US3715083A

US3715083A - Method for controlling the grind in a single stage autogenous grinding mill

Info

Publication number: US3715083A
Application number: US00099182A
Authority: US
Inventors: R Funk
Original assignee: Bethlehem Steel Corp
Current assignee: Bethlehem Steel Corp
Priority date: 1970-12-17
Filing date: 1970-12-17
Publication date: 1973-02-06
Anticipated expiration: 1990-02-06
Also published as: CA951699A

Abstract

Crushed run-of-the-mine ore is fed to an autogenous mill in size ranges arbitrarily classified as relatively coarse (RCF), relatively medium (RMF) and relatively fine (RFF) particles. The output from the autogenous mill is also arbitrarily classified as relatively coarse (RCO), relatively medium (RMO) and relatively fine (RFO) particles. The particles in the output are smaller than the crushed run-of-the-mine ore fed to the mill. The relatively coarse particles (RCO) of the output are stored, and, intermittently, amounts thereof are returned to the mill as a portion of the feed thereto to maintain a ratio of the size consist in the mill at 35/40 percent relatively coarse:20/30 percent relatively medium:35/40 percent relatively fine particles. The relatively medium particles (RMO) can be recycled to the mill as a part of the feed. The relatively fine (RFO) particles in the output from the mill are passed to beneficiation. Maximum throughput of run-of-the-mine ore at constant power input to the mill is maintained.

Description

United States Patent Funk METHOD FOR CONTROLLING THE GRIND IN A SINGLE STAGE AUTOGENOUS GRINDING MILL I HOPPER I Feb. 6, 1973 57 ABSTRACT Crushed run-of-themine ore is fed to an autogenous mill in size ranges arbitrarily classified as relatively coarse (RCF), relatively medium (RMF) and relatively fine (RFF) particles. The output from the autogenous mill is also arbitrarily classified as relatively coarse (RCO), relatively medium (RMO) and relatively fine (RFO) particles. The particles in the output are smaller than the crushed run-of-the-mine ore fed to the mill. The relatively coarse particles (RCO) of the output are stored, and, intermittently, amounts thereof are returned to the mill as a portion of the feed thereto to maintain a ratio of the size consist in the mill at 35/40 percent relatively coarse:20/3O percent relatively mediumz35/4O percent relatively fine particles. The relatively medium particles (RMO) can be recycled to the mill as a part of the feed. The relatively fine (RFO) particles in the output from the mill are passed to beneficiation. Maximum throughput of run-of-the-mine ore at constant power input to the mill is maintained.

1 Claim, 2 Drawing Figures RECYCLED R C O y FEED MIX AUTOGENOUS MILL \ I MlLLP I 2a OUT UT RCO PARTICLE l3 STORAGE l4 SCREENS TO SEPARATOR PATENTEDFEBHB 1975 3,715,083

HOPPER} RECYCLED RCO AUTOGENOUS FEED MIX M|LL u l mu.

m OUTPUT RCO E" PARTICLE STORAGE TD SEPARATOR -1 HOPPER RECYCLED R c o AUTOGENOUS FEED mx mu. u

MILL

UTP 'r I20 RCO PARTICLE V STORAGE RECYCLED PARTICLES RMO '4 SCREENS R F0 H TO SEPARATOR INVENTOR Robert/l4 Funk METHOD FOR CONTROLLING THE GRIND IN A SINGLE STAGE AUTOGENOUS GRINDING MILL BACKGROUND OF THE INVENTION trolling the size consist therein.

