Method and apparatus for cooling hot bulk material

Claim 2

In a method for cooling hot bulk material, such as glowing coke, clinker, or sinter material, comprising the steps of: introducing the hot bulk material through an inlet into a vertically oriented cooling tank wherein it flows downwardly under gravity and is discharged from an outlet of the cooling tank; feeding at least two partial currents of cooling gas into the cooling tank at respective feeding points therein, said feeding points being respectively arranged one over the other and so that the cooling gas flows upwardly in the tank around the material as the latter flows downwardly to cool the same with the cooling gas being simultaneously heated, the improvement comprising: the cooling gas partial current fed into the cooling tank at a lower feeding point is at a lower temperature than the cooling gas partial current fed into the cooling tank at a feeding point which is arranged above said lower feeding point.

Claim 3

The method of claim 1 wherein the cooling gas fed into the cooling tank at a lower feeding point or points is heated as it flows upwardly in the cooling tank to a particular feeding point which is arranged above said lower point or points to a temperature which corresponds to the temperature of the cooling gas partial current fed into the cooling tank at said particular feeding point.

Claim 4

The method of claim 1 including the further steps of discharging the heated cooling gas from the upper region of the cooling tank, dividing the discharged cooling gas into said partial currents and directs said cooling gas partial currents into respective channels, recooling each of the cooling gas partial currents in its respective channel, and feeding the recooled cooling gas partial currents through said channels into the cooling tank at said respective feeding points.

Claim 5

The method of claim 3 wherein in at least one of said channels the heated cooling gas is directed to a heat exchanger having at least two heating surfaces arranged in series.

Claim 6

The method of claim 1 wherein the temperature difference between the bulk material and the cooling gas at substantially all levels of the cooling tank are substantially the same.

Claim 7

Apparatus for cooling hot bulk material, such as glowing coke, clinker, or sinter material, comprising: a vertically oriented cooling tank having an upper inlet through which the material is introduced so as to flow downwardly under gravity and a lower outlet through which the material is discharged; at least two gas feed means arranged over each other in said cooling tank for feeding respective partial currents of cooling gas into said cooling tank so that the cooling gas flows upwardly in the tank around the material as the latter flows downwardly to cool the same with the cooling gas being heated; separate gas flow channels communicating with respective ones of said gas feed means for directing respective partial currents of cooling gas thereto; gas discharge means arranged proximate to said upper inlet for discharging the cooling gas from said cooling tank; and recooling means situated in said gas flow channels for recooling the cooling gas partial currents fed into the cooling tank such that the cooling gas partial current fed into the cooling tank through a lower gas feed means is at a lower temperature than the cooling gas partial current fed into the cooling tank through a gas feed means arranged above said lower gas feed means.

Claim 8

Apparatus for cooling hot bulk material, such as glowing coke, clinker, or sinter material, comprising: a vertically oriented cooling tank having an upper inlet through which the material is introduced so as to flow downwardly under gravity and a lower outlet through which the material is discharged; at least two gas feed means arranged over each other in said cooling tank for feeding respective partial currents of cooling gas into said cooling tank so that the cooling gas flows upwardly in the tank around the material as the latter flows downwardly to cool the same with the cooling gas being heated; separate gas flow channels communicating with respective ones of said gas feed means for directing respective partial currents of cooling gas thereto; gas discharge means arranged proximate to said upper inlet for discharging the cooling gas from said cooling tank; and recooling means situated in said gas flow channels for recooling the cooling gas partial currents fed into the cooling tank such that the cooling gas partial current fed into the cooling tank through a lower gas feed means is at a lower temperature than the cooling gas partial current fed into the cooling tank through a gas feed means arranged above said lower gas feed means.

Claim 9

The combination of claim 6 further including hot gas dust arrester means in fluid communication with said gas discharge means.

Claim 10

The combination of claim 6 wherein said recooling means comprises a heat recovery plant.

Claim 11

The combination of claim 8 wherein said heat recovery plant comprises a steam generating plant.

Claim 12

The combination of claim 9 wherein said steam generating plant includes at least one fluid circuit and associated heat transfer surfaces, said heat transfer surfaces being situated in at least one of said gas flow channels.

Claim 13

The combination of claim 10 wherein said heat transfer surfaces are situated in respective gas flow channels, and means for directing different amounts of cooling gas through the different gas flow channels, respectively.

Claim 14

The combination of claim 10 wherein said heat transfer surfaces include a superheater heating surface situated in one of said gas flow channels, and further including means located prior to one of said gas flow channels for moderating the temperature of the cooling gas being directed into the same.

Claim 15

The combination of claim 12 wherein said gas temperature moderating means comprise a heat accumulator.

Claim 16

The combination of claim 12 wherein said gas temperature moderating means comprise an adjustable cooling means.

Claim 17

The combination of claim 10 wherein said heat transfer surfaces are arranged in a parallel manner and are situated in respective ones of said gas flow channels and further including adjustable blowers located in respective gas flow channels for directing respective partial currents of cooling gas thereto to respective gas feed means.

Claim 18

The combination of claim 10 wherein heat transfer surfaces are arranged in series with each other and are situated in respective ones of said gas flow channels.