Nozzle and a tundish arrangement for the granulation of molten material

Abstract

A nozzle, a tundish arrangement used for the production of granulated material, and a method and apparatus for the production of a granulated material with an improved size distribution are provided. The grain size and grain size distribution is controlled by a nozzle having a specific design. The nozzle comprises an upper inlet opening, sidewalls forming a channel, a bottom and at least one outlet opening or at least one row of outlet openings at the lower end of the channel. The outlet opening(s) in the channel have a size of at least 5 mm in the smallest dimension. A cross sectional area of the channel at the inlet A.sub.C is at least 3 times bigger than the total area of the outlet openings A.sub.T.

Claims

1. A nozzle for the granulation of molten material, for obtaining a granulated material having a mean size in a range of 10-50 mm, wherein an amount of fines in the granulated material with a size of less than 8 mm is limited to 5%, the nozzle comprising: an inlet defining an inlet opening, a bottom, sidewalls forming a channel from the inlet to the bottom, at least one row of no more than 4 outlet openings at a lower end of the sidewalls, wherein each outlet opening of the 4 outlet openings has a diameter of 10-35 mm, wherein A.sub.C6A.sub.T, with A.sub.C being a cross sectional area of the channel at the inlet opening, and A.sub.T being a total area of the 4 outlet openings, and wherein the granulated material is selected from a group comprising iron, pig iron, steel, and ferroalloy.

2. The nozzle according to claim 1, fulfilling at least one requirement selected from a group, comprising: a length L of the nozzle is 80 cm, the length L of the nozzle is 60 cm, the channel is straight and has a circular cross section with a diameter of 80-200 mm, the channel is tapered and has a circular cross section at the inlet with a diameter of 80-200 mm, A.sub.C10A.sub.T, and A.sub.C15A.sub.T.

3. A tundish for the production of the granulated material comprising the nozzle as defined in claim 1.

4. The tundish according to claim 3, further comprising a rotator attached thereto.

5. The tundish according to claim 4, wherein the tundish has a circular cross section and the nozzle is centrally attached thereto.

6. An apparatus for producing the granulated material having a mean size of at least 5 mm, the apparatus comprising: a cooling tank for containing a cooling fluid, a tundish comprising the nozzle according to claim 1, and a feeder for feeding the molten material to the tundish, wherein the tundish is positioned above the cooling tank.

7. The apparatus according to claim 6, further comprising at least one feature selected from a group comprising: a circulator for circulating the cooling fluid in the cooling tank in a same direction with respect to the circulator, a circulator for circulating the cooling fluid in the cooling tank in an opposite direction with respect to the circulator, a height adjuster for adjusting the height of the nozzle in relation to an upper level of the cooling fluid in the cooling tank, a material remover for removing the granulated material from the cooling tank, a controller for controlling rotation of the tundish within a range of 1-50 rpm, a regulator for regulating the flow of the molten material from the feeder to a distributor, an intermediate receptor for supplying the molten material to the tundish, a chute for supplying the molten material to the tundish, and a refractory safety plate positioned below the nozzle, wherein the refractory safety plate spreads a stream of the molten material over a surface of the cooling fluid in case of a nozzle breakage.

8. A method of producing a granulated material, comprising: a) providing the apparatus according to claim 6, b) rotating the tundish at a speed of 1-50 rpm, c) feeding the molten material to the tundish, d) distributing at least one stream of the molten material over the cooling fluid in the cooling tank, e) disintegrating the molten material at least one of above and within the cooling fluid, and f) forming at least partly solidified granules of the granulated material, and g) recovering the granulated material from a bottom of the cooling tank.

9. The method of producing the granulated material according to claim 8, further comprising at least one feature selected from a group comprising: using water with additions as the cooling fluid, using water without additions as the cooling fluid, rotating the tundish at a speed of 1-10 rpm, feeding the molten material at a rate of 0.5-10 t/min circulating the cooling fluid in the cooling tank in a same direction with respect to a rotator, circulating the cooling fluid in the cooling tank in an opposite direction with respect to the rotator, adjusting a height between the cooling fluid in the cooling tank to openings in a rotating distributor to be 0.1-1.5 m, controlling a melt level in the tundish by controlling a flow from a feeder for the molten material to the rotating distributor, controlling the melt level in the rotating distributor by controlling the flow from the feeder for the molten material to the rotating distributor, controlling a rate of granulation by controlling a level of the molten material in at least one of the tundish and the rotating distributor, recovering solidified granules dischargeable from a lower end of the cooling tank using a water and an air ejector, and controlling the rate of granulation by controlling the level of at least one of a liquid slag and the molten metal in at least one of the tundish and the rotating distributor.

