AU2018218644B2

AU2018218644B2 - Metal oxide smelting method

Info

Publication number: AU2018218644B2
Application number: AU2018218644A
Authority: AU
Inventors: Yukihiro GODA; Takashi Iseki; Jun-Ichi Kobayashi; Shuji Okada
Original assignee: Sumitomo Metal Mining Co Ltd
Current assignee: Sumitomo Metal Mining Co Ltd
Priority date: 2017-02-09
Filing date: 2018-01-31
Publication date: 2021-05-06
Anticipated expiration: 2038-01-31
Also published as: JP6900696B2; AU2018218644A1; JP2018127695A; US20200010925A1; PH12019501858A1; WO2018147146A1

Abstract

Provided is a smelting method in which, for example, a metal oxide such as a nickel oxide ore including nickel oxide is used as a source material and is reduced with a carbonaceous reducing agent to obtain a reduced product, with which method efficient processing can be achieved. This metal oxide smelting method is, for example, a nickel oxide ore smelting method. Specifically, the method includes a reduction process step that has: a drying step in which a mixture that was obtained by mixing a metal oxide and a carbonaceous reducing agent is dried; a preheating step in which the dried mixture is preheated; a reduction step in which the preheated mixture is reduced using a rotary hearth furnace, said rotary hearth having a hearth that rotates and not having a partition structure in an interior; and a cooling step in which the obtained reduced product is cooled.

Description

METAL OXIDE SMELTING METHOD TECHNICAL FIELD

The present invention relates to a metal oxide smelting method and

relates to a smelting method in which, for example, nickel oxide ore or the

like is used as a source material and is reduced with a carbonaceous reducing

agent to obtain a reduced product.

BACKGROUND ART

As methods for smelting nickel oxide ore which is called limonite or

saprolite, known are a dry smelting method for producing nickel matte using

a flash smelting furnace, a dry smelting method for producing ferronickel

using a rotary kiln or a moving hearth furnace, a HPAL process that is a

hydrometallurgical method for obtaining nickel-cobalt mixed sulfide (mixed

sulfide) using an autoclave by adding a high pressure acid leach sulfating

agent, and the like.

Among the various methods mentioned above, particularly, in a case

where nickel oxide ore is reduced and smelted using a dry smelting method,

a treatment for forming nickel oxide ore of a source material into a lump

product by crushing the nickel oxide ore into a proper size and the like, a

treatment for forming a slurry, or the like is performed as a pretreatment.

Specifically, when nickel oxide ore is formed into a limp product, that

is, a lump is formed from a powdery or granular ore, it is general that the

nickel oxide ore is mixed with other components, for example, a binder or a

reducing agent such as coke to obtain a mixture and the mixture is further

subjected to moisture adjustment and the like, then charged into a lump product manufacturing machine, and formed into a lump product referred to as a pellet or a briquette (hereinafter, collectively simply referred to as the

"pellet") having, for example, one side or a diameter of about 10 mm to 30

mm.

Further, the pellet is required to exhibit gas permeability to a certain

degree in order to "emit" the moisture contained. Furthermore, the

composition of the reduced product to be obtained is non-uniform and a

trouble that metal is dispersed or unevenly distributed is caused when the

reduction does not uniformly proceed in the pellet. For this reason, it is

important to uniformly mix the mixture and maintain the temperature as

constant as possible when the pellet is subjected to the reduction treatment.

In addition, it is also a significantly important technique to coarsen the

ferronickel to be generated by reduction. The reason for this is that, in a case

where the generated ferronickel has a fine size of, for example, several tens of

pm to several hundreds of pm or less, it is difficult to separate the ferronickel

from slag to be generated at the same time, and thus a recovery rate (yield)

as ferronickel greatly decreases. For this reason, a treatment for coarsening

the reduced ferronickel is required.

Further, it is also an important technical problem how the smelting

cost can be suppressed low, and a continuous treatment that can be

operated in a compact facility is desired.

For example, Patent Document 1 discloses a technique relating to a

method for producing ferronickel, and particularly to a method for producing

ferronickel or a source material for smelting ferronickel from nickel oxide ore of

a low grade with high efficiency. Specifically, disclosed is a method including a

mixing step of mixing a source material containing nickel oxide and iron oxide

with a carbonaceous reducing material to obtain a mixture, a reduction step of reducing the mixture in a moving hearth furnace by heating to obtain a reduced mixture, and a melting step of melting the reduced mixture in a melting furnace to obtain ferronickel.

