U.S. patent application number 14/386222 was filed with the patent office on 2015-02-19 for production method for hematite for iron production.
The applicant listed for this patent is Sumitomo Metal Mining Co., Ltd.. Invention is credited to Yasumasa Kan, Hiroyuki Mitsui, Hideki Sasaki.
Application Number | 20150050200 14/386222 |
Document ID | / |
Family ID | 49222305 |
Filed Date | 2015-02-19 |
United States Patent
Application |
20150050200 |
Kind Code |
A1 |
Sasaki; Hideki ; et
al. |
February 19, 2015 |
PRODUCTION METHOD FOR HEMATITE FOR IRON PRODUCTION
Abstract
Provided is a production method for refining iron oxide
(hematite), which has such a low sulfur content as to be used as a
raw material for ironmaking from a leach residue containing iron
oxide, the leach residue being produced by a high pressure acid
leach (HPAL) process and being a raw material that can be cheaply
and stably procured. In the method of producing (high purity)
hematite for ironmaking by a process of adding an oxidant and
sulfuric acid to nickel oxide ore and then leaching nickel, a leach
residue obtained after the leaching of nickel is heated to
600.degree. C. or more, and preferably 800.degree. C. or more and
1400.degree. C. or less.
Inventors: |
Sasaki; Hideki; (Minato-ku,
JP) ; Mitsui; Hiroyuki; (Minato-ku, JP) ; Kan;
Yasumasa; (Minato-ku, JP) |
|
Applicant: |
Name |
City |
State |
Country |
Type |
Sumitomo Metal Mining Co., Ltd. |
Tokyo |
|
JP |
|
|
Family ID: |
49222305 |
Appl. No.: |
14/386222 |
Filed: |
January 16, 2013 |
PCT Filed: |
January 16, 2013 |
PCT NO: |
PCT/JP2013/050671 |
371 Date: |
September 18, 2014 |
Current U.S.
Class: |
423/150.1 |
Current CPC
Class: |
C22B 3/20 20130101; C01G
49/06 20130101; Y02P 10/20 20151101; C22B 23/0461 20130101; C01B
17/507 20130101; Y02P 10/234 20151101; C01P 2006/80 20130101; C22B
3/22 20130101 |
Class at
Publication: |
423/150.1 |
International
Class: |
C22B 3/22 20060101
C22B003/22 |
Foreign Application Data
Date |
Code |
Application Number |
Mar 19, 2012 |
JP |
2012-062794 |
Claims
1. A method of producing high purity hematite for ironmaking
comprising: adding an oxidant and sulfuric acid to nickel oxide ore
leaching nickel after adding the oxidant and sulfuric acid to the
nickel oxide ore; and heating a leach residue obtained after the
leaching of nickel to 600.degree. C. or more.
2. A method of producing high purity hematite for ironmaking
comprising: adding an oxidant and sulfuric acid to nickel oxide
ore; leaching nickel after adding the oxidant and sulfuric acid to
the nickel oxide ore; and heating a leach residue obtained after
the leaching of nickel to 800.degree. C. or more and 1400.degree.
C. or less.
Description
BACKGROUND
[0001] 1. Field of the Invention
[0002] The present invention relates to a production method for
refining a leach residue obtained by hydrometallurgical refining of
nickel oxide ore into hematite that can be used as an iron-making
raw material and has low-grade sulfur.
[0003] 2. Description of the Related Art
[0004] In steel smelting, a method of charging iron ore containing
iron oxide into a blast furnace along with a reductant such as
coke, heating and melting the iron ore under a reducing atmosphere
to obtain crude steel, and refining the crude steel in a converter
to obtain desired steel has been used.
[0005] The iron oxide that is a raw material of the steel is a
limited resource, and furthermore it is gradually hard to obtain
high-quality iron ore required to maintain a quality of steel.
[0006] Meanwhile, with respect to nickel becoming a raw material of
stainless steel, technology for smelting low-grade oxide ore as a
raw material due to a tendency toward resource exhaustion of
sulfide ore that has been used in the past has been developed and
put to practical use.
