Burner and fine solids feeding apparatus for a burner

Abstract

Provided are a burner such as a concentrate burner, a calcine burner, or a matte burner, or a burner using a mixture of these for feeding reaction gas and fine solids into a reaction shaft of a suspension smelting furnace, and a fine solids feeding apparatus for a burner such as a concentrate burner, a calcine burner, or a matte burner, or a burner using a mixture of these. The fine solids feeding apparatus comprises gas outlets in a fine solids discharge channel upstream of a downstream outlet end of the fine solids discharge channel. The gas outlets comprise spiral path guiding members configured to facilitate gas to flow from the gas outlets in a spiral flow path around a center axis A of the fine solids discharge channel.

Claims

1. A fine solids feeding apparatus for a burner, wherein the fine solids feeding apparatus comprises: a fine solids discharge channel that is radially outwardly limited by a fine solids discharge channel wall of the fine solids discharge channel and that is radially inwardly limited by a fine solids dispersion device arranged in the fine solids discharge channel so that the fine solids discharge channel has an annular cross-section, wherein the fine solids dispersion device has dispersion gas openings and a dispersion gas channel for conducting dispersion gas to the dispersion gas openings, wherein the fine solids dispersion device extends out of a downstream outlet end of the fine solids discharge channel, and wherein the fine solids dispersion device has at the downstream outlet end of the fine solids discharge channel an enlarged section, where the diameter of the fine solids dispersion device increases in the direction towards a free distal end of the fine solids dispersion device, wherein the fine solids feeding apparatus further comprises: gas outlets in the fine solids discharge channel upstream of the downstream outlet end of the fine solids discharge channel, wherein the gas outlets comprise spiral path guiding members configured to facilitate gas to flow from the gas outlets in a spiral flow path around a center axis A of the fine solids discharge channel, partition walls in the fine solids discharge channel upstream of the gas outlets in the fine solids discharge channel, wherein the partition walls divide the fine solids discharge channel into sectors, wherein the partition walls are planar and extend in the direction of the center axis A of the fine solids discharge channel, and wherein a distance between the partition walls and the downstream outlet end of the fine solids discharge channel is between 0.1 and 1.5 m.

2. The fine solids feeding apparatus according to claim 1, comprising an annular gas channel surrounding the dispersion gas channel of the fine solids dispersion device.

3. The fine solids feeding apparatus according to claim 2, wherein the annular gas channel is arranged in the fine solids discharge channel.

4. The fine solids feeding apparatus according to claim 3, wherein the annular gas channel is arranged at the fine solids dispersion device.

5. The fine solids feeding apparatus according to claim 3, wherein the annular gas channel is arranged at the fine solids discharge channel wall of the fine solids discharge channel.

6. The fine solids feeding apparatus according to claim 3, wherein the annular gas channel is provided at a distance from the fine solids discharge channel wall and at a distance from the fine solids dispersion device.

7. The fine solids feeding apparatus according to claim 2, wherein the annular gas channel is provided in the fine solids dispersion device.

8. The fine solids feeding apparatus according to claim 2, wherein the annular gas channel is provided in the fine solids discharge channel wall of the fine solids discharge channel.

9. The fine solids feeding apparatus according to claim 1, wherein the dispersion gas openings are arranged in the fine solids discharge channel upstream of the enlarged section of the fine solids dispersion device.

10. The fine solids feed apparatus according to claim 1, wherein the burner is selected from the group consisting of a concentrate burner, a calcine burner, a matte burner, and mixtures thereof.

