U.S. patent number 3,708,206 [Application Number 05/056,373] was granted by the patent office on 1973-01-02 for process for leaching base elements, such as uranium ore, in situ.
This patent grant is currently assigned to Union Carbide Corporation. Invention is credited to Robert A. Hard, Robert L. Ripley.
United States Patent |
3,708,206 |
Hard , et al. |
January 2, 1973 |
PROCESS FOR LEACHING BASE ELEMENTS, SUCH AS URANIUM ORE, IN
SITU
Abstract
This invention relates to a process for leaching base elements,
such as uranium values, from an underground water saturated ore
deposit containing oxidizable materials such as sulfides, carbon
and the like. An oxygen bearing gas is introduced into the ore
deposit prior to or simultaneously with a leach solution to oxidize
the base elements within the ore deposit to a soluble state where
they can then be dissolved in the leach solution. Thereafter the
pregnant solution is withdrawn and treated by conventional
techniques to remove the base elements.
Inventors: |
Hard; Robert A. (Lewiston,
NY), Ripley; Robert L. (Niagara Falls, NY) |
Assignee: |
Union Carbide Corporation (New
York, NY)
|
Family
ID: |
22003957 |
Appl.
No.: |
05/056,373 |
Filed: |
July 20, 1970 |
Current U.S.
Class: |
299/5; 423/20;
423/17 |
Current CPC
Class: |
E21B
43/28 (20130101) |
Current International
Class: |
E21B
43/28 (20060101); E21B 43/00 (20060101); E21b
043/28 () |
Field of
Search: |
;299/4,5
;75/101,103,121 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Purser; Ernest R.
Claims
What is claimed is:
1. A process of leaching at least one base element selected from
the group consisting of uranium, copper, nickel, molybdenum,
rhenium and selenium, from an underground body of ore, in situ,
which is saturated with ground water comprising:
a. drilling at least one well into the underground body of ore;
b. casing and sealing said well;
c. introducing an oxygen bearing gas through at least one well into
a zone in said ore body surrounding the well so that the oxygen
bearing gas can contact and oxidize the base element in said zone
of the ore body;
d. discontinuing said introduction of the oxygen bearing gas;
e. subsequently introducing a leach solution into said oxygen
treated zone to dissolve the solubilized base element therein;
f. recovering the pregnant leach solution containing the dissolved
base element from at least one well; and
g. treating said pregnant leach solution to extract the base
element values therefrom.
2. The process of claim 1 wherein said oxygen bearing gas is
introduced into the zone in said ore body in the form of a
oxygenated foam.
3. The process of claim 2 wherein said base element is uranium.
4. The process of claim 1 wherein said oxygen bearing gas in step
(c) is introduced under pressure, said pressure determined by the
permeability, depth of ore deposit, hydrostatic head pressure,
extent of ore formation and rate of oxidation of the ore so that
the volume of the zone penetrated by the oxygen bearing gas will be
substantially confined to a zone that the leach solution can
contact and be recovered from without being essentially diluted
with ground water.
5. The process of claim 4 wherein said oxygen bearing gas is
selected from a group consisting of air, oxygen and mixtures
thereof.
6. The process of claim 5 wherein the leach solution is introduced
into at least one well and recovered from at least one different
well located within the oxidized treated zone.
7. The process of claim 5 wherein after step (d) the step of
maintaining the pressure on the oxygen bearing gas during
introduction of the leach solution is added.
8. The process of claim 7 wherein said base element is uranium.
9. The process of claim 5 wherein said leach solution is selected
from a group consisting of ammonium carbonate, sodium carbonate and
sulfuric acid.
10. The process of claim 9 wherein said leach solution is saturated
with an oxygen bearing gas under pressure.
11. The process of claim 10 wherein said base element is
uranium.
12. The process of claim 9 wherein said leach solution is
supersaturated with an oxygen bearing gas with respect to the
hydrostatic ground water pressure.
13. The process of claim 12 wherein said base element is
uranium.
14. A process of leaching at least one base element selected from a
group consisting of uranium, copper, nickel, molybdenum, rhenium
and selinium, from an underground body of ore, in situ, which is
saturated with ground water comprising:
a. drilling at least one well into the underground body of ore;
b. casing and sealing said well;
c. introducing under pressure a leach solution saturated with an
oxygen bearing gas into at least one well so that the solution will
displace the ground water in a zone of the ore body surrounding the
well so that the oxygen bearing gas can contact and oxidize the
base element therein and the leach solution can contact and
dissolve the solubilized base element so formed;
d. recovering the pregnant leach solution containing the dissolved
base element from at least one well; and
e. treating said pregnant leach solution to extract the base
element values therefrom.
