Processes for removing entrained particulates from a gas

Patent metadata

Field	Value
Publication number	US-9393512-B2
Application number	US-201414262348-A
Country	US
Kind code	B2
Filing date	Apr 25, 2014
Priority date	Apr 25, 2014
Publication date	Jul 19, 2016
Grant date	Jul 19, 2016

Abstract

In a process for removing entrained particulates from a gas, a chemical reaction may be conducted in a vessel. Conducting the chemical reaction may include suspending particulates in a gas in a fluidized bed in the vessel. A portion of the gas and entrained particulates may be directed to a filter medium and the entrained particulates may be filtered from the gas. Filtering the entrained particulates may include directing the gas from a feed side of the filter medium through the filter medium to a filtrate side of the filter medium and may also include directing at least a portion of the entrained particulates generally tangentially along the feed side of the filter medium to scour the feed side of the filter medium. The particulates may then be directed from the feed side of the filter medium into a dip leg.

First claim

The invention claimed is:

1. A process for removing entrained particulates from a gas comprising:
conducting a chemical reaction in a vessel, including suspending particulates in a gas in a fluidized bed in the vessel;
directing a portion of the gas and entrained particulates to a permeable filter medium in the vessel;
filtering a substantial portion of the entrained particulates from the gas within the vessel, including directing the gas from a feed side of the filter medium through the filter medium to a filtrate side of the filter medium in the vessel and directing at least a portion of the entrained particulates generally tangentially along the feed side of the filter medium to scour the feed side of the filter medium in the vessel; and
directing the particulates from the feed side of the filter medium into a dip leg in the vessel, the process further comprising discharging the filtered gas from the vessel.

2. The process of claim 1 further comprising passing the particulates from the dip leg to the fluidized bed in the vessel.

3. The process of claim 1 wherein directing the gas through the filter medium includes directing the gas radially through a plurality of hollow, elongate, filter tubes, each filter tube including a filter medium, and wherein directing at least a portion of the entrained particulates along the feed side of the filter medium includes directing entrained particulates generally axially along the feed sides of the filter tubes.

4. The process of claim 3 wherein directing gas radially through a plurality of filter tubes includes directing the gas radially inside-out through the filter tubes, wherein directing the entrained particulates generally axially along the feed sides of the filter tubes includes directing the entrained particulates generally downwardly along the feed sides within the filter tubes from an inlet end to an outlet end of each tube, and wherein directing the particulates into a dip leg includes directing the particulates from the outlet end of each filter tube into the dip leg below the filter tubes.

5. The process of claim 1 wherein directing a portion of the gas and entrained particulates to the feed side of the filter medium includes increasing the velocity of the gas and entrained particulates and then directing the higher velocity gas and entrained particulates to the feed side of the filter medium.

6. The process of claim 1 wherein directing at least a portion of the particulates generally tangentially along the feed side of the filter medium includes diverting the particulates against the feed side of the filter medium.

7. A process for removing catalyst particulates from a gas comprising:
regenerating catalyst particulates, including suspending catalyst particulates in a hot gas in a fluidized bed in a regenerator vessel;
directing a portion of the gas and entrained catalyst particulates to a feed side of a permeable filter medium in the regenerator vessel;
filtering the entrained catalyst particulates from the gas in the regenerator vessel, including directing the gas from the feed side of the filter medium through the filter medium to a filtrate side of the filter medium and directing at least a portion of the entrained catalyst particulates generally tangentially along the feed side of the filter medium to scour the feed side of the filter medium;
discharging the filtered gas from the regenerator vessel; and
directing the catalyst particulates from the feed side of the filter medium into a dip leg in the regenerator vessel.

8. The process of claim 7 further comprising passing the catalyst particulates from the dip leg into the fluidized bed in the regenerator vessel.

9. The process of claim 7 wherein directing the gas through the filter medium includes directing the gas radially through a plurality of hollow, elongate, filter tubes, each filter tube including a filter medium, and wherein directing at least a portion of the entrained catalyst particulates along the feed side of the filter medium includes directing entrained catalyst particulates generally axially along the feed sides of the filter tubes.

10. The process of claim 9 wherein directing gas radially through a plurality of filter tubes includes directing the gas radially inside-out through the filter tubes, wherein directing the entrained catalyst particulates generally axially along the feed sides of the filter tubes includes directing the entrained particulates generally downwardly along the feed sides within the filter tubes from an inlet end to an outlet end of each tube, and wherein directing the catalyst particulates into a dip leg includes directing the particulates from the outlet end of each filter tube into the dip leg below the filter tubes.

Assignees

• Pall Corp

Inventors

• Schuttenberg Kurt R

Classifications

• B04C3/06

  Construction of inlets or outlets to the vortex chamber · CPC title

• B01D46/005 Primary

  Crossflow filtration, i.e. having an inlet and two outlets · CPC title

• B01D45/16

  generated by the winding course of the gas stream {, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes} · CPC title

• B01D45/12

  by centrifugal forces (centrifuges B04B; cyclones B04C) · CPC title

• B01D46/0042 Primary

  Use of the inlet flow in order to clean the filter surface · CPC title