U.S. patent number 3,715,083 [Application Number 05/099,182] was granted by the patent office on 1973-02-06 for method for controlling the grind in a single stage autogenous grinding mill.
This patent grant is currently assigned to Bethlehem Steel Corporation. Invention is credited to Robert M. Funk.
United States Patent |
3,715,083 |
Funk |
February 6, 1973 |
METHOD FOR CONTROLLING THE GRIND IN A SINGLE STAGE AUTOGENOUS
GRINDING MILL
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.
Inventors: |
Funk; Robert M. (Allentown,
PA) |
Assignee: |
Bethlehem Steel Corporation
(N/A)
|
Family
ID: |
22273368 |
Appl.
No.: |
05/099,182 |
Filed: |
December 17, 1970 |
Current U.S.
Class: |
241/24.1 |
Current CPC
Class: |
B02C
25/00 (20130101) |
Current International
Class: |
B02C
25/00 (20060101); B02c 017/00 () |
Field of
Search: |
;241/24,33,34,69,79,80,97 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Custer, Jr.; Granville Y.
Claims
I claim:
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.
Description
BACKGROUND OF THE INVENTION
This invention is directed to an improvement in the method of
preparing coarse, friable ore containing metal values, such as
iron, for beneficiation to recover said metal values. Specifically,
the invention is directed to a method of controlling the grind of a
raw friable run-of-the-mine ore in an autogenous mill by
controlling 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 fine output (RFO). The size of the RFO particles is less
than the size of the RFF particles. The size of the RMO particles
is most comparable in size to the RFF particles, and the size of
the RCO 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 RCO 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-of-the-mine ore
feed to the mill and/or an increase in the power to the mill is
required to maintain production. In 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 the autogenous
grinding mill wherein maximum throughput at constant power to the
mill is maintained.
It is another object of this invention to provide a method for
grinding raw friable run-of-the-mine ore in an autogenous grinding
mill wherein the ratio of relatively coarse, relatively medium and
relatively fine particles in the size consist in the mill is
controlled to obtain optimum efficiency in the mill.
SUMMARY OF THE INVENTION
Broadly, the method of the invention comprises controlling 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. 1 is a schematic view of the autogenous grinding mill circuit
of the invention.
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 run-of-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 10 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 found that for optimum
grinding efficiency, that is, 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 20 percent to about 30 percent
particles having a size -6,+3 inch and about 35 to about 40 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 controlling 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) +1 inch, relatively medium (RMO) -1,+3/8
inch and relatively fine (RFO) -3/8 inch. The size consist of the
output from the mill is as follows:
Output from Particle Size Size Autogenous Mill
__________________________________________________________________________
Coarse +1 inch 7.5% Medium -1,+3/8 inch 27.5% Fine -3/8 inch
75.0%
I have found that the RCO particles are a critical size. The RCO
particles are stored in hopper 15. The amount of the RCO particles
recycled to the mill is, therefore, easily controlled thereby
controlling the size consist in the mill. All the RMO and RFO
particles are passed to beneficiation processes (not shown).
As shown in FIG. 2, a variation in the practice of the invention,
the RCO particles, that is, the particles +1 inch, from the mill
output are passed to storage. Substantially all RMO particles
(-1,+3/8 inch) in the output are recycled to the mill and the RFO
particles (-3/8 inch) are passed to further processing, for
example, secondary grinding, froth flotation and/or magnetic
separation to recover the metal values therein.
If an imbalance in the size consist in the mill occurs, 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 RCO 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 RCO 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 mill will 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
imbalance, the portion of the RCO 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 % Discharge from Autogenous Mill RCO +1 inch 11.3%
RMO (+1/2 inch 18.5% (+3/8 inch 15.4% RFO -3/8 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 -3/8 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 RCO 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.
* * * * *