15. The process of claim 14 wherein the leach solution is
introduced into at least one well and recovered from at least one
different well located within the zone.
16. The process of claim 14 wherein the oxygen bearing gas is
selected from a group consisting of air, oxygen and mixtures
thereof.
17. The process of claim 16 wherein the leach solution is selected
from a group consisting of ammonium carbonate, sodium carbonate and
sulfuric acid.
18. The process of claim 17 wherein said base element is
uranium.
19. The process of claim 14 wherein the leach solution is
supersaturated with an oxygen bearing gas with respect to the
hydrostatic ground water pressure.
20. The process of claim 19 wherein said oxygen bearing gas is
selected from a group consisting of air, oxygen and mixtures
thereof, and wherein said leach solution is selected from a group
consisting of ammonium carbonate, sodium carbonate and sulfuric
acid.
21. The process of claim 20 wherein said base material is uranium.
Description
FIELD OF THE INVENTION
This invention relates to a method for recovering at least one base
element selected from a group consisting of uranium, copper,
nickel, molybdenum, rhenium and selenium, from underground water
saturated ore bodies, in situ, which contain oxidizable materials
such as sulfides, carbon and the like. More specifically, the
invention is directed to an improved method for economically
solubilizing at least one base element, such as uranium, in
underground ore bodies by utilizing an oxygen bearing gas in
conjunction with a leach solution.
DESCRIPTION OF THE PRIOR ART
Presently many uranium and similar mineral mines, located
throughout the Western United States, are not in a position to be
commercially developed because of their low ore concentration
and/or because they are located at remote regions which makes them
economically unfeasible for conventional type exploitation. Even
ore bodies possessing relatively high ore concentration and located
in accessible regions may have its valuable deposit at a depth that
conventional mining may not be mechanically or economically
feasible.
In recent years a process for tapping these underground ore bodies,
in situ, has evolved which has resulted in recovering some mineral
values which were formally considered inaccessible by conventional
mining techniques. The process consists mainly of drilling a well
into an underground ore deposit and then introducing a leach
solution to contact the ore therein. The leach solution dissolves
the mineral within the ore deposit and thereafter the pregnant
solution is recovered and processed by conventional extraction
means to recover the particular mineral values therefrom.
However certain preliminary requirements or steps are necessary
before the leaching process of minerals, in situ, can be employed.
For example, when uranium is to be extracted, the following
preliminary information is required:
A. Does the uranium ore occur in a relatively horizontal bed and is
it located below the static water level?
B. What is the direction and velocity of the regional water
flow?
C. What does a mineralogy test of a sample of the ore reveal as to
its characteristics and composition?
The latter information is required so that an intelligent
evaluation of the amenability of the ore to different leaching
solutions can be made.
At the present time, leaching of minerals, such as uranium, in
underground ore bodies, using an acidic leach solution, has been
accomplished with some success. One of the primary obstacles
encountered, however, is the fact that when leaching uranium, in
situ, it is usually present in the tetravalent state and is
therefore not amenable to dissolution in an acidic leach solution.
Chemical oxidizing agents are presently incorporated in the leach
solution to convert, by oxidation, the uranium from its tetravalent
state to a soluble hexavalent state which can then be easily
dissolved in the leach solution.
The use of chemical oxidizing agents in leach solutions is
effective in many respects but has the disadvantage of being a
relatively high price raw material. In ore deposits containing
significant amounts of readily oxidizable materials other than the
base elements, e.g., carbon and sulfur in the form of sulfides, the
high cost necessary to extract the base elements by use of chemical
oxidizing agents has economically made them inaccessible.
To economically leach these base elements from underground deposits
containing other oxidizable materials, it is necessary to oxidize
the base elements without consuming excessive amounts of the
expensive chemical oxidizing agents or to use a low-cost oxidizing
agent that will not provide a financial penalty from the
co-oxidation of the oxidizable materials along with the base
elements. Since it is almost impossible to selectively oxidize the
base elements without consuming the oxidizing agent on other
materials found with the base elements in ore deposits, most
chemical oxidants are economically ruled out.