Herein, Patent Document 1 describes that by setting the metallized

rate of Ni in the reduced mixture to 40% or more, preferably 85% or more,

heat required for reducing nickel oxide remaining in the reduced mixture in

the melting furnace is decreased so that energy consumption in the melting

furnace can be reduced. However, even if the heat required for the reduction

in the melting furnace is decreased by increasing the metallized rate of Ni in

the reduced mixture (hereinafter, also referred to as the "metallized rate"),

the heat quantity itself required for metallizing Ni is the same, the energy

consumption is not reduced when considered as a whole, and accordingly, the

smelting cost is not reduced.

Further, Patent Document 1 describes that a reduced lump product

(reduced mixture) reduced in the moving hearth furnace is generally cooled to

about 1000 0 C with, for example, a radiant cooling plate or a refrigerant

spraying machine provided in the moving hearth furnace and then is

discharged with a discharger. However, upon the reduced lump product is

cooled to about 1000 0 C or lower and discharged and recovered from the

moving hearth furnace, the moving hearth furnace is cooled, and energy for

increasing the temperature again for the reduction is needed, which incurs

cost. Further, when cooling and heating are repeated, thermal shock to the

furnace increases to shorten the life span of the device, which also causes an

increase in cost.

As described above, there are many problems in order to obtain

ferronickel by mixing and reducing nickel oxide ore and continuously

performing smelting at low cost.

Patent Document 1: Japanese Unexamined Patent

Application, Publication No. 2004-156140

SUMMARY OF THE INVENTION

The present invention has been made in view of such circumstances,

and may in some embodiments provide a smelting method in which, for

example, a metal oxide such as nickel oxide ore including nickel oxide or the

like may be used as a source material and may be reduced with a

carbonaceous reducing agent to obtain a reduced product, with which method

an efficient treatment may be achieved.

The present inventors have found that an efficient smelting treatment

may be performed, in some embodiments, by subjecting a mixture containing

a source material of a metal oxide to a reduction treatment in which a drying

step, a preheating step, a reduction step using a rotary hearth furnace which

does not have a partition structure in an interior, and a cooling step are

sequentially performed, whereby the present invention has been completed.

(1) A first invention of the present invention is a metal oxide smelting

method including a reduction treatment step including: a drying step in which

a mixture obtained by mixing a metal oxide and a carbonaceous reducing

agent is dried at a temperature of 5000 C or lower by blowing hot air to the

mixture, the metal oxide being a nickel oxide ore; a preheating step in which

the dried mixture is preheated at a temperature of 6000 C or higher and

1280 0C or lower; a reduction step in which the preheated mixture is reduced

using a rotary hearth furnace, the rotary hearth having a hearth that rotates

and not having a partition structure in an interior; and a cooling step in which

the obtained reduced product is cooled.

(2) A second invention of the present invention is the metal oxide

smelting method in the first invention, in which the reduced product

obtained through the reduction step is subjected to a temperature

maintenance step in which the reduced product is maintained at a

prescribed temperature in the rotary hearth furnace, and after maintained

for a prescribed time, the reduced product is supplied to the cooling step.

(3) A third invention of the present invention is the metal oxide

smelting method in the first invention, in which a treatment in the

reduction step and a treatment in the temperature maintenance step are

performed using the same rotary hearth furnace.

(4) A fourth invention of the present invention is the metal oxide

smelting method in the second or third invention, in which the reduced product

is maintained at a temperature of 1300 0 C or higher and 15000 C or lower in the

temperature maintenance step.

(5) A fifth invention of the present invention is the metal oxide

smelting method in any one of the first to fourth inventions, in which in the

reduction step, reduction is performed while a reducing temperature is set to

1200 0C or higher and 1500 0 C or lower.

(6) A sixth invention of the present invention is the metal oxide

smelting method in the fifth invention, in which in the reduction step, the

mixture is reduced at reducing temperatures of two steps, the reducing

temperature at the first step is 12000 C or higher and 14500 C or lower, and

the reducing temperature at the second step is 13000 C or higher and

1500 0C or lower.

