Dust separator useful with dry scrubber system

Patent metadata

Field	Value
Publication number	US-9643117-B2
Application number	US-201514869113-A
Country	US
Kind code	B2
Filing date	Sep 29, 2015
Priority date	Oct 3, 2014
Publication date	May 9, 2017
Grant date	May 9, 2017

Abstract

An air quality control system (AQCS) 14 useful for treating flue gas FG, such as flue gas FG produced by a fossil fuel fired boiler 12 is described. The AQCS 14 is equipped with a dust separator 37 . The dust separator 37 is useful under relatively high dust load conditions downstream from a dry scrubber reactor 36 with limited equipment wear and limited space requirements. As such, the dust separator captures particulate matter with a dust trap that intercepts the flow of particulate matter for collection of the particulate matter in a hopper.

First claim

The invention claimed is:

1. An air quality control system for treating flue gas produced in a combustion process to produce cleaned flue gas comprising:
a dry scrubber reactor with a distribution device therein for dispersal of a moistened reducing agent in a flue gas flowing through the dry scrubber reactor;
a dust separator comprising a dust separator housing with a dust trap connected to the dry scrubber reactor for capture of flue gas particulate matter flowing through the dust separator housing, with relatively small sized particulate matter intercepted by opposed angled arms of the dust trap and relatively large sized particulate matter intercepted by a plate of the dust trap; and
a particulate removal device connected to the dust separator for capture of particulate matter from the flue gas flowing through the particulate removal device to produce a treated flue gas for release through a stack.

2. The system of claim 1 , wherein the dust separator captures particulate matter flowing around an axis perpendicular to flue gas flow through the dry scrubber reactor creating inertia wherein the relatively small sized particulate matter of relatively low inertia flow along a curved inner wall of the dust separator housing and the relatively large sized particulate matter of relatively high inertia flow along an interior surface of dust separator housing.

3. The system of claim 1 , wherein the dust separator captures particulate matter with the dust trap arranged within the dust separator housing by capturing relatively small sized particulate matter with the opposed angled arms of the dust trap for flow through connected chutes into a hopper and by capturing relatively large sized particulate matter with the plate of the dust trap for flow from the plate or beneath the plate into the hopper.

4. The system of claim 1 , wherein the dust separator captures particulate matter with the dust trap intercepting the particulate matter for collection of the particulate matter in a hopper prior to particulate matter flow into the distribution device.

5. The system of claim 1 , wherein flue gas exits the dust separator housing by horizontal flow through a flue gas outlet.

6. A dust separator for use in treating flue gas produced in a combustion process to produce cleaned flue gas comprising:
a dust separator housing with a dust trap, fluidly connected to a dry scrubber reactor comprising a distribution device for dispersal of a moistened reducing agent from the distribution device into the flue gas flowing through the dry scrubber reactor, for dust separator capture of particulate matter from the flue gas flowing from the dry scrubber reactor through the dust separator housing, with relatively small sized particulate matter intercepted by opposed angled arms of the dust trap and relatively large sized particulate matter intercepted by a plate of the dust trap.

7. The dust separator of claim 6 , wherein the dust separator housing captures particulate matter flowing around an axis perpendicular to flue gas flow through the dry scrubber reactor creating inertia wherein the relatively small sized particulate matter of relatively low inertia flow along a curved inner wall of the dust separator housing and the relatively large sized particulate matter of relatively high inertia flow along an interior surface of dust separator housing.

8. The dust separator of claim 6 , wherein the dust separator housing captures particulate matter with the dust trap arranged within an interior area of the dust separator housing by capturing relatively small sized particulate matter with the opposed angled arms of the dust trap for flow through connected chutes into a hopper and by capturing relatively large sized particulate matter with the plate of the dust trap for flow from the plate or beneath the plate into the hopper.

9. The dust separator of claim 6 , wherein the dust separator housing captures particulate matter flowing through the dust separator housing with the dust trap intercepting the particulate matter for collection of the particulate matter in a hopper prior to particulate matter flow into the distribution device.

10. The dust separator of claim 6 , wherein flue gas exits the dust separator housing by horizontal flow through a flue gas outlet.

11. A method of using an air quality control system for treating flue gas produced in a combustion process to produce cleaned flue gas comprising:
dispersing using a distribution device a moistened reducing agent into a flue gas flowing through a dry scrubber reactor;
capturing particulate matter from the flue gas using a dust separator connected to the dry scrubber reactor, the dust separator comprising a dust separator housing and a dust trap for relatively small sized particulate matter interception by opposed angled arms of the dust trap and relatively large sized particulate matter interception by a plate of the dust trap; and
producing treated flue gas for release through a stack by capturing particulate matter from the flue gas using a particulate removal device connected to the dust separator.

12. The method of claim 11 , wherein the dust separator captures particulate matter flowing around an axis perpendicular to flue gas flow through the dry scrubber reactor creating inertia wherein the relatively small sized particulate matter of relatively low inertia flow along a curved inner wall of the dust separator housing and the relatively large sized particulate matter of relatively high inertia flow along an interior surface of the dust separator housing.

13. The method of claim 11 , wherein the dust separator captures particulate matter with the dust trap arranged within an interior area of the dust separator housing by capturing relatively small sized particulate matter with the opposed angled arms of the dust trap for flow through connected chutes into a hopper and by capturing relatively large sized particulate matter with the plate of the dust trap for flow from the plate or beneath the plate into the hopper.

14. The method of claim 11 , wherein the dust separator captures particulate matter with the dust trap intercepting the particulate matter for collection of the particulate matter in a hopper prior to particulate matter flow into the distribution device.

15. The method of claim 11 , wherein flue gas exits the dust separator housing by horizontal flow through a flue gas outlet.

Assignees

• Alstom Technology Ltd
• General Electric Technology Gmbh

Inventors

• Råhlin Robert
• Tabikh Ali Mustapha

Classifications

• B01D53/508

  by treating the gases with solids · CPC title

• B01D53/80

  Semi-solid phase processes, i.e. by using slurries · CPC title

• B01D53/504

  characterised by a specific device · CPC title

• B01D53/75

  Multi-step processes · CPC title

• B01D45/12

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