The present invention is therefore directed to an improved method
in which an oxygen bearing gas is economically used as the oxidant
in a leaching process for the recovery of at least one base
element, such as uranium, located in an underground ore body below
the static water level.
SUMMARY OF THE INVENTION
This invention relates to an improved method for recovering at
least one base element selected from the group consisting of
uranium, copper, nickel, molybdenum, rhenium and selenium, from an
underground ore body containing oxidizable materials, such as
carbon and sulfides, and which is located below the static water
level. Specifically, an oxygen bearing gas is introduced, under
pressure, prior to and/or simultaneously with a leach solution,
into an ore bed to convert the relatively insoluble state of a
deposited base element in the ore to the solubilizable state. The
method of bringing this relatively inexpensive oxidizing agent in
sufficient quantities to the ore is extremely important when the
ore contains the base element in addition to other oxidizable
materials, such as, carbon and sulfur in the form of various
sulfides, since a percentage of the oxidant will be consumed in the
oxidation of these materials. In addition, it is believed, although
not factually proven, that the use of a pressurized oxygen bearing
gas will penetrate into the ore body better than expensive chemical
oxidizing agents and thereby possibly fracture crevices in the ore
body thus exposing a greater surface of the base element for
extraction.
With basic compounds, such as limestone or other carbonates,
present in the ore deposit, an acidic leach solution can not be
economically employed since a large proportion of the acidic
solution would be consumed by the carbonates. A basic leach
solution, such as ammonium carbonate or sodium carbonate, in
conjunction with an oxygen bearing gas such as oxygen, air and any
and all mixtures thereof form the principal ingredients of the
leaching process of this invention.
Although the process of this invention is directed to the leaching
of a variety of base elements from underground ore bodies, the
discussion hereinafter will be directed to the leaching of uranium,
in situ, which will serve as an example to explain how the process
could be implemented to increase the recovery of the base elements
from underground ore bodies.
To increase the recovery of uranium values from an underground ore
body, it is necessary to convert the relatively insoluble
tetravalent state of the uranium in the ore to the solubilizable
hexavalent state.
The complete dissolution of uranium in a carbonate solution occurs
in two steps, either of which may be considered rate-controlling
for the recovery of uranium values. The first reaction involves the
oxidation of uranium by absorbing oxygen and the second reaction is
the dissolution of the oxidized uranium in a carbonate solution.
The rate of dissolution of the latter reaction is dependent upon
the surface area of the uranium exposed and the concentration of
the carbonate ion in solution. With both reactions assumed to be
rate-controlling, a finding that in a particular leach process the
carbonate ion concentration is having little effect would indicate
that the rate-controlling step is in the oxidation reaction. To
increase the recovery of uranium values, the oxygen concentration
would have to be increased which requires the pressure of the
oxygen to be increased so that a sufficient supply of oxygen will
be available to convert the uranium into its soluble tetravalent
state. On the other hand, if oxygen pressure has little or no
effect on the percentage of uranium being recovered, then the
dissolution reaction is the rate-controlling step. To increase the
percentage of uranium recovery, the carbonate ion concentration has
to be increased to a sufficient level in the leach solution to
dissolve all the uranium in the hexavalent state.
The proper analysis of an ore body, along with the effect produced
by varying the oxygen pressure and carbonate concentration in the
leach solution, can be used to provide the optimum combination of
these ingredients for recovering maximum uranium from the ore body.
However, a limiting factor in deciding the pressure is to limit it
to a value at which rock failure and/or ground level uplift occurs.
In addition the pressure limitation should depend on the
permeability, depth of ore deposit, hydrostatic head pressure,
extent of ore formation and rate of oxidation of the ore so that
the volume penetrated by the oxygen bearing gas will be
substantially confined to a zone that the leach solution can
contact and be recovered from without being essentially diluted
with ground water.
The object of this invention, as exemplified by the leaching of
uranium, in situ, will be apparent from the following description
and claims taken in conjunction with the drawings of FIGS. 1
through 3.
FIG. 1 is a cross-sectional elevated view of an arrangement
suitable for the practice of this invention which shows a well
communicating with an ore body for introducing of reagents;
FIG. 2 shows a modification of the arrangement of FIG. 1 wherein a
pressurized casing cap is added so that the leach solution can be
injected while holding the oxygen bearing gas under pressure.
