Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
  • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
  • B02C17/00—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
  • B02C17/18—Details
  • B02C17/20—Disintegrating members

Definitions

• the invention relates to a process for the fine grinding of mineral particles by means of a grinder containing grinding bodies comprising steel or cast iron balls, having dimensions of between 20 mm and 120 mm.
• the object of the invention is to develop a fine grinding process for mineral particles making it possible to obtain an optimum yield from the grinder with energy savings and an increase in productivity.
• the method according to the invention is characterized by the following stages consisting in: - manufacturing by atomization of steel balls with high carbon content or of cast iron in a range of particle size remaining less than 15 mm, - and mixing the balls with the balls inside the mill according to a predetermined weight proportion depending on the particle size of the mineral particles to be ground, and the desired reduction ratio between the feed and the final product.
• the proportion by weight of the balls in the mixture increases in the event of a reduction in the particle size distribution of the particles at the inlet, and conversely decreases in the event of an increase in said particle size distribution.
• the steel or the cast iron balls have a carbon content of the order of 0.6% to 3.5%, and can be alloyed with Cr and / or Mo. According to another characteristic of the invention, the balls undergo, after atomization, a heat treatment for hardening to the core intended to reinforce the mechanical resistance and the resistance to corrosion.
• FIG. 1 is a schematic view of the grinding circuit equipped with a primary mill upstream of a secondary mill for fine grinding of the particles;
• FIG. 2 illustrate two diagrams of the reduction ratio of the particles of the product to be ground according to the weight proportion of the balls in the ground mixture.
• the invention relates to the fine grinding of mineral particles, in particular of rocks, ores, concentrated sulphides or other minerals with a high metallic content, or even industrial minerals, having previously undergone a first reduction in size in a primary mill 10
• the dimensions of the mineral particles obtained following this prior grinding are generally greater than 50 or 100 microns.
• Subsequent fine grinding is then carried out in a secondary reciprocating mill 12 with recirculation (closed circuit) to reduce the particle size of the particles at the outlet 14. It is also possible to use a mill without recirculation (open circuit not shown) in Figure 1).
• the primary crusher 10 of the autogenous type is associated with a screen 16 surmounted by a watering ramp 18 to separate the solid fragments of rock according to their size. The largest fragments are recycled in the primary mill 10, and the finest are sent to the secondary grinding circuit.
• the base of the screen 16 is connected by a pipe 18 to a recovery tank 20, which is connected by a pump 22 to at least one cyclone separation device 24.
• Cyclone 24 has an underflow 26 for recycling and an overflow 28 for evacuation of the finished product corresponding to fine grinding whose particle size is less than 100 microns.
• a pipe 30 connects the underflow 26 to a hopper 32 for supplying the secondary mill 12 to ensure the recycling of excessively large particles.
• the secondary crusher 12 with horizontal rotary drum 33 has an inlet 34 in connection with the hopper 32, and a longitudinal chamber 35 containing bodies or grinding media constituted by a mixture of balls 36 and balls 38 of steel.
• the outlet 14 of the secondary crusher 12 is offset downward relative to the level of the inlet 34, and comprises a grid 40 disposed above the recovery tank 20.
• the balls 36 and the balls 38 are distributed over the entire length of the chamber 35 while remaining stored by gravity at a filling level set back from the inlet 34 and the outlet 14, said level depending on the load factor.
• the particles to be ground are injected into the chamber 35 in the axial direction indicated by the arrow F.
• the balls 36 of the grinding charge are used in a conventional manner in grinders, and are generally made of steel or cast iron with sizes between 20 mm and 120 mm.
• the shape of the balls 36 can be spherical or cylindrical with precise diameters.
• liquid phase grinding system described above can also be replaced by dry grinding in open or closed circuit with recirculation.
• the fluid is air.
• the innovation consists in mixing the balls 38 of smaller sizes with the balls 36 to optimize the reduction ratio of the particles inside the secondary mill 12.
• the balls 38 have spherical or slightly flattened shapes, with diameters less than 15 mm.
• the chemical composition of the balls 38 can be that of steel or cast iron shot, with a carbon content of the order of 0.6% to 3.5%.
• the steel or cast iron can be alloyed with Cr and / or Mo, or any other element capable of reinforcing the resistance to wear, to corrosion and to mechanical shocks occurring during grinding.
• the steel or cast iron balls 38 are advantageously obtained by atomization with water or by centrifugation, with a range of variable particle sizes remaining less than 15 mm. After the atomization phase, the balls 38 undergo a selection of the shape, sorting by sizes, and then heat treatments to carry out core hardening intended to standardize the hardness at the periphery and in the center.
• the minimum cooling rate in the mass of a ball 38 is preferably greater than 10 ° C / second.
• the proportion by weight of the balls 38 in the mixture with the balls 36 depends on the particle size of the particles at the inlet 34 of the secondary mill 12. It will be all the greater the finer the particle size of the particles at the inlet. Conversely, in the event of an increase in the particle size of the particles of the product to be ground, it is necessary to reduce the proportion of the balls 38 relative to the balls 36. During the rotation of the grinding drum 33, the balls 38 attack the small particles , while the balls 36 take care of the larger particles. The grindability of the product to be ground can also influence the proportion of the balls 38.
• the balls 38 and the balls 36 of the grinding bodies have a real density greater than 7.5.
• the smallest balls 38 will occupy the interstices between the balls 36 so as to increase the apparent density of the load, and to release volume for the pulp 42.
• the apparent density of the balls (38) must be greater than 4.
• the diameter of the spherical balls (38) is preferably between 1 mm and 12 mm.
• the pulp layer 42 exceeds the level of the grinding load, at a level substantially coplanar with the outlet 14, and below the inlet 34.
• FIG. 2 shows two diagrams of the reduction ratio of the particles of the product to be ground as a function of the weight proportion of the balls 38 in the grinding mixture corresponding to two particle sizes of 160 microns and 370 microns of the particles, and at the same grinding time on the order of 30 minutes.
• the reduction ratio of the particles is optimum (approximately 7.5) when the percentage of beads 38 in the mixture is 60%.
• the reduction ratio increases linearly by 40% (from 5.3 to 7.5) for a percentage of beads 38 varying from 0 to 60%.
• the reduction ratio of the particles is optimum (approximately 6.2) when the percentage of beads 38 in the mixture is 30%. It then decreases with a slight slope (up to 5.8) when the percentage of beads 38 varies from 30% to 60%.
• the reduction ratio increases linearly by 16% (from 5.3 to 6.2) for a percentage of beads 38 varying from 0 to 30%.
• the vertices A and B of the two curves correspond to the maximum degree of grinding of the grinder for predetermined particle sizes at the inlet.
• the optimum final particle size at the outlet of the secondary mill 12 is then of the order of 20 microns following the reduction ratio of 7.5 for an inlet particle size of 160 microns, and 60 microns following the reduction ratio of 6 , 2 for an input particle size of 370 microns.