11. A burner comprising a fine solids feeding apparatus according to claim 1.

Description

LIST OF FIGURES

(1) In the following the invention will described in more detail by referring to the figures, of which

(2) FIG. 1 shows a first embodiment of the burner,

(3) FIG. 2 shows a second embodiment of the burner,

(4) FIG. 3 shows a third embodiment of the burner,

(5) FIG. 4 shows a fourth embodiment of the burner,

(6) FIG. 5 shows a fifth embodiment of the burner,

(7) FIG. 6 shows a sixth embodiment of the burner,

(8) FIG. 7 shows a first embodiment of the fine solids feeding apparatus,

(9) FIG. 8 shows a second embodiment of the fine solids feeding apparatus,

(10) FIG. 9 shows a third embodiment of the fine solids feeding apparatus,

(11) FIG. 10 shows a fourth embodiment of the fine solids feeding apparatus,

(12) FIG. 11 shows a fifth embodiment of the fine solids feeding apparatus, and

(13) FIG. 12 shows a sixth embodiment of the fine solids feeding apparatus.

DETAILED DESCRIPTION OF THE INVENTION

(14) The invention relates to a burner such as a concentrate burner, a calcine burner, or a matte burner, or a burner using a mixture of these for feeding reaction gas and fine solids into a reaction shaft of a suspensions smelting furnace, and to a fine solids feeding apparatus for a burner such as a concentrate burner, a calcine burner, or a matte burner, or a burner using a mixture of these.

(15) First the burner and some embodiments and variants of the burner will be described in greater detail.

(16) The burner comprises a fine solids discharge channel 1 that is radially outwardly limited by a wall 3 of the fine solids discharge channel 1 and that is radially inwardly limited by a fine solids dispersion device 3 arranged in the fine solids discharge channel 1 so that the fine solids discharge channel 1 has an annular cross-section.

(17) The burner comprises an annular reaction gas channel 4 that surrounds the fine solids discharge channel 1 and that is radially outwardly limited by a reaction gas channel wall 5 of the reaction gas channel 4 and that is radially inwardly limited by the wall 3 of the fine solids discharge channel 1.

(18) The fine solids dispersion device 3 has dispersion gas openings 6 and a dispersion gas channel 7 for conducting dispersion gas to the dispersion gas openings 6.

(19) The fine solids dispersion device 3 extends out of a downstream outlet end 8 of the fine solids discharge channel 1.

(20) The fine solids dispersion device 3 has at the downstream outlet end 8 of the fine solids discharge channel 1 an enlarged section 9, where the diameter of the fine solids dispersion device 3 increases in the direction towards a free distal end 10 of the fine solids dispersion device 3.

(21) The burner comprises gas outlets 11 in the fine solids discharge channel 1 upstream of the downstream outlet end 8 of the fine solids discharge channel 1.

(22) The gas outlets 11 comprise spiral path guiding members such as a circumferential row of individual nozzles configured to facilitate gas to flow from the gas outlets 11 in a spiral flow path around a center axis A of the fine solids discharge channel 1. The gas outlet flow momentum and the inclination angle, from the vertical axis, of the gas discharge must be sufficient in order to induce a rotational movement on the fine solid flow. Suitable discharge angle, from the vertical axis, of the spiral guiding members or the individual nozzles is between 30 and 150. Suitable discharge velocity of the spiral guiding members or the circumferential row of individual nozzles is between 5 m/s and 300 m/s, depending on the fine solid feed rate, gas composition and the vertical location of the gas discharge. The discharge velocity is regulated using flow control of the gas.

(23) The gas can for example be or comprise nitrogen or oxygen.

(24) The burner can comprise partition walls 12 in the fine solids discharge channel 1 upstream of the gas outlets 11 in the fine solids discharge channel 1, wherein the partition walls 12 dividing the fine solids discharge channel 1 into sectors, and wherein the partition walls 12 being planar and extending in the direction of the center axis A of the fine solids discharge channel 1. If the burner comprise such partition walls 12, the distance between the partition walls 12 and the downstream outlet end 8 of the fine solids discharge channel 1 is preferably, but not necessarily, between 0.1 and 3 m, such as between 0.5 and 1.5 m.

(25) The burner can comprise an annular gas channel 13 between the annular reaction gas channel 4 and the dispersion gas channel 7 of the fine solids dispersion device 3, as shown in FIGS. 1 to 6.