(7) A seventh invention of the present invention is the metal oxide

smelting method in the sixth invention, in which the rotary hearth furnace

includes a plurality of heating sources, and a temperature distribution inside the rotary hearth furnace is controlled by controlling an amount of energy supplied to each heating source.

(8) An eighth invention of the present invention is the metal oxide

smelting method in any one of the first to seventh inventions, in which the

mixture to be dried in the drying step is obtained through a mixing treatment

step in which at least a metal oxide and a carbonaceous reducing agent are

mixed to obtain a mixture, and a pretreatment step in which a treatment of

forming the obtained mixture into a lump product or a treatment of filling the

mixture in a prescribed container is performed.

(9) A ninth invention of the present invention is the metal oxide

smelting method in any one of the first to eighth inventions, further including

a separating step in which the reduced product cooled in the cooling step in

the reduction treatment step is separated into a metal and slag and the metal

is recovered.

(10) A tenth invention of the present invention is the metal oxide

smelting method in any one of the first to ninth inventions, in which the metal

oxide is nickel oxide ore.

(11) An eleventh invention of the present invention is the metal

oxide smelting method in any one of the first to tenth inventions, in which

the reduced product contains ferronickel.

According to some aspects of the present invention, it may be

possible to provide a smelting method in which, for example, a metal oxide

such as nickel oxide ore including nickel oxide or the like is used as a source

material and may be reduced with a carbonaceous reducing agent to obtain

a reduced product, with which method an efficient treatment may be

achieved.

BRIEF DESCRIPTION OF THE DRAWINGS

Fig. 1 is a process diagram illustrating an example of the flow of a method

for smelting nickel oxide ore.

Fig. 2 is processing illustrating a treatment step to be performed in a

reduction treatment step.

Fig. 3 is a diagram (plan view) illustrating a configuration example of a rotary

hearth furnace, the rotary hearth having a hearth that rotates and not having

a partition structure in an interior.

PREFERRED MODE FOR CARRYING OUT THE INVENTION

<<1. Overview of Present Invention>>

A metal oxide smelting method according to the present invention is a

smelting method in which a metal oxide is used as a source material and a

reduction treatment is performed by a carbonaceous reducing agent at a high

temperature to obtain

a reduced product. For example, there is mentioned a method for producing

ferronickel by using nickel oxide as a metal oxide or nickel oxide ore including

iron oxide or the like as a source material and reducing the source material

for smelting using a carbonaceous reducing agent under a high temperature.

Specifically, the metal oxide smelting method according to the present

invention includes reduction treatment step that includes a drying step in

which a mixture obtained by mixing a metal oxide and a carbonaceous

reducing agent is dried, a preheating step in which the dried mixture is

preheated, a reduction step in which the preheated mixture is reduced using

a rotary hearth furnace, the rotary hearth having a hearth that rotates and

not having a partition structure in an interior, and a cooling step in which the

obtained reduced product is cooled.

In this manner, according to the present invention, the mixture

containing metal oxide as a source material is subjected to the treatment in

each step mentioned above, and further the treatment in the reduction step is

performed using the rotary hearth furnace, the rotary hearth having a hearth

that rotates and not having a partition structure in an interior, so that the

metal contained in the metal oxide can be effectively metallized and an

efficient smelting treatment can also be performed.

Hereinafter, as a specific embodiment of the present invention

(hereinafter, referred to as the "present embodiment"), a method for smelting

nickel oxide ore will be described as an example. The nickel oxide ore serving

as a source material for smelting contains at least nickel oxide. In this method

for smelting nickel oxide ore, ferronickel (iron-nickel alloy) can be produced by

reducing nickel oxide and the like contained in the source material.

Incidentally, in the present invention, the metal oxide is not limited to

nickel oxide ore and the smelting method is also not limited to a method for

producing ferronickel from nickel oxide ore containing nickel oxide and the

like. Further, various modifications can be made without changing the gist of

the present invention.

<<2. Method for Smelting Nickel Oxide Ore>>

The method for smelting nickel oxide ore according to the present

embodiment is a method for generating ferronickel, which is a metal, and

slag by mixing and kneading nickel oxide ore serving as a source material for

smelting with a carbonaceous reducing agent or the like to obtain a mixture

and subjecting the mixture to a reduction treatment. Incidentally, ferronickel,

which is a metal, can be recovered from a mixture containing a metal and

slag obtained through the reduction treatment by separating the metal.