[0007] To be specific, nickel oxide ore such as limonite or
saprolite is put into a pressure device such as an autoclave along
with a sulfuric acid, and nickel is leached under high pressure and
high temperature of about 240 to 260.degree. C.
[0008] The nickel leached into a solution of the sulfuric acid is
used as nickel metal or a nickel salt compound by adding a
neutralizer to neutralize a surplus acid, separating a leach
residue by solid-liquid separation, separating impurities to
recover the leach residue as an intermediate raw material in the
form of hydroxide or sulfide, and further refining the intermediate
raw material.
[0009] In such a process called high pressure acid leach (HPAL),
nickel can be almost completely leached even from low-grade ore in
which valuable metals intended for recovery are contained by not
more than 1% to 2% by weight (hereinafter indicated by "%" with
regard to a grade). Further, the HPAL process has a feature of
concentrating the valuable metals up to the same grade as a
conventional raw material by producing an intermediate raw material
from a leachate, and refining the nickel in a process similar to a
conventional process.
[0010] Further, the HPAL process may be applied to various types of
ores such as nickel sulfide ore, copper sulfide ore, and copper
oxide ore, in addition to the nickel oxide ore.
[0011] Further, a main component of the leach residue obtained by
the HPAL process is iron oxide having the form of hematite. This is
secondarily obtained because each of oxide ore and sulfide ore of
nickel or copper used as a raw material contains iron of an amount
far more than a content of nickel or copper.
[0012] These leach residues are created at a high temperature, and
thus have the form of oxide that is chemically or environmentally
stable. However, the leach residues have no special utility value,
and have been scrapped to a residue disposal yard. For this reason,
it has been a grave challenge how to secure the disposal yards for
an enormous amount of leach residues generated along with the
smelting.
[0013] Furthermore, the leach residue of the HPAL process cannot be
directly used for the aforementioned iron-making raw material. The
reason is that the leach residue of the HPAL process contains
gangue and impurities, particularly sulfur, in addition to the iron
oxide and requires exhaust gas treatment, and thus is not suitable
for the raw material used in the conventional iron-making process
in common.
[0014] Particularly, a grade of sulfur in iron oxide usable for the
iron-making raw material differs depending on facility capacity and
an amount of production of individual ironworks, and generally
needs to be suppressed to less than 1%.
[0015] The sulfur is hardly contained in the original nickel oxide
ore. Nevertheless, the sulfur contained in the leach residue by
about 1 to 3% results from calcium sulfate (plaster) generated by
reaction of sulfuric acid and limestone or slaked lime added as the
neutralizer in order to neutralize free sulfuric acid remaining at
the leach slurry.
[0016] Therefore, it is considered that what creates a soluble salt
may be used as the added neutralizer, not the slaked lime or what
forms insoluble sediment, such as the slaked lime, after the
neutralization.
[0017] For example, the neutralizer suitable for such application
includes sodium hydroxide, potassium hydroxide, magnesium
hydroxide, and magnesium oxide.
[0018] However, these neutralizers are expensive, and have a
limited amount of production. Thus, when a large quantity of
neutralizer is required as in the HPAL process, it is industrially
difficult to cover the whole quantity.
[0019] For this reason, there has been no choice but to use a
calcium-based neutralizer in whole or in part which forms the
insoluble sediment after the neutralization as described above, and
thereby mixing of the sulfur has been inevitable. As such, it has
been impossible to process the leach residue created in the HPAL
process into the hematite and to use it as the iron-making raw
material.
[0020] On the other hand, a method of separating sulfur in jarosite
using a pressure device such as an autoclave is also known.
[0021] For example, JP H03-176081 A discloses a method that
includes stirring a jarosite-containing residual and a zinc sulfide
inclusion in an autoclave at least under oxygen partial pressure of
1000 kPa at a temperature of 130 to 170.degree. C. along with a
free sulfuric acid of 40 to 100 g/l, substantially dissolving iron
and zinc fractions of a concentrate containing the residual and
zinc sulfide, introducing the solution into a leach circulation
passage for zinc electrolysis to settle iron in the form of
hematite, and separating sulfur from the above solid, and supplying
the residual for separate application.
