IP Library Patent Application 13960384
Patent Application
App. No. 13/960,384

SYSTEM AND METHOD FOR CONTROLLING SCALE BUILD-UP IN A WFGD

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Quick Facts
Patent No.
US None
App. No.
13/960,384
Abstract

The present invention relates generally to the cleaning of a flue gas and, in one embodiment, to a device, system and method that mitigates and/or prevents slurry deposition at the flue inlet to a wet flue gas desulfurization (WFGD) unit in order to keep the inlet dry and minimize deposition (e.g., deposition scale) at the flue inlet to the WFGD tower. In one embodiment, a wet flue gas desulfurization (WFGD) unit, system and/or method according to the present invention comprises, among other features, a scale prevention system comprising a plenum air device and/or forced-air box located proximate the inlet transition zone. In another embodiment, a wet flue gas desulfurization (WFGD) unit, system and/or method according to the present invention comprises, among other features, a scale prevention system comprising at least one chill plate located proximate the inlet transition zone.

Claims (51)

1 . A scale prevention system for a wet flue gas desulfurization unit, the system comprising:

a flue structure, wherein the flue structure is connected to a flue inlet of a wet flue gas desulfurization unit;

at least two air nozzles, each air nozzle having a respective air supply line, wherein the at least two air nozzles are positioned on the interior of the flue structure so as to provide air coverage across the horizontal width of a flue inlet to the wet flue gas desulfurization unit; and

at least one inlet awning designed to deflect a slurry from the wet flue gas desulfurization unit, the at least one inlet awning being position above the flue inlet to the wet flue gas desulfurization unit.

2 . The system of claim 1 , wherein the flue structure has a rectangular or square cross-sectional shape and the at least two air nozzles are positioned on opposite interior walls of the flue.

3 . The system of claim 2 , wherein the at least two air nozzles are positioned on opposite vertical interior walls of the flue.

4 . The system of claim 1 , wherein the at least two air nozzles receive temperature controlled air that is within a range of about −25° F. to about +25° F. of the wet flue gas desulfurization unit slurry temperature.

5 . A scale prevention system for a wet flue gas desulfurization unit, the system comprising:

a flue structure, wherein the flue structure is connected to a flue inlet of a wet flue gas desulfurization unit and the flue structure has a cross-sectional shape selected from a rectangle or a square;

at least two air nozzles, each air nozzle having a respective air supply line, wherein at least one air nozzle is positioned on each opposite vertical interior wall of the flue structure so as to provide air coverage across the horizontal width of a flue inlet to the wet flue gas desulfurization unit; and

at least two lateral air nozzles, each lateral air nozzle having a respective air supply line, wherein each lateral air nozzle is positioned internally of each of the at least two air nozzles and are positioned at the top edge of the flue inlet to the wet flue gas desulfurization unit so as to provide air coverage across the horizontal width of the flue inlet to the wet flue gas desulfurization unit.

6 . The system of claim 5 , wherein the at least two lateral air nozzles are separated by a baffle plate.

7 . The system of claim 5 , wherein the system further comprises at least one inlet awning designed to deflect a slurry from the wet flue gas desulfurization unit, the at least one inlet awning being position above the flue inlet to the wet flue gas desulfurization unit.

8 . The system of claim 5 wherein the at least two air nozzles receive temperature controlled air that is within a range of about −25° F. to about +25° F. of the wet flue gas desulfurization unit slurry temperature.

9 . A scale prevention system for a wet flue gas desulfurization unit, the system comprising:

a flue structure, wherein the flue structure is connected to a flue inlet of a wet flue gas desulfurization unit; and

at least two chill plates, each chill plate having a respective supply line, wherein the at least two chill plates are positioned on the interior of the flue structure so as to provide temperature control across the horizontal width of a flue inlet to the wet flue gas desulfurization unit.

10 . The system of claim 9 , wherein each chill plate receives temperature controlled gas.

11 . The system of claim 9 , wherein each chill plate receives temperature controlled liquid.

12 . The system of claim 9 , wherein the at least two chill plates receive a temperature controlled gas that is within a range of about −25° F. to about +25° F. of the wet flue gas desulfurization unit slurry temperature.

13 . The system of claim 9 , wherein the at least two chill plates receive a temperature controlled liquid that is within a range of about −25° F. to about +25° F. of the wet flue gas desulfurization unit slurry temperature.

14 . The system of claim 9 , wherein the system further comprises at least one inlet awning designed to deflect a slurry from the wet flue gas desulfurization unit, the at least one inlet awning being position above the flue inlet to the wet flue gas desulfurization unit.

15 . The system of claim 9 , wherein the flue structure has a rectangular or square cross-sectional shape and at least one chill plate is positioned on each of the opposite vertical interior walls of the flue structure.

16 . The system of claim 9 , wherein the flue structure has a cross-sectional shape selected from a rectangle or a square and at least one chill plate is positioned on each of the opposite bottom interior corners of the flue structure.

17 . A scale prevention system for a wet flue gas desulfurization unit, the system comprising:

a flue structure, wherein the flue structure is connected to a flue inlet of a wet flue gas desulfurization unit;

at least two air nozzles, each air nozzle having a respective air supply line; and

at least two chill plates, each chill plate having a respective supply line,

wherein the combination of the at least two air nozzles and the at least two chill plates are positioned on the interior of the flue structure so as to provide temperature control across the horizontal width of a flue inlet to the wet flue gas desulfurization unit.