FIG. 3 shows another arrangement of FIG. 1 whereby pressurizing
means is added for supersaturating a leach solution with an oxygen
bearing gas with respect to the hydrostatic ground water
pressure.
The preliminary step to be conducted in the leaching operation of
this invention is to test and analyze a sample of the ore body so
as to ascertain the extent of its mineral contents. A lithological
study of the ore body will reveal the porosity and permeability of
the ore and the materials surrounding it. One method presently
employed for this purpose is to drill out cores of the ore
formation at different depth intervals and then have the cores
chemically analyzed to determine permeability and ore level
formation.
Once this information is obtained and evaluated, and found to
contain uranium, a well bore is drilled into the ore body. An
oxygen bearing gas is then introduced, under pressure, through the
well into the uranium ore body located below the ground water
level. Although the exact mechanism occuring in the ore body is not
known, and since we don't want to be bound by theory, we are of the
opinion that the oxygen bearing gas enters the ore body in the form
of at least one large bubble which displaces the ground water about
the well. This exposes the ore body in a zone surrounding the well
to the oxygen bearing gas which oxidizes the ore, such as uranium,
into a soluble state. A leach solution is thereafter introduced
into this oxygen treated ore zone to dissolve the uranium therein
and then the solution is recovered and treated by conventional
means to extract the uranium values.
In a particular embodiment for practicing this invention, as shown
in FIG. 1, a conventional well bore 10 is drilled from surface 20
into an underground body of uranium ore 30 which is located below
the static water level 25 and sandwiched between impermeable clay
seams 80 and 85. A casing tube 40 is positioned within and spaced
from well 10 and terminated at a depth indicated by 45 which is
within horizontal ore body 30. A slotted member 50, such as a
screen or other similar arrangement, forms the lower extremity of
casing 40 and extends in a downward direction through ore body 30.
The length of the slotted member 50 depends upon the depth of ore
body 30.
A water permeable material 75, such as sized gravel or the like is
placed in annular cavity 70 between slotted member 50 and well bore
10, for the entire length of slotted member 50.
Annular cavity 60, between well 10 and casing 40, is sealed its
entire length down to slotted member 50. Any suitable sealer 65 can
be used such as cement or a solution of chemical gel which can be
triggered to solidify once in position.
Compressor means 15 is coupled to diffuser 55 and together they are
used to force feed the oxygen bearing gas, under pressure, through
casing 40 into zone 35 surrounding screen member 50. During this
injection feed it may be necessary to cap the casing, as shown in
FIG. 2, so as to force the gas into zone 35. The exact contour of
zone 35 is not known, but it is believed that the pressurized
oxygen bearing gas displaces the water surrounding screen member 50
in a radially outward direction forming a somewhat circular to
cylindrical zone 35. The size of zone 35 is variable and depends
among other things on the porosity of the ore body, the presence of
impermeable clay zones, the flow rate of the ground water and the
pressure produced by the static head or through pumping.
In zone 35, the uranium values in the ore are contacted with the
oxygen bearing gas which converts the uranium from the tetravalent
state to the soluble hexavalent state in the same general manner as
provided through the use of chemical oxidizing agents. After
sufficient time has elapsed for this uranium conversion to occur,
the pressure on the gas can be released and the ground water
permitted to return into zone 35. The time for oxidizing the
uranium in the ore body is a function of the physical and chemical
properties of the ore body.
Thereafter a leach solution containing ammonium carbonate, sodium
carbonate or sulfuric acid, depending upon the nature of the ore
body, is introduced into well casing 40 by gravity or by using, for
example, pump 90. The leach solution passes through well casing 40
and slotted member 50 into the water saturated, oxygen treated ore
body 30. The solution displaces the ground water surrounding screen
member 50 in approximately the location of previously established
oxygen treatment zone 35. The leach solution reacts with and
dissolves the previously oxidized hexavalent uranium values and is
subsequently withdrawn by means of submersible pump 95. The
pregnant leach solution is thereafter treated by conventional
techniques to recover the uranium values.
In a further embodiment of the invention, as shown in FIG. 2 with
some members identical to those shown in FIG. 1 and numbered
accordingly, a pressure casing cap 100 is disposed on casing 40 to
maintain pressure within the casing. Thus the pressurized oxygen
bearing gas from compressor means 15 can be held under pressure
while the leach solution is injected into zone 35 by means of pump
90.
