Sulfide oxidation process and apparatus

Patent metadata

Field	Value
Publication number	US-2017014751-A1
Application number	US-201615210510-A
Country	US
Kind code	A1
Filing date	Jul 14, 2016
Priority date	Jul 17, 2015
Publication date	Jan 19, 2017
Grant date	—

Abstract

A separation zone and a method of separating a mixed stream are described. The separation zone includes a tank and a stack having a gas outlet. A first baffle is positioned between the sides and defines a disulfide liquid compartment. The stack is positioned above the disulfide liquid compartment. A second baffle is positioned between the first baffle and the second side and defines an alkali compartment. The second baffle has a height less than the height of the first baffle. A third baffle is positioned between the first and second baffles. The bottom of the third baffle is at a height less than the height of the second baffle, and the top of the third baffle is at a height greater than the height of the first baffle.

First claim

1 . A separation zone comprising:
a tank having an inlet, a disulfide liquid outlet, an alkali liquid outlet, and a stack having a gas outlet, the tank having front and back sides and first and second sides a first baffle extending upward from the bottom of the tank and having a first height, the first baffle positioned between the first and second sides and extending from the front side to the back side, a space between the first side and the first baffle defining a disulfide liquid compartment, the stack being positioned above the disulfide liquid compartment; a second baffle extending upward from the bottom of the tank and having a second height less than the first height, the second baffle positioned between the first baffle and the second side and extending from the front side to the back side, a space between the second baffle and the second side defining an alkali compartment; and a third baffle spaced apart from the bottom of the tank, the third baffle positioned between the first and second baffles and extending from the front side to the back side, the bottom of the third baffle being at a height less than the second height, the top of the third baffle being at a height greater than the first height.

2 . The separation zone of claim 1 further comprising a coalescing medium positioned between the first and third baffles.

3 . The separation zone of claim 2 wherein the top of the coalescing medium is at a height greater than the first height.

4 . The separation zone of claim 2 wherein the coalescing medium comprises a material having oleophilic properties.

5 . The separation zone of claim 1 further comprising a disulfide scrubber in the stack.

6 . The separation zone of claim 1 further comprising an absorbent zone downstream of the gas outlet.

7 . The separation zone of claim 1 wherein the disulfide liquid outlet is positioned in the disulfide liquid compartment at a level lower than the first height.

8 . The separation zone of claim 1 wherein the alkali liquid outlet is positioned in the alkali compartment at a level lower than the second height.

9 . A method of separating a mixed stream comprising a rich alkali liquid, liquid disulfide compounds, and rich air, the method comprising:
introducing the mixed stream into a separation zone comprising:
a tank having an inlet, a disulfide liquid outlet, an alkali liquid outlet, and a stack having a gas outlet, the tank having front and back sides and first and second sides;
a first baffle extending upward from the bottom of the tank and having a first height, the first baffle positioned between the first and second sides and extending from the front side to the back side, a space between the first side and the first baffle defining a disulfide liquid compartment, the stack being positioned above the disulfide liquid compartment;
a second baffle extending upward from the bottom of the tank and having a second height less than the first height, the second baffle positioned between the first baffle and the second side and extending from the front side to the back side, a space between the second baffle and the second side defining an alkali compartment; and
a third baffle spaced apart from the bottom of the tank, the third baffle positioned between the first and second baffles and extending from the front side to the back side, the bottom of the third baffle being at a height less than the second height, the top of the third baffle being at a height greater than the first height; separating the mixed stream into a liquid phase comprising the liquid disulfide compounds and the rich alkali liquid and a gas phase comprising the rich air and disulfide compound vapors, the liquid disulfide compounds forming a layer on the rich alkali liquid; passing the liquid disulfide compounds over the first baffle into the disulfide liquid compartment and out through the disulfide liquid outlet; passing the rich alkali liquid under the third barrier, and over the second barrier into the alkali compartment, and out through the alkali liquid outlet.

10 . The method of claim 9 wherein the separation zone further comprises a coalescing medium positioned between the first and third baffles, and further comprising:
passing the rich alkali liquid through the coalescing medium before passing the rich alkali liquid under the third baffle.

11 . The method of claim 10 wherein the top of the coalescing medium is at a height greater than the first height.

12 . The method of claim 10 wherein the coalescing medium comprises a material having oleophilic properties.

13 . The method of claim 9 wherein the separation zone further comprises a disulfide scrubber in the stack, and further comprising:
passing the gas phase through the disulfide scrubber to remove the disulfide compound vapors.

14 . The method of claim 13 further comprising:
introducing a wash oil into the disulfide scrubber, the disulfide compounds being transferred to the wash oil; and
collecting the wash oil containing the disulfide compounds in the disulfide liquid compartment.

15 . The method of claim 9 wherein the separation zone further comprises an absorbent zone downstream of the gas outlet; and further comprising:
passing the gas phase through the absorbent zone to remove the disulfide compound vapors.

16 . The method of claim 9 wherein the gas phase alternately passes through a first absorbent bed and a second absorbent bed.

17 . The method of claim 9 wherein the disulfide liquid outlet is positioned in the disulfide liquid compartment at a level lower than the first height.

18 . The method of claim 9 wherein the alkali liquid outlet is positioned in the alkali compartment at a level lower than the second height.

19 . The method of claim 9 wherein the gas phase further comprises hydrocarbon vapors, and further comprising removing the hydrocarbon vapors in the absorbent zone.

20 . A method of separating a mixed stream comprising a rich alkali liquid, liquid disulfide compounds, and rich air, the method comprising:
introducing the mixed stream into a separation zone comprising:
a tank having an inlet, a disulfide liquid outlet, an alkali liquid outlet, and a stack having a gas outlet, the tank having front and back sides and first and second sides;
a first baffle extending upward from the bottom of the tank and having a first height, the first baffle positioned between the first and second sides and extending from the front side to the back side, a space between the first side and the first baffle defining a disulfide liquid compartment, the stack being positioned above the disulfide liquid compartment;
a second baffle extending upward from the bottom of the tank and having a second height less than the first height, the second baffle positioned between the first baffle and the second side and extending from the front side to the back side, a space between the second baffle and the second side defining an alkali compartment;
a third baffle spaced apart from the bottom of the tank, the third baffle positioned between the first and second baffles and extending from the front side to the back side, the bottom of the third baffle being at a height less than the second height, the top of the third baffle being at a height greater than the first height; and
an absorbent zone downstream of the gas outlet;
separating the mixed stream into a liquid phase comprising the liquid disulfide compounds and the rich alkali liquid and a gas phase comprising the rich air and disulfide comp

Assignees

• Uop Llc

Inventors

• Laricchia Luigi

Classifications

• B01D53/04

  with stationary adsorbents {(B01D53/025 takes precedence)} · CPC title

• B01D17/0211 Primary

  with baffles · CPC title

• B01D2257/306

  Organic sulfur compounds, e.g. mercaptans · CPC title

• B01D2259/402

  using two beds · CPC title

• B01D2259/40084

  by exchanging used adsorbents with fresh adsorbents · CPC title