Landscapes

• Engineering & Computer Science (AREA)
• Food Science & Technology (AREA)
• Crushing And Grinding (AREA)
• Disintegrating Or Milling (AREA)
• Finish Polishing, Edge Sharpening, And Grinding By Specific Grinding Devices (AREA)
• Manufacture Of Metal Powder And Suspensions Thereof (AREA)
• Manufacture And Refinement Of Metals (AREA)
• Crushing And Pulverization Processes (AREA)

Applications Claiming Priority (3)

Publications (2)

Family

ID=8864731

Family Applications (1)

Country Status (12)

Families Citing this family (8)

Family Cites Families (13)

• 2001
  • 2001-06-25 FR FR0108350A patent/FR2826299B1/fr not_active Expired - Fee Related
• 2002
  • 2002-06-25 DE DE60209921T patent/DE60209921T2/de not_active Expired - Lifetime
  • 2002-06-25 AT AT02760362T patent/ATE320313T1/de not_active IP Right Cessation
  • 2002-06-25 WO PCT/FR2002/002197 patent/WO2003000427A1/fr active IP Right Grant
  • 2002-06-25 EP EP02760362A patent/EP1401583B1/de not_active Expired - Lifetime
  • 2002-06-25 JP JP2003506659A patent/JP4156510B2/ja not_active Expired - Fee Related
  • 2002-06-25 US US10/480,815 patent/US7093782B2/en not_active Expired - Fee Related
  • 2002-06-25 BR BRPI0210639-6A patent/BR0210639B1/pt not_active IP Right Cessation
  • 2002-06-25 MX MXPA03011233A patent/MXPA03011233A/es active IP Right Grant
  • 2002-06-25 ES ES02760362T patent/ES2260473T3/es not_active Expired - Lifetime
  • 2002-06-25 CA CA002450190A patent/CA2450190C/en not_active Expired - Fee Related
• 2003
  • 2003-12-17 ZA ZA200309746A patent/ZA200309746B/en unknown

Non-Patent Citations (1)

Also Published As

Similar Documents

Legal Events