(26) The burner can comprise an annular gas channel 13 between the annular reaction gas channel 4 and the dispersion gas channel 7 of the fine solids dispersion device 3 so that the annular gas channel 13 is arranged in the fine solids discharge channel 1, as shown in FIGS. 1 and 2.

(27) The burner can comprise an annular gas channel 13 between the annular reaction gas channel 4 and the dispersion gas channel 7 of the fine solids dispersion device 3 so that the annular gas channel 13 is arranged in the fine solids discharge channel 1 at the fine solids dispersion device 3, as shown in FIG. 1.

(28) The burner can comprise an annular gas channel 13 between the annular reaction gas channel 4 and the dispersion gas channel 7 of the fine solids dispersion device 3 so that the annular gas channel 13 is arranged in the fine solids discharge channel 1 at the fine solids discharge channel wall 2 of the fine solids discharge channel 1, as shown in FIG. 2

(29) The burner can comprise an annular gas channel 13 between the annular reaction gas channel 4 and the dispersion gas channel 7 of the fine solids dispersion device 3 so that the annular gas channel 13 being provided in the fine solids dispersion device 3, as shown in FIG. 3.

(30) The burner can comprise an annular gas channel 13 between the annular reaction gas channel 4 and the dispersion gas channel 7 of the fine solids dispersion device 3 so that the annular gas channel 13 being provided in the fine solids discharge channel wall 2 of the fine solids discharge channel 1, as shown in FIG. 4.

(31) The burner can comprise a first set of gas outlets 11 arranged upstream of the downstream outlet end 8 of the fine solids discharge channel 1 at a first distance from the downstream outlet end 8 of the fine solids discharge channel 1, and second set of gas outlets 11 arranged upstream of the downstream outlet end 8 of the fine solids discharge channel 1 at a second distance from the downstream outlet end 8 of the fine solids discharge channel 1, wherein the second distance is longer than the first distance, as is shown in FIG. 5.

(32) The burner can comprise an annular gas channel 13 between the annular reaction gas channel 4 and the dispersion gas channel 7 of the fine solids dispersion device 3 so that the annular gas channel 13 is provided at a distance from the fine solids discharge channel wall 2 and at a distance from the fine solids dispersion device 3, as shown in FIG. 6.

(33) The gas openings are preferably, but not necessarily, arranged in the fine solids discharge channel 1 upstream of the enlarged section 9 of the fine solids dispersion device 3.

(34) Next the fine solids feeding apparatus for a burner such as a concentrate burner, a calcine burner, or a matte burner, or a burner using a mixture of these and some embodiments and variants of the fine solids feeding apparatus will be described in greater detail.

(35) The fine solids feeding apparatus comprises a fine solids discharge channel 1 that is radially outwardly limited by a fine solids discharge channel wall 2 of the fine solids discharge channel 1 and that is radially inwardly limited by a fine solids dispersion device 3 arranged in the fine solids discharge channel 1 so that the fine solids discharge channel 1 has an annular cross-section.

(36) The fine solids dispersion device 3 has dispersion gas openings 6 and a dispersion gas channel 7 for conducting dispersion gas to the dispersion gas openings 6.

(37) The fine solids dispersion device 3 extends out of a downstream outlet end 8 of the fine solids discharge channel 1.

(38) The fine solids dispersion device 3 has at the downstream outlet end 8 of the fine solids discharge channel 1 an enlarged section 9, where the diameter of the fine solids dispersion device 3 increases in the direction towards a free distal end 10 of the fine solids dispersion device 3.

(39) The fine solids feeding apparatus comprises gas outlets 11 in the fine solids discharge channel 1 upstream of the downstream outlet end 8 of the fine solids discharge channel 1.

