Unit for processing a liquid/gas phase mixture, mercaptan oxidation system including the same, and method of processing a liquid/gas phase mixture

Patent metadata

Field	Value
Publication number	US-9643146-B2
Application number	US-201314093155-A
Country	US
Kind code	B2
Filing date	Nov 29, 2013
Priority date	Nov 29, 2013
Publication date	May 9, 2017
Grant date	May 9, 2017

Abstract

A unit for processing a liquid/gas phase mixture, a mercaptan oxidation apparatus, and a method of processing a liquid/gas phase mixture are provided. In an embodiment, a unit for processing a liquid/gas phase mixture includes a vessel that is adapted to receive the liquid/gas phase mixture and a distributor that is disposed in the vessel. The distributor is adapted for flow of the liquid/gas phase mixture into the vessel, and the distributor includes a first outlet pipe that is horizontally disposed within the vessel. The first outlet pipe includes top orifices and bottom orifices that are spaced along the first outlet pipe, and the first outlet pipe is in fluid communication with the vessel through the top orifices and the bottom orifices. The top orifices have a smaller cross-sectional area than the bottom orifices.

First claim

What is claimed is:

1. A unit for processing a liquid/gas phase mixture, wherein the unit comprises:
a vessel adapted to receive the liquid/gas phase mixture; and
a distributor disposed in the vessel, wherein the distributor is adapted for flow of the liquid/gas phase mixture into the vessel, and wherein the distributor comprises a first outlet pipe horizontally disposed within the vessel, wherein the first outlet pipe comprises top orifices and bottom orifices spaced therealong with the first outlet pipe in fluid communication with the vessel through the top orifices and the bottom orifices, and wherein the top orifices have a smaller cross-sectional area than the bottom orifices and the top orifices and the bottom orifices are configured to balance a pressure differential across the respective orifices to a ΔP up to 10 KPa.

2. The unit of claim 1 , wherein the distributor further comprises a header extending into the vessel and in fluid communication with the first outlet pipe for conveying the liquid/gas phase mixture to the first outlet pipe.

3. The unit of claim 2 , wherein an additional outlet pipe is in fluid communication with the header separate from the first outlet pipe, wherein the additional outlet pipe also comprises top orifices and bottom orifices, and wherein the top orifices of the additional outlet pipe have a smaller cross-sectional area than the bottom orifices of additional outlet pipe.

4. The unit of claim 3 , wherein more than one additional outlet pipe is in fluid communication with the header.

5. The unit of claim 2 , wherein the header further comprises top orifices and bottom orifices, wherein the top orifices of the header have a smaller cross-sectional area than the bottom orifices of the header.

6. The unit of claim 5 , wherein top orifices and/or the bottom orifices of the header are spaced differently than the top orifices and/or the bottom orifices in the additional outlet pipe or the first outlet pipe.

7. The unit of claim 2 , wherein the first outlet pipe is configured to laterally extend across a cross section of the vessel, with the first outlet pipe disposed transverse to the header.

8. The unit of claim 1 , wherein the first outlet pipe is removably connected to the header through a pipe coupler.

9. The unit of claim 1 , wherein a ratio of cross-sectional areas of the bottom orifices to the top orifices is from about 5:1 to about 20:1.

10. The unit of claim 1 , wherein the top orifices are laterally offset from a vertical plane passing through a center of the first outlet pipe.

11. The unit of claim 10 , wherein the top orifices located on both sides of the vertical plane.

12. The unit of claim 1 , wherein a packing material is disposed in the vessel, and wherein the vessel is a fixed bed vessel.

13. A mercaptan oxidation apparatus comprising:
a mercaptan extraction unit adapted to receive a hydrocarbon stream comprising mercaptan and a caustic stream, and further adapted to mix the caustic stream and the hydrocarbon stream and produce a mercaptan-depleted stream and a first stream comprising a sulfur-containing component;
an oxidizer in fluid communication with the mercaptan extraction unit and configured to receive packing material therein, wherein the oxidizer is adapted to receive a liquid/gas phase mixture comprising air in the gas phase and the first stream in the liquid phase; and
a distributor disposed in the oxidizer, wherein the distributor is adapted for flow of the liquid/gas phase mixture into the oxidizer, and wherein the distributor comprises a first outlet pipe horizontally disposed within the oxidizer, wherein the first outlet pipe comprises top orifices and bottom orifices spaced therealong with the first outlet pipe in fluid communication with the oxidizer through the top orifices and the bottom orifices, and wherein the top orifices have a smaller cross-sectional area than the bottom orifices and the top orifices and the bottom orifices are configured to balance a pressure differential across the respective orifices to a ΔP up to 10 KPa.

Assignees

• Uop Llc

Inventors

• Tertel Jonathan Andrew
• Yuan Quan
• Addison Stephen R

Classifications

• B01J10/002 Primary

  carried out in foam, aerosol or bubbles · CPC title

• C10G19/02 Primary

  with aqueous alkaline solutions · CPC title

• B01J4/008

  Feed or outlet control devices · CPC title

• C10G2300/202

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

• B01J4/004

  Sparger-type elements · CPC title