[0022] However, this method requires an expensive device such as an
autoclave, increases a facility cost, and further has a problem
even in the aspect of productivity.
[0023] The invention is intended to provide a production method for
refining hematite, which has such a low sulfur component as to be
used as an iron-making raw material, from a leach residue
containing iron oxide produced by a high pressure acid leach (HPAL)
process.
SUMMARY OF THE INVENTION
[0024] To solve the above problems, a first aspect of the present
invention provides a method for producing (high purity) hematite
for ironmaking by a process of adding an oxidant and sulfuric acid
to nickel oxide ore and then leaching nickel. The method further
includes heating a leach residue, which is obtained after the
nickel is leached, to 600.degree. C. or more.
[0025] A second aspect of the present invention provides a method
for producing (high purity) hematite for ironmaking by a process of
adding an oxidant and sulfuric acid to nickel oxide ore and then
leaching nickel. The method further includes heating a leach
residue, which is obtained after the nickel is leached, to
800.degree. C. or more and 1400.degree. C. or less.
[0026] The present invention can bring about several industrially
significant effects.
[0027] First, is possible to easily obtain hematite that has
low-grade sulfur and can be used as an iron-making raw
material.
[0028] Second, a raw material that can be cheaply and stably
procured is used. Thus, hematite with the low-grade sulfur can be
obtained inexpensively.
[0029] Third, wastes, such as a leach residue, discharged in a
refining process can be applied to the iron-making raw materials,
and it is thus possible to remarkably reduce an amount of the
scrapped leach residue and further reduce production costs by
lowering an environmental risk, reducing scrapping costs, and
reducing construction costs of a leach residue disposal yard;
and
[0030] Fourth, when hematite with the low-grade sulfur is produced,
a special facility is not required, and thus establishment of its
producing process is easy.
BRIEF DESCRIPTION OF DRAWINGS
[0031] FIG. 1 is a flow chart showing a recovery process of
performing high-pressure sulfuric acid leach on a mineral
containing valuable metals and iron to recover the valuable metals,
and further showing a refining process of hematite having low-grade
sulfur which is associated with the recovery process; and
[0032] FIG. 2 is a diagram illustrating a relation between a
heating temperature and a grade of sulfur in a leach residue.
DETAILED DESCRIPTION
[0033] The present invention is to heat a leach residue obtained
when a mineral, such as nickel oxide ore, containing valuable
metals and iron is subjected to high-pressure sulfuric acid leach,
to separate sulfur, and to produce high-purity hematite that can be
used as an iron-making raw material having a low sulfur
content.
[0034] FIG. 1 illustrates a flow for a recovery process of
performing high-pressure sulfuric acid leach on a mineral, such as
nickel oxide ore, containing valuable metals and iron to recover
the valuable metals and a further flow for a refining process of a
production method according to the present invention of producing
hematite having low-grade sulfur from a leach residue obtained in
association with the recovery process.
[0035] The flow for the recovery process of the valuable metals is
indicated by an outline arrow, and the flow for the refining
process of the hematite according to the invention is indicated by
a black arrow.
Refining Process of Hematite
[0036] A leach residue to be a starting raw material of the present
process is obtained as sediment when a leach slurry, which is
generated by neutralizing a leachate obtained in the event of
high-pressure sulfuric acid leach as illustrated in FIG. 1, is
subjected to solid-liquid separation. As such, the leach residue is
formed in a state in which a reaction product of a neutralizer
input in the neutralization process and a surplus acid is
contained. Accordingly, limestone or slaked lime added as the
neutralizer and sulfuric acid are reacted to neutralize a free
sulfuric acid remaining in the leach slurry. Thereby, the leach
residue contains sulfur resulting from created calcium sulfate
(plaster) by several percentage (%).
Heating of Leach Residue
[0037] Therefore, as a method of separating a sulfur component from
such a leach residue containing several percentage of sulfur, the
leach residue is heated on given conditions. That is, as
illustrated in FIG. 1, the iron oxide (hematite) for ironmaking
which has low-grade sulfur is refined by roasting the leach residue
and evaporating the sulfur component.
[0038] FIG. 2 illustrates a relation between a heating temperature
and the sulfur grade in the leach residue.