To prepare the run-of-the-mine ore for autogenous grinding, the large pieces of raw ore obtained in mining are crushed to a range of sizes arbitrarily referred to as relatively coarse, relatively medium and relatively fine particles which are fed to the mill. These particles which are fed to the mill hereinafter will be referred to as relatively coarse feed (RCF), relatively medium feed (RMF) and relatively fine feed (RFF). Generally, the above size ranges are set at the primary crusher. However, it is impossible to control the amounts of material in each size range. The autogenous mill produces its own grind of particles hereinafter referred to as relatively coarse output (RCO), relatively medium output (RMO) and relatively tine output (RFO). The size of the RFC particlesis less than the size of the RFF particles. The size of the RMO particles is most comparable in size to the REF particles, and the size of the RC particles is most comparable in size to the RMF particles. As is well known, a portion of the ore which is ground and passed out of the mill contains particles which are too large to be beneficiated and a portion'of the discharge is fine enough to be passed to beneficiation. The particles which are too large for beneficiation are recycled to the mill as part of the feed. The recycled material contains all the particles which are classified as RC0 and RMO particles in the output of the mill. If a major portion of the recycled material consists of RMO particles, the amount of the RCF particles and RMF particles in the size consist in the mill is reduced. There is an insufficient amount of RCF particles in the mill for effective grinding. The mill becomes overloaded, necessitating either a cut-back in the amount of run-of-the-mine ore feed to the mill and/or an increase in the power consumption to the mill to maintain production. On the other hand, if the recycled material contains a major portion of RCO particles there is an attendant buildup of this size particle in the size consist in the mill. The mill becomes overloaded with this size particle and a cut-back in the amount of run-ofthemine ore feed to the mill and/or an increase in the power to the mill is required to maintain production. In

SUMMARY OF THE INVENTION Broadly, the method of the invention comprises con- I trolling the amount of the particles having a critical size range recycled to the mill from the discharge therefrom, to control the size consist in the mill.

DESCRIPTION OF THE DRAWING FIG. I is a schematic view of the: autogenous grinding 0 mill circuit of the invention.

either case, production is reduced and power is increased thereby causing an increase in costs and a decrease in efficiency in operation.

It is therefore an object of this invention to provide a method for controlling the size consist in the autogenous mill to control the grinding of a raw friable run-of-the-mine ore in theautogenous grinding mill FIG. 2 is a branch circuit added to the circuit of FIG. 1 whereby the method of the invention can be practiced.

PREFERRED EMBODIMENT OF THE INVENTION In the practice of the invention, FIG. 1, a raw friable run-of-the-mine ore is crushed in a primary crusher (not shown) and is stored in hopper 10. The primary crusher (not shown) produces crushed raw friable runof-the-mine ore which contains particles covering a wide scope of particles having sizes which are arbitrarily classified as relatively coarse (RCF), relatively medium (RMF) and relatively fine (RFF). The amounts of each size range from the primary crusher are not readily controllable. Therefore, the crushed raw friable ore delivered to the autogenous mill 12 from storage hopper by the conveyor 11 contains varying amounts of the three size ranges. The size ranges can be +6 inch, 6,+3 inch and 3 inch, respectively. I have maximum throughput of ore at constant power, the size consist of the particles in the mill should be in a weight ratio of about 35 percent to about 40 percent particles having a size +6 inch, about percent to about percent particles having a size 6,1+3 inch and about to about percent particles having a size 3 inch. Deviations from the desired ratio mentioned above result in either reduced production of the mill at constant power input or increased power input to the mill to maintain production. I have found that by con trolling the amount of material from the output of the mill recycled to the feed of the mill, the size consist in the mill can be controlled to contain the above mentioned weight ratio. The particles 13 in the output from the autogenous mill 12 are also classified into three size ranges designated as relatively coarse (RCO), relatively medium (RMO) and relatively fine (RFO). The largest size particles in the output from the mill are controlled by a screen 12a having apertures which will allow all particles smaller than a predetermined size to pass through as the output of the mill. I prefer to use a screen having apertures which will allow particles having a size of up to about -3 inches to pass out of the mill. The particle sizes in the aforementioned output size ranges are fixed by screen 14 having appropriate apertures therein. I prefer to classify the particle size of the output from the mill into the following size ranges:

relatively coarse (RCO) +l inch, relatively medium I (RMO) l,+ 56 inch and relativelyfine (RFO) inch. The size consist of the output from the mill is as follows:

Output from Particle Size Size Autogenous Mill ,Coarse +l inch 7.5% Medium l inch 27.5% Fine -96 inch 75.0%