Fig. 1 is a process diagram illustrating an example of the flow of a

method for smelting nickel oxide ore. As illustrated in Fig. 1, this method

for smelting nickel oxide ore includes a mixing treatment step S1 in which

nickel oxide ore and a material such as a carbonaceous reducing agent are

mixed to obtain a mixture, a reduction charging pretreatment step S2 in

which the obtained mixture is formed into a lump product or filled in a

prescribed container, a reduction treatment step S3 in which the mixture is

reduced at a prescribed temperature (reducing temperature), and a

separating step S4 in which the metal is separated and recovered from the

mixture containing the metal and slag generated by the reduction

treatment.

<2-1. Mixing Treatment Step>

The mixing treatment step S1 is a step in which source material

powders including nickel oxide ore are mixed to obtain a mixture.

Specifically, in the mixing treatment step S1, nickel oxide ore serving as a

source material for smelting and source material powders, such as iron ore, a

flux component, a binder, or a carbonaceous reducing agent, having a

particle diameter of, for example, about 0.2 mm to 0.8 mm are mixed at a

prescribed ratio to obtain a mixture.

The nickel oxide ore serving as an ore of a source material for

smelting is not particularly limited, but limonite ore, saprolite ore, and

the like can be used.

As the iron ore, for example, iron ore having an iron grade of about

%, hematite to be obtained by hydrometallurgy of nickel oxide ore, and the

like can be used.

An example of compositions (% by weight) of nickel oxide ore serving

as a source material and iron ore is presented in the following Table 1.

Incidentally, the composition of the source material is not limited thereto.

[Table 1]

Source material

.

[% by weight] N1 Fe203 C

Nickel oxide ore 1~2 50~60-

Iron ore - 80~95

Further, examples of the binder may include bentonite, a

polysaccharide, a resin, water glass, and dehydrated cake. Further, examples

of the flux component may include calcium oxide, calcium hydroxide, calcium

carbonate, and silicon dioxide.

The carbonaceous reducing agent is not particularly limited, and

examples thereof include coal powder and coke. Incidentally, this

carbonaceous reducing agent preferably has a size equivalent to the particle

size of the nickel oxide ore of the source material ore. Further, the amount

of the carbonaceous reducing agent mixed can be adjusted such that the

proportion of carbon amount is 5% or more and 60% or less when the total

value (also conveniently referred to as the "total value of chemical

equivalents") of a chemical equivalent required for reducing the entire

amount of nickel oxide contained in the mixture to be formed into nickel

metal and a chemical equivalent required for reducing ferric oxide contained

in the pellet into iron metal is regarded as 100%.

In the mixing treatment step S1, a mixture is obtained by uniformly

mixing source material powders including nickel oxide ore as described above.

Upon this mixing, kneading may be performed at the same time as mixing or

kneading may be performed after mixing. In this manner, by mixing and

kneading the source material powders, the contact area between the source

materials increases and by decreasing voids, the reduction reaction is likely to

occur and the reaction can be uniformly conducted. Accordingly, the reaction time of the reduction reaction can be shortened and variation in the quality is diminished. As a result, a highly productive treatment can be performed and high quality ferronickel can be produced.

Further, after kneading the source material powders, the mixture may

be extruded using an extruder. By extruding the mixture using an extruder in

this manner, a still higher kneading effect can be obtained, the contact area

between the source material powders increases, and voids can be decreased.

Accordingly, high quality ferronickel can be efficiently produced.

<2-2. Reduction Charging Pretreatment Step (Pretreatment Step)>

The reduction charging pretreatment step S2 is a step in which the

mixture obtained in the mixing treatment step S1 is formed into a lump

product or filled in a container. That is, in this reduction charging

pretreatment step S2, the mixture obtained by mixing the source material

powders is molded such that the mixture is easily charged into a furnace used

in the reduction treatment step S3 described later and the reduction reaction

efficiently occurs.