(40) The gas outlets 11 comprise spiral path guiding members such as a circumferential row of individual nozzles configured to facilitate gas to flow from the gas outlets 11 in a spiral flow path around a center axis A of the fine solids discharge channel 1. The gas outlet flow momentum and the inclination angle, from the vertical axis, of the gas discharge must be sufficient in order to induce a rotational movement on the fine solid flow. Suitable discharge angle, from the vertical axis, of the spiral guiding members or the individual nozzles is between 30 and 150. Suitable discharge velocity of the spiral guiding members or the circumferential row of individual nozzles is between 5 m/s and 300 m/s, depending on the fine solid feed rate, gas composition and the vertical location of the gas discharge. The discharge velocity is regulated using flow control of the gas.

(41) The gas can for example be or comprises nitrogen or oxygen.

(42) The fine solids feeding apparatus can comprise partition walls 12 in the fine solids discharge channel 1 upstream of the gas outlets 11 in the fine solids discharge channel 1, wherein the partition walls 12 dividing the fine solids discharge channel 1 into sectors, and wherein the partition walls 12 being planar and extending in the direction of the center axis A of the fine solids discharge channel 1. If the burner comprise such partition walls 12, the distance between the partition walls 12 and the downstream outlet end 8 of the fine solids discharge channel 1 is preferably, but not necessarily, between 0.1 and 3 m, such as between 0.5 and 1.5 m.

(43) The fine solids feeding apparatus can comprise an annular gas channel 13 surrounding the dispersion gas channel 7 of the fine solids dispersion device 3, as shown in FIGS. 7 to 12.

(44) The fine solids feeding apparatus can comprise an annular gas channel 13 surrounding the dispersion gas channel 7 of the fine solids dispersion device 3 so that the annular gas channel 13 is arranged in the fine solids discharge channel 1, as shown in FIGS. 7 and 8.

(45) The fine solids feeding apparatus can comprise an annular gas channel 13 surrounding the dispersion gas channel 7 of the fine solids dispersion device 3 so that the annular gas channel 13 is arranged in the fine solids discharge channel 1 at the fine solids dispersion device 3, as shown in FIG. 7.

(46) The fine solids feeding apparatus can comprise an annular gas channel 13 surrounding the dispersion gas channel 7 of the fine solids dispersion device 3 so that the annular gas channel 13 is arranged in the fine solids discharge channel 1 at the fine solids discharge channel wall 2 of the fine solids discharge channel 1, as shown in FIG. 8

(47) The fine solids feeding apparatus can comprise an annular gas channel 13 surrounding the dispersion gas channel 7 of the fine solids dispersion device 3 so that the annular gas channel 13 being provided in the fine solids dispersion device 3, as shown in FIG. 9.

(48) The fine solids feeding apparatus can comprise an annular gas channel 13 surrounding the dispersion gas channel 7 of the fine solids dispersion device 3 so that the annular gas channel 13 being provided in the fine solids discharge channel wall 2 of the fine solids discharge channel 1, as shown in FIG. 10.

(49) The fine solids feeding apparatus can comprise a first set of gas outlets 11 arranged upstream of the downstream outlet end 8 of the fine solids discharge channel 1 at a first distance from the downstream outlet end 8 of the fine solids discharge channel 1, and second set of gas outlets 11 arranged upstream of the downstream outlet end 8 of the fine solids discharge channel 1 at a second distance from the downstream outlet end 8 of the fine solids discharge channel 1, wherein the second distance is longer than the first distance, as is shown in FIG. 11.

(50) The fine solids feeding apparatus can comprise an annular gas channel 13 surrounding the dispersion gas channel 7 of the fine solids dispersion device 3 so that the annular gas channel 13 is provided at a distance from the fine solids discharge channel wall 2 and at a distance from the fine solids dispersion device 3, as shown in FIG. 12.

(51) The gas openings are preferably, but not necessarily, arranged in the fine solids discharge channel 1 upstream of the enlarged section 9 of the fine solids dispersion device 3.

(52) The invention relates also to a burner comprising a fine solids feeding apparatus as described above.

(53) It is apparent to a person skilled in the art that as technology advanced, the basic idea of the invention can be implemented in various ways. The invention and its embodiments are therefore not restricted to the above examples, but they may vary within the scope of the claims.