10. The nozzle according to claim 1, wherein each outlet opening of the 4 outlet openings is elliptically shaped, having a height to width ratio (h/w) in a range from 1:1.2 to 1:10.

11. The nozzle according to claim 1, wherein each outlet opening of the 4 outlet openings is directed 0-45 upwards.

12. The nozzle according to claim 1, wherein the outlet opening of the 4 outlet openings is directed 0-45 downwards.

Description

BRIEF DESCRIPTION OF THE FIGURES

(1) In the following, the invention will be described in more detail with reference to the preferred embodiments and the appended drawings.

(2) FIG. 1 is a schematic drawing of the apparatus used in the Granshot process.

(3) FIG. 2 is a schematic drawing of one embodiment of the present invention in which the pouring nozzle is attached to a rotating tundish.

(4) FIG. 3 is a schematic drawing of a pouring nozzle according to the invention.

(5) FIG. 4 is a schematic drawing of a tundish arrangement according to the invention.

(6) FIG. 5 discloses the size distribution of the granules of the invention obtained in Example 1 wherein the ferronickel contained 32% Ni and 0.1% Si.

(7) FIG. 6 discloses the size distribution of the granules of the comparative method wherein the ferronickel contained 32% Ni and 0.1% Si.

(8) FIG. 7 discloses the size distribution of the granules of Example 1 wherein the ferronickel contained 32% Ni and 0.27% Si.

(9) FIG. 8 discloses the size distribution of the granules of the comparative method wherein the ferronickel contained 32% Ni and 0.27% Si.

(10) FIG. 9 is a schematic drawing of a tapered pouring nozzle according to the invention.

DETAILED DESCRIPTION OF THE INVENTION

(11) The present invention will be described in detail with reference to the attached drawings.

(12) The inventive nozzle and tundish arrangement can be used in an apparatus for the production of granulated material as shown in FIG. 2. The apparatus comprises a cooling tank containing a cooling fluid, means for feeding the liquid material to a rotatable tundish which is positioned above the cooling tank, a nozzle attached to the bottom of the rotatable tundish, the nozzle comprises an upper inlet opening, sidewalls forming a channel, a bottom and at least one outlet opening or at least one row of outlet openings at the lower end of the channel, wherein the outlet openings in the channel have a size of at least 5 mm in the smallest dimension and not more than 50 mm in its largest dimension and wherein the cross section area of the channel at the upper inlet (A.sub.C) is at least 3 times bigger than the total area of the outlet openings (A.sub.T); A.sub.C3 A.sub.T. The smallest dimension of the outlet openings may be 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18 19 or 20 mm. The largest dimension may be restricted to 50, 45, 50, 40, 35, 30, 25, 20, 18 or 16 mm.

(13) The nozzle is designed in order to optimize the flow conditions for granulation.

(14) FIG. 3 discloses a nozzle according to the invention. The length (L) of the nozzle may be limited to 80 cm, preferably to 60 cm. Hence, the length may be restricted to 80, 70, 60, 55, 50, 45, 40, 35, 30, 25 or 20 cm. The vertical channel formed by the sidewalls may have any suitable form. It may have a polygonal cross section such as a square or be elliptic. However, for practical reasons the channel may have a general cylindrical form as shown in FIG. 3 with a diameter (d) in the range of 6 to 20 cm or 8 to 15 cm. Hence, the diameter may be 6, 7, 8, 9, 10, 11, 12, 13, 14 or 15 cm. The diameter of the vertical channel is much larger than the diameter of the outlets.