(Forming Mixture into Lump Product)

In the case of forming the obtained mixture into a lump product, the

mixture is formed (granulated) into a lump product. Specifically, moisture is

added to the obtained mixture in a prescribed amount required for forming

the mixture into a lump product and the mixture is molded into a lump

(hereinafter, also referred to as the "pellet") using, for example, a lump

product manufacturing apparatus (such as a tumbling granulator, a

compression molding machine, or an extrusion molding machine) or the like.

The shape of the pellet is not particularly limited, and the shape of the

pellet can be, for example, a spherical shape. By adopting a spherical pellet,

the reduction reaction easily proceeds relatively uniformly, which is preferable.

Further, the size of the lump product to be formed into a pellet is not

particularly limited, but for example, the size (the diameter in the case of a

spherical pellet) of the pellet to be charged into a smelting furnace, which is

used for performing the reduction treatment (reduction step S33), through the

drying treatment (drying step S31) and the preheating treatment (preheating

step S32) can be set to about 10 mm to 30 mm. Incidentally, the reduction

step and the like will be described in detail later. (Filling of Mixture in

Container)

In the case of filling the obtained mixture in a container, the mixture

can be filled in a prescribed container while being kneaded by an extruder or

the like. In this manner, after the mixture is filled in the container, the

reduction treatment may be performed in the subsequent step of the reduction

treatment step S3 without any changes, but the mixture filled in the container

is preferably compressed by a press or the like. By compressing and molding

the mixture in the container, the density of the mixture can be increased, the

density becomes uniform, the reduction reaction easily proceeds more

uniformly, and ferronickel having small variation in the quality can be

produced.

The shape of the mixture to be filled in the container is not particularly

limited, but for example, the shape is preferably a rectangular parallelepiped

shape, a cubic shape, a cylindrical shape, or the like. Further, the size thereof

is not also particularly limited, but for example, if the shape is a rectangular

parallelepiped shape or a cubic shape, the inside dimensions of the height and

the width is preferably approximately 500 mm or less. With such a shape and

such a size, the variation in the quality becomes small and highly productive

smelting can be performed.

<2-3. Reduction Treatment Step>

In the reduction treatment step S3, the source material powders are

mixed in the mixing treatment step S1 and the mixture formed into a lump

product or filled in the container in the reduction charging pretreatment step

S2 is reduced and heated at a prescribed reducing temperature. By the

reduction and heat treatment of the mixture in the reduction treatment step

S3, the smelting reaction proceeds and a metal and slag are generated.

Fig. 2 is a process diagram illustrating a treatment step to be

performed in the reduction treatment step S3. As illustrated in Fig. 2, the

reduction treatment step S3 in the present embodiment includes a drying step

S31 in which the mixture is dried, a preheating step S32 in which the dried

mixture is preheated, a reduction step S33 in which the mixture is reduced,

and a cooling step S35 in which the obtained reduced product is cooled.

Further, preferably, the reduction treatment step S3 includes a temperature

maintenance step S34 in which the reduced product obtained through the

reduction step S33 is maintained in a prescribed temperature range.

Herein, the treatment in the reduction step S33 is performed using a

rotary hearth furnace, a hearth of which rotates. Further, this rotary hearth

furnace does not have a partition structure in an interior. Furthermore, in a

case where the temperature maintenance step S34 in which the reduced

product is maintained in a prescribed temperature range is performed, at

least the treatment in the reduction step S33 and the treatment in the

temperature maintenance step S34 are performed in the rotary hearth

furnace.

In this manner, by performing those treatments in the rotary hearth

furnace, the temperature in the rotary hearth furnace can be maintained at a

high temperature, so that it is unnecessary to increase or decrease the

temperature every time the treatments in the respective steps are performed, and energy cost can be considerably reduced. Further, according to the treatment using the rotary hearth furnace, the control or management of the temperature is easily conducted. According to these, high quality ferronickel can be continuously stably produced at high productivity.

Furthermore, by performing the treatment using the rotary hearth

furnace which does not have a partition structure in an interior, the

maintenance cost of the rotary hearth furnace can be reduced, an efficient

treatment can be conducted, and the temperature in the furnace can be still

more uniformly controlled.

(1) Drying Step

In the drying step S31, the mixture obtained by mixing the source

material powders is subjected to the drying treatment. This drying step S31

is mainly intended to extract moisture or crystalline water in the mixture.