I have found that the RC particles are a critical size. The RCO particles are stored in hopper 15. The amount of the RC0 particles recycled to the mill is,

therefore, easily controlled thereby controlling the size that is, if the ratio of particles varies from the aforementioned ratio because of the lack of RCO particles, reduction in the mill will be essentially by abrasion rather than by attrition or impact. A material build-up in the mill occurs because reduction by abrasion is a slower and more inefficient method of reducing particle size than is attrition or impact. The result is a net increase in grinding power requirement due to lower feed at the same mill power. To reestablish the ratio of the size consist in the mill, a portion of the RC0 particles in the mill output which has been stored is charged into the mill as a portion of the feed thereto. The amount of the critical sized particles in the size consist in the mill is increased. The amounts of the other size particles in the size consist are decreased and the above desired weight ratio in the size consist in the mill is reestablished. Maximum throughput at constant power is now obtained.

If all the RC0 particles, +1 inch, from the output are recycled to the mill and an imbalance in the size consist in the autogenous mill is created because the amount of RMF particles therein has increased to more than about 30 percent by weight, the throughput of the autogenous mill is again reduced. The millwill continue to produce an overabundance of RCO particles in the output therefrom. A build-up of this size range in the mill occurs. Power consumption must be increased to maintain maximum throughput. To correct the im- 7 balance, the portion of the RC0 particles from the mill output usually recycled as part of the feed to the mill is discontinued. The RCO particles are diverted to a secondary crusher to be reduced in size and passed to beneficiation. The amount of the critical RCO particles in the size consist in the mill is thereby reduced. The desired weight ratio of particles in the size consist is reestablished. The throughput of the mill is reestablished and maximum throughput at constant power is obtained.

In an example of the invention, it was desired to grind 0.6 ton of taconite ore per hour in a pilot plant autogenous grinding mill. The feed to the mill was as follows:

Particle Size in Size Consist in Mill RCF +6 inches 40% RMF 6,+3 inches 20% RFF 3 inches 40% The mill discharge was as follows:

Particle Size Dischar e from Autogenous Mi 1 RC0 +1 inch 11.3% RMO 1% inch 18.5% inch 15.4% RFO -46 inch 54.8%

The desired particle size for beneficiation was 200 mesh. The mill operated at about 13.4 KW hr./LT. of new feed. Increasing the amount of RCF particles in the size consist in the mill resulted in an increase of the inch particles in the output. The throughput of the mill was decreased to 0.51 tons per hour. The power to the mill was increased to 14.0 KW hr./LT. of new feed to increase throughput. In order to maintain the desired ratio in the size consist in the mill about 0.10 ton per hour of+1 inch size particles (RCO) from the output of the mill was recycled to the feed to the mill. The desired weight ratio of particles was reestablished in the mill. Throughput in the mill increased to 0.58 tons per hour and the mill power was 13.5 KW hr./LT. of new feed.

Adding an increased amount of RMF particles to increase an amount thereof in the size consist in the mill to more than 20 percent resulted in a drop in the throughput of the mill to 0.52 ton per hour, the power to the mill was increased to 13.8 KW hr./LT. of new feed. The amount of the RC0 particles in the mill output which was recycled to the mill was decreased to an amount which reduced the amount of this particle size in the mill to about 20 percent. Throughput of the mill increased 0.58 ton per hour. The power to the mill was reduced to 13.5 KW. hr./LT. of new feed.

In this specification and claims wherever percentages or ratios are referred to, such percentages and ratios are by weight unless otherwise noted.

lclaim:

1. An improvement in the method of autogenous grinding run-of-the-mine ore in which the feed to said mill is ore having relatively coarse particles, relatively medium particles and relatively fine particles, the ore discharged from said mill is classified into relatively coarse particles, relatively medium particles and relatively fine particles, and the relatively fine particles discharged from said mill are passed to beneficiation, the improvement comprising passing that portion of the ore discharged from said mill and classified as relatively coarse particles to storage and intermittently feeding a portion of the relatively coarse particles from storage to said mill to control the ratio of the amount of relatively coarse particles, relatively medium particles and relatively fine particles in the size consist in the mill.