In the operational mode an oxygen bearing gas, under pressure, is
introduced into zone 35 to oxidize the uranium contained in ore
zone 30. After a sufficient oxidation period has elapsed, the
pressure on the oxygen bearing gas can be maintained while a leach
solution is introduced from pump 90 through well casing 40 into
zone 35. The advantage of maintaining the pressure on the oxygen
bearing gas during the introduction of the leach solution is that
the gas could possibly form somewhat of a barrier between the leach
solution and the ground water thus decreasing the likelihood of
dilution of the former with the latter. In addition, with an oxygen
bearing gas present in sufficient quantity during the dissolution
of the hexavalent uranium values, newly exposed or unoxidizable
tetravalent uranium values can be oxidized and immediately
dissolved in the leach solution.
It is also possible with this arrangement to introduce the oxygen
bearing gas first and then after releasing the pressure to
reintroduce an additional supply of the oxygen bearing gas at the
same time as introducing the leach solution. This will provide a
leach solution saturated with the oxygen bearing gas in zone 35
during the dissolution of the hexavalent uranium values.
Another embodiment of the invention, as shown in FIG. 3 and having
some members identical to those shown in FIG. 2 and numbered
accordingly, employs a pressurizing chamber 200 coupled to tube 205
having an enlarged injection pipe 210 at its lower portion. At the
lower extremity of pipe 210 is an expansion orifice 215. A leach
solution and an oxygen bearing gas is fed via pumps 90 and 15,
respectively, into compressor 200 which in turn injects a
leach-oxygenated foam into zone 35 via pipe 210 and orifice
215.
In the operational mode, a pressurized oxygen bearing gas and a
leach solution are introduced into pressurizing chamber 200 wherein
the leach solution is saturated with the pressurized oxygen bearing
gas. The solution is pumped through tube 205, pipe 210 and then
expands through orifice 215 whereupon a supersaturated oxygen foam
is created due to a drop in pressure. This oxygenated foam is fed
into zone 35 of ore body 30 in the form of a multiple of small
bubbles which contacts and oxidizes the uranium therein to the
hexavalent state which is then dissolved by the leach solution.
Thus, by having a leach-oxygenated foam solution introduced into
zone 35, the oxygen bearing gas can then be dispersed in a
multitude of small bubbles throughout ore body 30 in a manner
somewhat analagous to the effervescence associated with common
seltzer water. Although not factually known, it is believed that
the small bubbles penetrate further into the crevices in the ore
formation oxidizing the uranium into a more solubilized state
whereby it can be dissolved in the leach solution. By
supersaturating the leach solution with the oxygen bearing gas,
ample oxygen will be available in small bubbles for the oxidation
reaction of the uranium. It is also possible to precede the initial
introduction of the supersaturated solution with an oxidation step
wherein the oxygen bearing gas is introduced alone so as to prepare
the uranium for solubilization. Whether or not to add this initial
oxidation step will depend on the quality and concentration of the
uranium and other minerals in the ore body along with the physical
characteristics of the ore formation. Initial testing of an ore
deposit will usually provide sufficient information for determining
which approach to take, i.e., whether to employ the initial
oxidation step or not. As stated above, in some ore deposits large
quantities of oxidizable materials are present in addition to
uranium, and therefore it might be advantageous to include this
oxidation step since a portion of the oxygen would be consumed by
such materials.
Although FIG. 3 shows one approach to producing an oxygenated foam,
that is, dissolving oxygen in a leach solution at above atmospheric
pressure and then releasing the pressure on the solution at the
vicinity of the ore zone, any means for creating an oxygenated foam
can be used as long as the foam can produce a multiple of oxygen
bearing gas bubbles in the vicinity of the ore zone. For example,
any oxygen bearing medium which is capable of being injected into
the ore zone and thereafter, through chemical or physical
mechanism, produce an oxygenated foam can be used.
It is to be understood that this invention can be practiced by
using only one well for both introducing the reagents and then
recovering the pregnant solution therefrom. Also two or more wells
penetrating the ore body may be used so that the reagents can be
introduced into the ore body through at least one well and the
pregnant solution recovered from at least one different well.