A large amount of moisture or the like is contained in the mixture

obtained in the mixing treatment step S1, the moisture evaporates and

expands at a time by a sharp increase to a high temperature like a reducing

temperature at the time of the reduction treatment in this state, the mixture

formed into a lump product is broken, or depending on the cases, is broken

into fragments, and thus it is difficult to perform a uniform reduction

treatment. For this reason, before the reduction treatment is performed,

the mixture is subjected to the drying treatment to remove moisture so that

breakage of the pellet or the like is prevented.

The drying treatment in the drying step S31 is preferably performed in

the form of being connected to a rotary hearth furnace. The drying treatment

is also considered to be performed while an area in which the drying treatment

is conducted (drying area) is provided in the rotary hearth furnace, but in such

a case, the drying treatment in the drying area is limited so that the treatment in the reduction step S33 and the treatment in the temperature maintenance step S34 may be affected.

Therefore, it is preferable that the drying treatment in the drying step

S31 is performed in a drying chamber which is provided outside the furnace

of the rotary hearth furnace and is connected to the rotary hearth furnace.

Incidentally, although will be described in detail later, Fig. 3 illustrates a

configuration example of a rotary hearth furnace 1 and a drying chamber 20

connected to the rotary hearth furnace 1. In this manner, by the drying

chamber 20 being provided outside the furnace of the rotary hearth furnace

1, a drying chamber can be designed quite separately from steps such as

preheating, reduction, and cooling described later, and desirable drying,

preheating, reduction, and cooling treatments are easily performed,

respectively. For example, in a case where a large amount of moisture

remains in the mixture depending on the source material, since it takes time

to perform the drying treatment, the entire length of the drying chamber 20

may be designed to be long or the transfer speed of the mixture in the drying

chamber 20 may be designed to be decreased.

As the drying treatment in the drying chamber 20, for example,

a treatment can be performed so that the solid content in the mixture is

about 70% by weight and the moisture is about 30% by weight.

Further, the drying method is not particularly limited, but the drying can

be performed by blowing hot air to the mixture transferred in the drying

chamber 20. Further, the drying temperature is not particularly limited,

but from the viewpoint that the reduction reaction is not started, the

drying temperature is preferably set to 500 0 C or lower and it is

preferable to perform uniform drying at the temperature of 5000 C or

lower.

An example of the composition (parts by weight) of the solid

content in the drying-treated mixture is presented in the following Table 2.

Incidentally, the composition of the mixture is not limited thereto.

[Table 2]

Composition of solid content Ni Fe20 SiO2 CaO Al203 MgO Binder Others in dried mixture (pellet) 0.5~1.5 50~60 8~15 4~8 1~6 2~7 About 1 Balance

[Parts by weight]

(2) Preheating Step

In the preheating step S32, the mixture after the moisture

has been removed by the drying treatment in the drying step S31 is

preheated (preliminarily heated).

When the mixture is charged into the rotary hearth furnace and

heated rapidly to a high temperature of a reducing temperature, the mixture

cracks due to thermal stress or becomes powders. Further, the temperature

of the mixture does not uniformly increase, variation in the reduction reaction

occurs, and the quality of the metal to be generated may deteriorate.

Therefore, it is preferable that the mixture is preheated to a prescribed

temperature after the mixture is subjected to the drying treatment, and

according to thus, the breakage of the mixture and the variation in reduction

reaction can be suppressed.

The preheating treatment in the preheating step S32 is preferably

performed in the treating chamber provided outside the furnace of the

rotary hearth furnace, similarly to the drying treatment, and the

preheating treatment is preferably performed in a preheating chamber

connected to the rotary hearth furnace. Incidentally, Fig. 3 illustrates a

configuration example of a preheating chamber 30 connected to the rotary

hearth furnace 1, and the preheating chamber 30 is provided outside the

furnace of the rotary hearth furnace 1 and is provided continuously from

the drying chamber 20 in which the drying treatment is performed. In this

manner, by performing the preheating treatment in the preheating

chamber 30 provided outside the furnace of the rotary hearth furnace 1,

the temperature in the rotary hearth furnace 1 in which the reduction

treatment is performed can be maintained to be a high temperature and

energy required for heating can be considerably saved.