(15) The cross sectional area of the channel at the inlet (A.sub.C) is much larger than the total area of the outlets (A.sub.T), wherein said total area is calculated from the size of the outlet openings on the inside of the sidewalls, because the outlet openings may be tapered. In order to optimize the flow conditions for granulation the ratio between the cross sectional area of the channel at the inlet and the total area of the outlets A.sub.C/A.sub.T should be at least 3. Preferably, A.sub.C/A.sub.T6, A.sub.C/A.sub.T12, A.sub.C/A.sub.T16 or even A.sub.C/A.sub.T20.

(16) The vertical channel formed by the sidewalls may have a larger cross sectional area at the inlet (A.sub.C) than at the lower end. The vertical channel may be tapered or conical. The diameter at the inlet (d) is then larger than at the lower end of the channel. FIG. 9 discloses a tapered nozzle. In this case the outer contour of the nozzle is also conical, which can simplify the mounting of the nozzle, e.g. in a conical seat. The outlet openings at the lower end of the channel may be lightly tapered.

(17) The nozzle may be provided with one or more of the following features.

(18) Circular openings may be provided at the lower end of the sidewalls having a diameter of 10-50 mm, 10-30, 20-35 or 12-30 mm. The smallest diameter of said opening can be 10, 11, 12, 13, 14, 15, 16, 17, 18 19 or 20 mm. The largest diameter may be restricted to 50, 45, 40, 35, 32, 30, 28, 26, 24, 22, 20, 18 or 16 mm. The size and number of the openings depend on the design capacity i.e. tonnes per minute.

(19) Elliptical openings may be provided having a height to width ratio (h/w) in the range of from 1:1.2 to 1:10. By adjusting the form of the opening, it is possible to adjust the form of the molten stream leaving the distributor. A wider opening results in a more film-like stream, thereby the size and shape of the granules may be influenced.

(20) One row of openings and, preferably, not more than 4 openings may be provided in said single row. In order to get a good heat dissipation, the number of openings may be 2, 3 or 4. This design is the most simple to produce and the method is easy to control. It is therefore a preferred design.

(21) Openings may be directed 0-45 upwards, e.g., 5 or 25 upwards, or 15-20 upwards. By this measure, it is possible to adjust the path and the time in the air before the stream hits the cooling liquid. Also, the spread of the molten stream over the cooling bath is influenced by the parabolic flight.

(22) Openings may be directed 0-45 downwards. By directing one or more streams downwards, it is possible to shorten the flight distance, reduce the risk of disintegration of the stream before it hits the cooling bath and influences the spread over the cooling bath.

(23) Tapered openings may be provided.

(24) FIG. 4 is a schematic drawing of a tundish arrangement according to the invention.

(25) According to a preferred embodiment the tundish has a circular cross section and the pouring nozzle is centrally attached thereto. The pouring nozzle may have 4 circular openings each having a diameter of 10-30 mm, preferably 20-25 mm. The pouring nozzle may have 3 circular openings each having a diameter of 10-35 mm, preferably 22-28 mm. The pouring nozzle may have 2 circular openings each having a diameter of 10-40 mm, preferably 26-35 mm.

(26) The tundish may be provided with a weighing system that automatically controls the level in the tundish in order to maintain a constant liquid head and thereby a constant flow rate through the pouring nozzle. Alternatively, the automatic control system may include optical or electromagnetic sensors.

(27) The granulated material obtained with the inventive method has a narrow size distribution and typically a mean size in the range of 12-50 mm, preferably 16-30 mm and wherein the amount of fines having a size of less than 8 mm may be limited to 5% or even to 3%. The amount of fines having a size of less than 6 mm may be limited to 3% or even to 1%. The amount of fines having a size of less than 5 mm may be limited to 1%. The upper limit for the mean size may be 45 mm, 40 mm, 35 mm, 32 mm, 30 mm or 25 mm. The lower limit for the mean size may be 12 mm, 14 mm, 16 mm, 18 mm or 20 mm. The upper and lower limits may be freely combined. A ferronickel material comprising more than 2 wt. % C and/or wt. % Si may be disclaimed from this invention.

(28) The amount of coarse granules having a size of >80 mm may be limited to 5% or even completely avoided.

(29) The amount of coarse granules having a size of >60 mm may be limited to 10%, 8%, 5%, 3% or 1%.