[0039] A temperature at which the leach residue is heated is
600.degree. C. or more, preferably 800.degree. C. or more, which is
an effective temperature in order to make the sulfur grade in the
leach residue less than 1%. Further, when the heating temperature
exceeds 800.degree. C., the sulfur grade is sharply reduced, which
is more preferable. When the heating temperature becomes
1300.degree. C., the sulfur grade can be reduced up to 0.1% or
less, which is more preferable, but when the heating temperature
more preferably exceeds 1400.degree. C., this gives no great
difference, and is not very preferable in the aspect of facility
investment such as an increase in heating energy or a need for heat
resistance of a furnace wall material. Accordingly, the heating
temperature is 600.degree. C. or more and 1400.degree. C. or less,
and preferably 800.degree. C. or more and 1300.degree. C. or
less.
[0040] A heating time is affected by a furnace size and an amount
of the residue, and thus may be adequately adjusted. Further, the
heating is performed in an oxidizing atmosphere such as atmospheric
air. Thereby, along with the heating, the sulfur is removed from
the leach residue as sulfur dioxide, and the high-purity iron oxide
(hematite) is formed.
EXAMPLES
[0041] Hereinafter, the invention will be described using
examples.
Example 1
[0042] Nickel oxide ore having 1% nickel grade and 46 to 48% iron
grade was adjusted to be a slurry of 30 to 40% by weight, and then
was mixed with sulfuric acid of 64% by weight. Subsequently, the
slurry was charged into a pressure device, heated to 240 to
250.degree. C., and maintained for one hour, and a leachate was
obtained by leaching nickel in the ore (HPAL).
[0043] After the leaching, the leachate was cooled to about
70.degree. C., and then slaked lime was added to neutralize a
surplus acid (neutralization). The slurry containing a leach
residue after the surplus acid was neutralized (hereinafter the
leach residue after the neutralization is referred to as
"neutralized residue`) was subjected to solid-liquid separation
using Nutsche and a filtering bottle, and was separated into the
leachate and the neutralized residue (solid-liquid separation).
[0044] In the neutralized residue, an iron grade was 49.9%, and a
sulfur grade was 1.5%.
[0045] Next, the neutralized residue was equally divided into six
parts, which were respectively raised to 30.degree. C., 200.degree.
C., 800.degree. C., 1000.degree. C., 1200.degree. C., and
1400.degree. C., heated for one hour, and cooled.
[0046] The sulfur grade of the leach residues after the cooling
were analyzed, and the analyzed results were illustrated in FIG.
2.
[0047] As illustrated in FIG. 2, it is found that the sulfur grade
is reduced up to about 1% at about 600.degree. C., and that, when
the temperature exceeds 800.degree. C., the sulfur grade is sharply
reduced, and the sulfur can be effectively separated.
[0048] In Table 1, results of measuring the iron and sulfur grades
in the neutralized residue after the heating are illustrated. The
iron and sulfur grades were measured by fluorescent X-ray
analysis.
TABLE-US-00001 TABLE 1 Sulfur grade Sample [% by weight] Supply
Neutralized residue 1.5 Heating 800.degree. C. 0.8 1000.degree. C.
0.4 1200.degree. C. 0.2
[0049] With this use of the invention, it is possible to separate
the sulfur from the HPAL leach residue, and to refine the hematite
so as to be usable as the raw material for ironmaking.
DRAWINGS
[0050] FIG. 1 [0051] 1: NICKEL OXIDE ORE [0052] 2: SULFURIC ACID
[0053] 3: LEACHATE [0054] 4: NEUTRALIZER [0055] 5: NEUTRALIZATION
[0056] 6: LEACH SLURRY [0057] 7: SOLID-LIQUID SEPARATION [0058] 8:
NEUTRALIZED RESIDUE [0059] 9: ROASTING [0060] 10: IRON OXIDE FOR
IRONMAKING [0061] 11: SULFUR [0062] 12: LEACHATE [0063] 13:
VALUABLE METALS
[0064] FIG. 2 [0065] 1: SULFUR GRADE IN RESIDUE [0066] 2:
TEMPERATURE
* * * * *