IP Library Granted Patent US 9,423,122
Granted Patent B2
US 9,423,122 · App. 13/976,065 · Granted Aug 23, 2016

Circulating fluidized bed boiler having two external heat exchangers for hot solids flow

Inventors: Kari Kauppinen (Varkaus, FI); Pertti Kinnunen (Varkaus, FI)
Assignee: AMEC FOSTER WHEELER ENERGIA OY
F22B31/003F22B31/0092F22D1/02F23C10/04F23C10/26F23C10/32F23C10/10
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Quick Facts
Patent No.
US 9,423,122
App. No.
13/976,065
Granted
Aug 23, 2016
Kind
B2
Abstract

A circulating fluidized bed boiler includes a furnace for combusting solid carbonaceous fuel in a fast fluidized bed. A solids separator is adjacent to a sidewall of the furnace and separates solids entrained with exhaust gas discharged via an outlet channel. A gas seal conveys at least a portion of the separated solids to a first fluidized bed heat exchange chamber that is arranged downstream of the gas seal and has internal heat exchange surfaces. A first lift channel has a lower end connected to a bottom portion of the first fluidized bed heat exchange chamber and an upper end connected to an upper end of a first return channel for discharging solids from the first fluidized bed heat exchange chamber and taking the cooled solids to a lower portion of the furnace. A second fluidized bed heat exchange chamber is arranged adjacent to a lower sidewall of the furnace.

Claims (16)

1. A circulating fluidized bed boiler comprising:

a furnace for combusting solid carbonaceous fuel in a fast fluidized bed, the furnace having (i) walls made of water/steam tube panels and used for evaporating water fed therein and (ii) an outlet channel for exhaust gas at an upper portion of the furnace;

a solids separator arranged adjacent to a sidewall of the furnace for separating solids entrained with exhaust gas discharged via the outlet channel from the upper portion of the furnace;

a gas seal for receiving at least a portion of the separated solids from the solids separator;

a first fluidized bed heat exchange chamber that is arranged downstream of the gas seal and has internal heat exchange surfaces, the first fluidized bed heat exchange chamber receiving the at least a portion of the separated solids from the solids separator via the gas seal;

at least one return channel connecting the first fluidized bed heat exchange chamber to the furnace, so that solids discharged from the first fluidized bed heat exchange chamber are only conveyed to a lower portion of the furnace via the at least one return channel;

a first lift channel having a lower end connected to a bottom portion of the first fluidized bed heat exchange chamber and an upper end connected to an upper end of a first the at least one return channel for discharging solids from the first fluidized bed heat exchange chamber to the at least one return channel;

a second fluidized bed heat exchange chamber being (i) arranged adjacent to a lower sidewall of the furnace and having internal heat exchange surfaces, (ii) positioned below the first fluidized bed heat exchange chamber, and (iii) narrower than the first fluidized bed heat exchanger;

a singular inlet channel for introducing hot solids from the furnace into the second fluidized bed heat exchange chamber, the singular inlet channel directly connecting the lower portion of the furnace to the second fluidized bed heat exchange chamber so that the second fluidized bed heat exchange chamber receives hot solids only directly from the lower portion of the furnace via the singular inlet channel; and

a second lift channel having a lower end connected to a bottom portion of the second fluidized bed heat exchange chamber and an upper end connected to the furnace for discharging solids from the second fluidized bed heat exchange chamber to the lower portion of the furnace,

wherein the first fluidized bed heat exchange chamber has two first lift channels and two return channels arranged at the lateral sides thereof such that the second fluidized bed heat exchange chamber is situated between the lower ends of the two return channels.

2. The circulating fluidized bed boiler according to claim 1 , further comprising at least one of a fuel feed, a bed material feed, a secondary gas feed, and a start up burner positioned between the first return channel and the second fluidized bed heat exchange chamber.

3. The circulating fluidized bed boiler according to claim 1 , wherein the first of the two return channels includes a receiver for receiving fuel to be introduced into the lower portion of the furnace.

4. The circulating fluidized bed boiler according to claim 1 , wherein the walls of each of the first and second fluidized bed heat exchange chambers are made of water tube panels.

5. The circulating fluidized bed boiler according to claim 4 , wherein the first of the two return channels has walls made of water tube panels.

6. The circulating fluidized bed boiler according to claim 4 , wherein the walls of at least one of the first fluidized bed heat exchange chamber, the second fluidized bed heat exchange chamber, and the first return channel are used for heating water to be introduced into the water/steam tube panels of the furnace.

Assignments (2)
CHANGE OF NAME Recorded May 11, 2015
From: FOSTER WHEELER ENERGIA OY
To: AMEC FOSTER WHEELER ENERGIA OY
Reel/Frame 035625/0912 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 8, 2013
From: KAUPPINEN, KARI; KINNUNEN, PERTTI
To: FOSTER WHEELER ENERGIA OY
Reel/Frame 030811/0941 →
Priority Claims (1)
FI 20115181 · Feb 24, 2011 · national
Continuity (1)
Related Publication 20130284120A1 · Oct 31, 2013