Coal burning arrangement

Claim 2

Coal burning apparatus which comprises, in combination: a spouted fluidized bed pyrolyzer, a fluidized bed combustor, a first cyclone, a second cyclone, and an afterburner, means for introducing pulverized coal and sorbent into said pyrolyzer, means for transferring char and sorbent from said pyrolyzer to said combustor, means for transferring gaseous materials with entrained particulate material from said pyrolyzer to said first cyclone, means for transferring gaseous materials from said first cyclone to said afterburner, means for introducing a combustion supporting gas into said combustor in quantity sufficient to maintain a temperature of combustion products below the fusion temperature of ash from the char, means for transferring gaseous materials with entrained particulate material from said combustor to said second cyclone, and means for transferring gaseous materials from said second cyclone to said afterburner.

Claim 3

The apparatus of claim 1 in which said fluidizedbed combustor is of fast, solids-recirculating, character.

Claim 4

Coal burning apparatus which comprises, in combination: a spouted fluidized bed pyrolyzer, a fluidized bed combustor, a first cyclone, a second cyclone, and an afterburner, the pyrolyzer being connected to accept pulverized coal and to discharge char to the combustor and gaseous materials with entrained particulate material to the first cyclone. the first cyclone being connected to deliver gases to the afterburner, the combustor being connected to accept also a combustion supporting gas and to deliver to the second cyclone gaseous materials with entrained particulate material, and the second cyclone being connected to deliver gaseous material to the afterburner, said pyrolyzer comprises a lower entrance passage progressively changing in direction from transverse to longitudinal, a cylindrical chamber portion defined by a line rotated about the longitudinal axis of said pyrolyzer, a conical transition portion between said entrance passage and said cylindrical chamber portion, an outlet passage of smaller diameter than said cylindrical chamber portion above said cylindrical chamber portion, a deflector positioned in said cylindrical chamber portion to bar flow directly along a parallel to said longitudinal axis from the lower portion of said cylindrical chamber portion into said outlet passage, and a standpipe emerging from said cylindrical chamber portion upstream of said deflector.

Claim 5

Coal burning apparatus which comprises, in combination: a spouted fluidized bed pyrolyzer, a fluidized bed combustor, a first cyclone, a second cyclone, and an afterburner, the pyrolyzer being connected to accept pulverized coal and to discharge char to the combustor and gaseous materials with entrained particulate material to the first cyclone. the first cyclone being connected to deliver gases to the afterburner, the combustor being connected to accept also a combustion supporting gas and to deliver to the second cyclone gaseous materials with entrained particulate material, and the second cyclone being connected to deliver gaseous material to the afterburner, said pyrolyzer comprises a lower entrance passage progressively changing in direction from transverse to longitudinal, a cylindrical chamber portion defined by a line rotated about the longitudinal axis of said pyrolyzer, a conical transition portion between said entrance passage and said cylindrical chamber portion, an outlet passage of smaller diameter than said cylindrical chamber portion above said cylindrical chamber portion, a deflector positioned in said cylindrical chamber portion to bar flow directly along a parallel to said longitudinal axis from the lower portion of said cylindrical chamber portion into said outlet passage, and a standpipe emerging from said cylindrical chamber portion upstream of said deflector.

Claim 6

Coal burning apparatus which comprises, in combination: a spouted fluidized bed pyrolyzer, a fluidized bed combustor, a first cyclone, a second cyclone, and an afterburner, the pyrolyzer being connected to accept pulverized coal and to discharge char to the combustor and gaseous materials with entrained particulate material to the first cyclone, the first cyclone being connected to deliver gases to the afterburner, the combustor being connected to accept also a combustion supporting gas and to deliver to the second cyclone gaseous materials with entrained particulate material, and the second cyclone being connected to deliver gaseous material to the afterburner, said fluidized-bed combustor being of fast, solids-recirculating character and said combustor includes a central recirculation chamber defined by a first portion cylindrical about the combustor longitudinal axis and a generally conical portion, an annular fast fluidized-bed chamber positioned around said central recirculation chamber, said central recirculation chamber and said fast fluidized-bed chamber communicating beneath said first portion, said first portion defining with said generally conical portion a central recirculation chamber annulus, said generally conical portion being provided therethrough with a multiplicity of air jets, and said fast fluidized-bed chamber being provided therethrough around a lower periphery thereof with a multiplicity of char inlet passages.

Claim 7

Coal burning apparatus which comprises, in combination: a spouted fluidized bed pyrolyzer, a fluidized bed combustor, a first cyclone, a second cyclone, and an afterburner, the pyrolyzer being connected to accept pulverized coal and to discharge char to the combustor and gaseous materials with entrained particulate material to the first cyclone, the first cyclone being connected to deliver gases to the afterburner, the combustor being connected to accept also a combustion supporting gas and to deliver to the second cyclone gaseous materials with entrained particulate material, and the second cyclone being connected to deliver gaseous material to the afterburner, said fluidized-bed combustor being of fast, solids-recirculating character and said combustor includes a central recirculation chamber defined by a first portion cylindrical about the combustor longitudinal axis and a generally conical portion, an annular fast fluidized-bed chamber positioned around said central recirculation chamber, said central recirculation chamber and said fast fluidized-bed chamber communicating beneath said first portion, said first portion defining with said generally conical portion a central recirculation chamber annulus, said generally conical portion being provided therethrough with a multiplicity of air jets, and said fast fluidized-bed chamber being provided therethrough around a lower periphery thereof with a multiplicity of char inlet passages.

Claim 8

The apparatus of claim 4 in which said central recirculation chamber and said fast fluidized-bed chamber communicate at their opposite ends around the other end of said first portion through a multiplicity of vanes angled to provide materials moving from said fast fluidized-bed chamber to said central recirculation chamber with a centrifugal movement to throw solids toward the inner wall of said first portion, and said generally conical portion includes a withdrawal standpipe.

Claim 9

The apparatus of claim 4 in which said air jets promote circulation from said central recirculation chamber to said fast fluidized-bed chamber.

Claim 10

The apparatus of claim 4 in which said fast fluidized-bed chamber is divided into a lower agglomerating chamber and an upper desulfurizing chamber.

Claim 11

The apparatus of claim 7 in which said agglomerating chamber and said desulfurizing chamber are separated by a fluid dynamic check valve.

Claim 14

The method of claim 9 in which said stoichiometric excess of air is brought into physical contact with said char.

Claim 15

The method of claim 9 in which said pyrolyzer is heated by burning a portion of the combustibles introduced thereinto.

Claim 16

The method of claim 9 in which a diluent gas is added to said volatiles before burning said volatiles in said mixture of gases.

Claim 17

The method of claim 9 in which H 2 O is added at said pyrolyzer.

Claim 18

The method of claim 13 in which preheated air is added in burning said volatiles.

Claim 19

The method of claim 9 in which said coal is Illinois high volatile bituminous Grade B, and said ash temperature is 1600° F.

Claim 20

The apparatus of claim 1 in which said pyrolyzer is a solids recirculating device.

Claim 21

The apparatus of claim 1 in which said combustor includes a collector therein.

Claim 22

The apparatus of claim 1 in which ejector means promote recirculation in said combustor.

Claim 23

The apparatus of claim 1 in which said pyrolyzer includes a standpipe for removal therefrom therethrough of char.

Claim 24

The apparatus of claim 1 in which hot particles recirculated into a portion of said combustor adjacent an outlet thereof are passed over vanes positioned therearound to provide a whirling motion and reduce needed freeboard to prevent escape of too-hot particles.