EXAMPLE I
In the Palangana Dome section of Duval County, Texas, a uranium ore
body was located in a calcareous sandstone formation. Core samples
from a hole dug to a depth of 270 feet in the region were taken and
chemically analyzed. A lithology of the core samples revealed a
uranium ore zone about 7 feet thick sandwiched between layers of
green clay. A permeability analysis of the ore zone disclosed a
horizontal permeability between 600 to 1,900 millidarcys while the
permeability in the clay layers varied between 4 to 8 millidarcys.
The static ground water level was 100 feet below the ground
surface.
A 4 -foot cased and sealed well having a slotted member at its
lower end, as illustrated in FIG. 2, except that a composite of
bentonite and mud was used to seal the well to the upper clay
layer, was embedded into the ore formation. A positive displacement
pump was used to force air through the well into the uranium ore
body. The rate of air introduction was 40 scfm at psig of 100. This
was continued for 16 hours. Based on the porosity of the ore body
and observations at monitor wells located circumferentially around
the air carrying well, a zone containing about 23,000 cubic feet
and essentially free of ground water extended radially into the ore
body for about 29 feet from the air carrying well. The flow was
discontinued and ground water returned to the zone from which it
had been displaced. An aqueous leach solution containing 26 grams
per liter of ammonium carbonate, (NH.sub.4).sub.2 CO.sub.3, was
introduced with the ore body at a rate of 8.7 gallons per minute. A
total of 24,078 gallons of leach solution was introduced. After a
period of 3 days, the leach solution was withdrawn through the well
and analysis showed it to contain an average of 0.13 g/liter of
U.sub.3 O.sub.8 with a maximum grade of 0.30 g/liter. This compared
to an analysis of an average of 0.08 g/liter of U.sub.3 O.sub.8
with a maximum grade of 0.12 g/liter which was obtained following
essentially the same procedure except that the air treatment was
not used.
EXAMPLE II
In the Palangana Dome section of Duval County, Texas, an identical
ore formation as in Example I was located and a cased and sealed
well was embedded into the ore formation in an identical
manner.
A positive displacement pump was used to force oxygen through the
well into the uranium ore body. The rate of oxygen introduction was
69 scfm at psig of 104. This was continued for 9 hours and 42
minutes. Based on the porosity of the ore body and observations at
monitor wells located circumferentially around the oxygen carrying
well, a zone containing about 23,000 cubic feet and essentially
free of ground water extended radially into the ore body for about
29 feet from the oxygen carrying well. The flow was discontinued
and pressure was maintained in the well for 18 hours. At the end of
this period pressure on the well was released on ground water
returned to the zone from which it had been displaced. An aqueous
leach solution containing 23 grams per liter of ammonium carbonate,
(NH.sub.4).sub.2 CO.sub.3, was introduced into the ore body at a
rate of 11.8 gallons per minute. A total of 21,272 gallons of leach
solution was introduced after which the leach solution was
immediately withdrawn through the well and analysis showed it to
contain an average of 0.47 grams per liter of U.sub.3 O.sub.8 with
a maximum grade of 1.20 grams per liter. This compared to an
analysis of an average of 0.08 grams per liter of U.sub.3 O.sub.8
with a maximum of 0.12 grams per liter which was obtained following
essentially the same procedure except that the oxygen treatment was
not used.
Although the above examples are directed to the leaching of
uranium, in situ, it is to be understood that the process of this
invention, wherein an oxygen bearing gas is used as an oxidant for
underground leaching, can be utilized to leach other base elements
such as nickel, copper, molybdenum, rhenium and selenium. For
example, small quantities of the latter four elements were leached
out along with the uranium in the above examples. The exact per
cent of each of these elements recovered was not ascertained since
only miniscule amounts of each element was present in the original
ore body. However, if substantial amounts of these elements were
present in the ore body then the recovery of these elements would
have been noticeably increased using the process of this
invention.
The process of this invention is therefore intended for use where
an inexpensive oxidant is required prior to or along with a leach
solution for the purpose of oxidizing any of a number of base
elements within an ore body to a state that will be amenable to
solubilization. For example, when sulfides of nickel are present in
an ore body, the oxygen bearing gas will react with the NiS to form
NiSo.sub.4 which can then react with a leach solution, such as
NH.sub.3, to form Ni(NH.sub.3).sub.6.sup.+.sup.+ + SO.sub.4 ----.
This pregnant nickel-bearing solution can then be extracted from
the ore body and thereafter treated by conventional techniques to
remove the nickel values.
* * * * *