18 . The system of claim 17 , wherein the system further comprises at least one inlet awning designed to deflect a slurry from the wet flue gas desulfurization unit, the at least one inlet awning being position above the flue inlet to the wet flue gas desulfurization unit.

19 . The system of claim 17 , wherein the flue structure has a rectangular or square cross-sectional shape and the at least two air nozzles are positioned on opposite vertical interior walls of the flue.

20 . The system of claim 17 , wherein the flue structure has a rectangular or square cross-sectional shape and at least one chill plate is positioned on each of the opposite vertical interior walls of the flue structure.

21 . The system of claim 17 , wherein the flue structure has a cross-sectional shape selected from a rectangle or a square and at least one chill plate is positioned on each of the opposite bottom interior corners of the flue structure.

22 . The system of claim 17 , wherein the at least two air nozzles receive temperature controlled air that is within a range of about −25° F. to about +25° F. of the wet flue gas desulfurization unit slurry temperature.

23 . The system of claim 17 , wherein the at least two chill plates receive a temperature controlled gas that is within a range of about −25° F. to about +25° F. of the wet flue gas desulfurization unit slurry temperature.

24 . The system of claim 17 , wherein the at least two chill plates receive a temperature controlled liquid that is within a range of about −25° F. to about +25° F. of the wet flue gas desulfurization unit slurry temperature.

25 . A scale prevention system for a wet flue gas desulfurization unit, the system comprising:

a flue structure, wherein the flue structure is connected to a flue inlet of a wet flue gas desulfurization unit;

at least two air nozzles, each air nozzle having a respective air supply line, wherein at least one air nozzle is positioned on each opposite vertical interior wall of the flue;

at least two lateral air nozzles, each lateral air nozzle having a respective air supply line, wherein each lateral air nozzle is positioned internally of each of the at least two air nozzles and are positioned at the top edge of the flue inlet to the wet flue gas desulfurization unit; and

at least two chill plates, each chill plate having a respective supply line, wherein the at least two chill plates are positioned on the interior of the flue,

wherein the combination of the at least two air nozzles, the at least two lateral air nozzles and the at least two chill plates are positioned on the internal surfaces of the flue structure so as to provide temperature control across the horizontal width of a flue inlet to the wet flue gas desulfurization unit.

26 . The system of claim 25 , wherein the at least two lateral air nozzles are separated by a baffle plate.

27 . The system of claim 25 , wherein the system further comprises at least one inlet awning designed to deflect a slurry from the wet flue gas desulfurization unit, the at least one inlet awning being position above the flue inlet to the wet flue gas desulfurization unit.

28 . The system of claim 25 , wherein the flue structure has a rectangular or square cross-sectional shape and the at least two air nozzles are positioned on opposite vertical interior walls of the flue.

29 . The system of claim 25 , wherein the at least two lateral air nozzles are separated by a baffle plate.

30 . The system of claim 25 , wherein the flue structure has a rectangular or square cross-sectional shape and at least one chill plate is positioned on each of the opposite vertical interior walls of the flue structure.

31 . The system of claim 25 , wherein the flue structure has a cross-sectional shape selected from a rectangle or a square and at least one chill plate is positioned on each of the opposite bottom interior corners of the flue structure.

32 . The system of claim 25 , wherein the at least two air nozzles receive temperature controlled air that is within a range of about −25° F. to about +25° F. of the wet flue gas desulfurization unit slurry temperature.

33 . The system of claim 25 , wherein the at least two chill plates receive a temperature controlled gas that is within a range of about −25° F. to about +25° F. of the wet flue gas desulfurization unit slurry temperature.

34 . The system of claim 25 , wherein the at least two chill plates receive a temperature controlled liquid that is within a range of about −25° F. to about +25° F. of the wet flue gas desulfurization unit slurry temperature.

Assignments (5)
RELEASE OF SECURITY INTEREST Recorded Jul 1, 2021
From: BANK OF AMERICA, N.A.
To: DIAMOND POWER INTERNATIONAL, LLC (F/K/A DIAMOND POWER INTERNATIONAL, INC.); MEGTEC TURBOSONIC TECHNOLOGIES, INC.; THE BABCOCK & WILCOX COMPANY (F/K/A BABCOCK & WILCOX POWER GENERATION GROUP, INC.); BABCOCK & WILCOX SPIG, INC.; BABCOCK & WILCOX TECHNOLOGY, LLC (F/K/A MCDERMOTT TECHNOLOGY, INC.); SOFCO-EFS HOLDINGS LLC; BABCOCK & WILCOX MEGTEC, LLC
Reel/Frame 057337/0823 →
CHANGE OF NAME Recorded Sep 24, 2015
From: BABCOCK & WILCOX POWER GENERATION GROUP, INC.
To: THE BABCOCK & WILCOX COMPANY
Reel/Frame 036675/0434 →
SECURITY INTEREST Recorded Jul 28, 2015
From: BABCOCK & WILCOX POWER GENERATION GROUP, INC. (TO BE RENAMED THE BABCOCK AND WILCOX COMPANY)
To: BANK OF AMERICA, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 036201/0598 →
SECURITY INTEREST Recorded May 22, 2014
From: BABCOCK & WILCOX POWER GENERATION GROUP, INC.
To: BANK OF AMERICA, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 032983/0122 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 27, 2013
From: JOHNSON, DANIEL B
To: BABCOCK & WILCOX POWER GENERATION GROUP, INC.
Reel/Frame 031086/0915 →