-B2
Application number	US-201815907927-A
Country	US
Kind code	B2
Filing date	Feb 28, 2018
Priority date	Mar 1, 2017
Publication date	Oct 20, 2020
Grant date	Oct 20, 2020

Abstract

The present invention relates to the field of the extraction of sulphur-containing compounds such as the mercaptans, COS or H 2 S from a hydrocarbon-containing cut. This selective extraction is carried out by bringing the hydrocarbon-containing cut in liquid phase into contact with an alkaline solution, for example soda. The process according to the invention is an improved process for the regeneration of the alkaline solution, making it possible to reduce the quantity of alkaline solution required in the regeneration section.

First claim

The invention claimed is:

1. Process for the regeneration of a used alkaline solution ( 1 a ) utilized in a unit for the extraction of the sulphur-containing compounds from a hydrocarbon-containing cut, comprising the following sequence of steps:
a) sending the used alkaline solution ( 1 a ) into an oxidation reactor ( 4 ) in which it is brought into contact with an oxidizing agent ( 5 ) and a catalyst ( 3 ), said used alkaline solution being heated to a temperature between 40° C. and 50° C. before being sent into the oxidation reactor ( 4 ),
b) sending the effluents ( 7 ) of the oxidation reactor ( 4 ) into a separator ( 8 ) from which a hydrocarbon phase rich in disulphides ( 10 ), and a partially regenerated alkaline solution ( 11 ) are separated and extracted,
c) cooling the partially regenerated alkaline solution ( 11 ) originating from step b) to a temperature less than or equal to 45° C.,
d) dividing the partially regenerated alkaline solution ( 15 ) cooled in step c) into two flows:
a flow constituting an excess of cooled partially regenerated alkaline solution which is recirculated and either sent upstream of ( 21 a ), or directly into ( 22 a ), the oxidation reactor ( 4 ), and which constitutes a cooling means used to control a rise in temperature of said oxidation reactor, and,
a flow ( 21 b ) or ( 22 b ) which continues in the following steps of the regeneration process,

e) mixing the flow ( 21 b ) or ( 22 b ), originating from step d), with a hydrocarbon-containing cut without sulphur-containing compounds ( 16 ), and
f) sending the mixture originating from step e) into a separator ( 18 ) from which a totally regenerated alkaline solution ( 19 ), and a hydrocarbon-containing cut partially enriched with disulphides ( 6 ) are separated and extracted.

2. Process for the regeneration of a used alkaline solution according to claim 1 , in which the excess ( 21 a ) of recirculated cooled partially regenerated alkaline solution is sent upstream of said oxidation reactor ( 4 ) and is introduced into said oxidation reactor ( 4 ) in a mixture with the used alkaline solution ( 1 a ).

3. Process for the regeneration of a used alkaline solution according to claim 1 , in which the excess ( 22 a ) of recirculated cooled partially regenerated alkaline solution is sent to the oxidation reactor ( 4 ) directly to one or more points of said oxidation reactor ( 4 ).

4. Process for the regeneration of a used alkaline solution according to claim 3 , in which the point or points of introduction of the excess of recirculated cooled partially regenerated alkaline solution into the oxidation reactor ( 4 ) are provided with a diffusion means or a mixing means.

5. Process for the regeneration of a used alkaline solution according to claim 3 , in which the point or points of introduction of the excess of recirculated cooled partially regenerated alkaline solution into the oxidation reactor ( 4 ) are positioned so as to control a rise in temperature of the oxidation reactor ( 4 ).

6. Process for the regeneration of a used alkaline solution according to claim 1 , in which the catalyst employed in the oxidation reactor ( 4 ) comprises cobalt or a vanadium phthalocyanine.

7. Process for the regeneration of a used alkaline solution according to claim 1 , in which the catalyst employed in the oxidation reactor ( 4 ) is added to the used alkaline solution ( 1 a ) when sent into the oxidation reactor ( 4 ), so as to achieve a concentration of catalyst in the used alkaline solution between 10 and 1,000 ppm by weight.

8. Process for the regeneration of a used alkaline solution according to claim 1 , in which the oxidation reactor ( 4 ) is equipped with an additional cooling means ( 23 ).

9. Process for the regeneration of a used alkaline solution according to claim 1 , in which the excess of recirculated cooled partially regenerated alkaline solution ( 21 a ) or ( 22 a ) is cooled to a temperature at least 5° C. less than that of the cooled partially regenerated alkaline solution from step c), before being sent to the oxidation reactor ( 4 ).

10. Process for the regeneration of a used alkaline solution according to claim 1 , in which the hydrocarbon-containing cut from which the sulphur-containing compounds are extracted to provide the used alkaline solution ( 1 a ) ranges from a methane cut to a kerosene cut.

11. Process for the regeneration of a used alkaline solution according to claim 1 , in which the catalyst employed in the oxidation reactor ( 4 ) is added to the used alkaline solution ( 1 a ) when sent into the oxidation reactor ( 4 ), so as to achieve a concentration of catalyst in the used alkaline solution between 10 and 500 ppm by weight.

Assignees

• Axens

Inventors

• Besnault Jean-Michel
• Ferrero Sebastien
• Do Mai Phuong

Classifications

• B01D53/00

  Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols, (recovery of volatile solvents by condensation B01D5/00; sublimation B01D7/00; cold traps, cold baffles B01D8/00; working-up undefined gaseous mixtures obtained by cracking hydrocarbon oils C10G70/00; cleaning coal gas C10K; working-up of natural gas, or synthetic natural gas, C10L3/10; separation of difficult-to-condense gases or air by liquefaction F25J; for investigating materials G01N30/00) · CPC title

• C10G2300/202

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

• C10G53/12

  including at least one alkaline treatment step · CPC title

• C10G19/08 Primary

  Recovery of used refining agents · CPC title

• C10G2300/104

  Light gasoline having a boiling range of about 20 - 100 °C · CPC title