Trim alkali metal desulfurization of refinery fractions

Patent metadata

Field	Value
Publication number	US-10494577-B2
Application number	US-201715815923-A
Country	US
Kind code	B2
Filing date	Nov 17, 2017
Priority date	Dec 19, 2016
Publication date	Dec 3, 2019
Grant date	Dec 3, 2019

Abstract

Systems and methods are provided for upgrading aromatic refinery fractions by performing trim alkali metal desulfurization. The alkali metal desulfurization can be performed by mixing the aromatic refinery fraction with alkali metal in finely dispersed solid and/or molten form, such as molten sodium. The aromatic nature of the refinery fraction can potentially be beneficial for the desulfurization reaction mechanism. The aromatic refinery fractions can correspond to fractions that have been previously processed to remove metals. Because only trim desulfurization is being performed, the desulfurization can be performed under relatively mild alkali metal desulfurization conditions that result in a reduced or minimized amount of feed conversion.

First claim

The invention claimed is:

1. A method for desulfurizing a feedstock, comprising:
exposing a feedstock to conversion conditions to form a conversion effluent, wherein the conversion effluent comprises a hydroprocessed effluent, the conversion conditions comprising hydrotreating conditions, demetallization conditions, or a combination thereof in the presence of at least one catalyst having a median pore diameter of at least 100 Angstroms, the hydrotreating conditions optionally comprising conditions effective for conversion of at least 50 wt % of the feedstock relative to 370° C.;
separating the conversion effluent to form at least a first converted fraction comprising at least 30 wt % aromatics, a sulfur content of 0.5 wt % to 3.5 wt %, a content of Ni, V, and Fe of 10 wppm or less, and a T5 distillation point of at least 230° C.;
contacting at least a portion of the first converted fraction with alkali metal in the presence of H 2 -containing gas to form a converted mixture comprising alkali metal salt, the converted mixture comprising a molar ratio of alkali metal to sulfur of 0.5 to 5.0;
separating the converted mixture to form a desulfurized converted fraction comprising a sulfur content of 0.05 wt % to 0.5 wt % and at least one alkali metal salt-containing fraction comprising at least 50 mol % of the alkali metal in the converted mixture; and
regenerating at least a portion of the alkali metal in the alkali metal salt-containing fraction to elemental alkali metal.

2. The method of claim 1 , wherein the alkali metal comprises sodium.

3. The method of claim 1 , wherein the contacting at least a portion of the first converted fraction with alkali metal in the presence of H 2 -containing gas comprises an H 2 -containing treat gas rate of about 15 Nm 3 /m 3 to about 200 Nm 3 /m 3 .

4. The method of claim 1 , wherein contacting the first converted fraction with alkali metal comprises contacting the first converted fraction with regenerated alkali metal.

5. The method of claim 1 , wherein contacting the first converted fraction with alkali metal comprises converting less than 30 wt % of the first converted fraction relative to a conversion temperature of 566° C.; or wherein contacting the first converted fraction with alkali metal comprises converting less than 10 wt % of the first converted fraction relative to a conversion temperature of 370° C.; or a combination thereof.

6. The method of claim 1 , wherein the feedstock comprises at least 10 wppm of Ni, V, and Fe.

7. The method of claim 1 , wherein the desulfurized converted fraction comprises a sulfur content of 0.1 wt % to 0.5 wt %, or wherein the desulfurized converted fraction comprises a sulfur content of 0.05 wt % to 0.1 wt %.

8. The method of claim 1 , wherein the converted mixture comprises a molar ratio of alkali metal to sulfur of 0.5 to 2.0.

9. The method of claim 1 , wherein the contacting at least a portion of the first converted fraction with alkali metal to form a converted mixture comprising alkali metal salt is performed during the separating the conversion effluent to form the first converted fraction.

10. The method of claim 1 , wherein regenerating at least a portion of the alkali metal in the alkali metal salt-containing fraction comprises:
exposing at least one of the converted mixture and the at least one alkali metal salt-containing fraction to H 2 S to convert at least a portion of alkali metal compounds to alkali metal hydrosulfide;
converting at least a portion of the alkali metal hydrosulfide to alkali metal polysulfide having a first stoichiometry by mixing the alkali metal hydrosulfide with alkali metal polysulfide having a second stoichiometry;
performing electrolysis on the alkali metal polysulfide having the first stoichiometry in the presence of a membrane to form modified alkali metal polysulfide having a third stoichiometry and a membrane permeate comprising alkali metal; and
heating at least a portion of the modified alkali metal polysulfide having the third stoichiometry to form sulfur and alkali metal polysulfide having the second stoichiometry.

11. The method of claim 10 , wherein the membrane comprises a NASICON membrane.

Assignees

• Exxonmobil Res & Eng Co

Inventors

• Hanks Patrick L

Classifications

• C10G2300/202

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

• C10G65/04

  including only refining steps · CPC title

• C10G2300/1096

  Aromatics or polyaromatics · CPC title

• C10G2300/207

  Acid gases, e.g. H2S, COS, SO2, HCN · CPC title

• C10G2300/308

  Gravity, density, e.g. API · CPC title