(30) The amount of coarse granules having a size of >40 mm may be limited to 15%, 10%, 5%, 3% or 1%.

(31) The amount of coarse granules having a size of >25 mm may be limited to 30%, 25%, 20%, 15%, 10%, 5%, 3% or, as shown in FIG. 1, to 1%.

(32) The limitations with respect to the amount of fines and coarse granules are expressed as % of the total weight.

(33) The invention is not to be seen as limited by the embodiments described above, but can be varied within the scope of the claims, as will be understood by the person skilled in the art.

EXAMPLES

(34) In the following results obtained according to the invention are compared to results obtained with the known apparatus having a flat spray head. In all examples ferronickel was melted in an induction furnace and supplied to the tundish by use of a tapping spout. Tapping temperature was 1650 C. The melt level in the tundish was manually controlled to be 300-400 mm. The nozzle diameter in the tundish was 72 mm. After completed granulation the granules were removed from the tank, dried, weighted and subjected to screening. Size classes used were <4 mm, 4-8 mm, 8-12 mm, 12-16 mm, 16-25 mm and >25 mm. The results are given in % of the total weight.

Example 1

(35) In this example the ferronickel contained 32% Ni and 0.1% Si.

(36) The nozzle according to the invention had four holes in one single row. The four openings had a total opening area (A.sub.T) of 346 mm2, thus A.sub.C10A.sub.T.

(37) A rotation speed of 3 rpm was used in order to secure an uniform heat dissipation.

(38) The size distribution of the granules obtained according to the invention is disclosed in FIG. 5 (Charge Nr. 108).

(39) The size distribution of the granules obtained with a conventional flat spray head is shown in FIG. 6 (Charge Nr. 110).

(40) It is evident that the inventive apparatus resulted in an improved size distribution in that the amount of fines was reduced, the mean size was increased and the size distribution was improved.

Example 2

(41) In this example the effect of an increased content of Si on the size distribution was examined.

(42) The ferronickel contained 32% Ni and 0.27% Si. The granulation conditions were the same as for Example 1.

(43) The size distribution of the granules obtained according to the invention is disclosed in FIG. 7 (Charge Nr. 116).

(44) The size distribution of the granules obtained with a conventional flat spray head is shown in FIG. 8 (Charge Nr. 115).

(45) An improved size distribution was achieved in both cases.

(46) The result for the conventional spray head was as expected, since it is known that Si has a positive influence on the size distribution. A comparison between Charge Nr. 115 and Charge Nr. 110 reveals that the increased Si content resulted in less fines and an improved size distribution.

(47) However, the increased content of Si turned out to have a remarkable effect on the size distribution obtained with inventive apparatus. A comparison of Charge Nr. 116 and Charge Nr. 115 reveals that the amount of fines was virtually eliminated and the mean size of the granules was very much increased.

Example 3

(48) In this experiment the generation of fines during the granulation of a commercial ferronickel grade having nominal content of 32% Ni and <0.5% Si. Nozzles of the type disclosed in FIG. 9 were used. The inner diameter (d) was 138 mm and the length (L) of the nozzle was 350 mm for all charges. The diameter of the outlet openings for the nozzle having three holes was 25 mm. The diameter of the outlet openings for the nozzle having four holes was 22 mm.

(49) The results are given in the Table 1 below.

(50) TABLE-US-00001 TABLE 1 Result from granulation of commercial FeNi. Charge No. 1 2 3 Melt. Temp. ( C.) 1643 1650 1641 Nozzle outlets 3 3 4 Rotation (RPM) 4 4 4 Tons granulated 48 18 13 A.sub.C/A.sub.T 9.9 9.9 9.6 Fines, % < 6 mm 3.00 2.05 1.85

(51) The cross section area of the channel at the inlet (A.sub.C) was nearly 10 times bigger than the total area of the outlet openings (A.sub.T) for all charges. The granules obtained had a low fraction of fines having a size of less than 6 mm. In fact, not more than 3 wt. % fines were generated for any of these charges.

INDUSTRIAL APPLICABILITY

(52) The invention is particular suited for application in the ferroalloy-, iron- and steel-industries.