The preheating treatment in the preheating chamber 30 is not

particularly limited, but it is preferable to perform the preheating treatment

while a preheating temperature is set to 600 0 C or higher and it is more

preferable to perform the preheating treatment while a preheating

temperature is set to 7000 C or higher and 12800 C or lower. By performing

the treatment at a preheating temperature in such a range, energy required

for reheating to the reducing temperature in the subsequent reduction

treatment can be considerably reduced.

(3) Reduction Step

In the reduction step S33, the mixture preheated in the preheating

step S32 is subjected to a reduction treatment at a prescribed reducing

temperature. Specifically, the reduction treatment in the reduction step S33

is performed using a rotary hearth furnace, a hearth of which rotates.

Furthermore, the rotary hearth furnace does not have a partition structure in

the furnace, that is, does not have a structure such as a partition or a

threshold.

In this manner, by performing the reduction treatment using the

rotary hearth furnace, the temperature in the furnace can be maintained in a

high temperature range, it is unnecessary to increase or decrease the

temperature, and energy cost can be considerably reduced. Further, the

control or management of the temperature is easily conducted and high

quality ferronickel can be stably generated. Furthermore, by using the rotary

hearth furnace which does not have a partition structure in the furnace, the

temperature in the furnace can be still more uniformly controlled. Further,

initial cost or maintenance cost for the partition structure can be reduced, and

a more efficient treatment can be performed.

[Configuration of Rotary Hearth Furnace]

Herein, Fig. 3 is a diagram (plan view) illustrating a configuration

example of a rotary hearth furnace, a hearth of which rotates. As illustrated

in Fig. 3, the rotary hearth furnace 1 has a region 10 in which the hearth

rotates and this region 10 does not have a partition structure such as a

partition or a threshold.

For example, regarding the rotary hearth furnace, a configuration is

considered in which a region of the rotating hearth is arbitrarily divided into a

plurality of regions to form a plurality of divided treating chambers. In the

plurality of treating chambers, treatments in the steps different from each

other can be performed by respectively adjusting or controlling the reaction

temperatures. Further, at this time, a configuration in which the respective

treating chambers, that is, the respective steps are partitioned by providing a

partition wall can be employed, and according to this, arbitrary temperature

setting or the like in the respective treating chambers can be performed, and

this also leads to a reduction in energy loss.

However, when a partition structure as mentioned above is provided in

the rotary hearth furnace to divide the furnace into a plurality of treating

chambers, the structure of the rotary hearth furnace is complicated, and

maintenance cost increases as well as initial cost increases. Further, by

having such a partition structure, uniform temperature setting in the furnace

becomes difficult and the reduction reaction does not sufficiently proceed,

which is considered to be inefficient.

In this regard, in the present embodiment, a rotary hearth furnace

which does not have a partition structure in the furnace is used. By using

such a rotary hearth furnace, the temperature in the furnace can be more

uniformly controlled, initial cost or maintenance cost for the partition

structure can be reduced, and an efficient treatment can be performed.

The rotary hearth furnace 1 includes, as described above, a hearth

which rotationally moves on the plane. Therefore, in the rotary hearth furnace

1, when the hearth on which the mixture is placed rotationally moves at a

prescribed speed, the reduction treatment is performed while the mixture is

transferred. Incidentally, an arrow on the rotary hearth furnace 1 in Fig. 3

indicates a rotation direction of the hearth and indicates a moving direction of

a material to be treated (mixture).

Further, the rotary hearth furnace 1 is connected to the drying

chamber 20 and the preheating chamber 30 which are provided outside the

furnace, and as described above, after the mixture is subjected to the drying

treatment in the drying chamber 20, the dried mixture is transferred to the

preheating chamber 30 and subjected to the preheating treatment and the

preheating-treated mixture is sequentially transferred to the inside of the

rotary hearth furnace 1. Further, the rotary hearth furnace 1 is connected to

a cooling chamber 40 provided outside the furnace, and the reduced product

obtained by performing the reduction treatment is transferred to the cooling

chamber 40 and subjected to the cooling treatment (cooling step S35

described later).

Further, in the rotary hearth furnace 1, a plurality of heating sources

are provided and the amount of energy supplied to each heating source is

controlled, so that the temperature distribution inside the rotary hearth

furnace 1 can be controlled. For example, the mixture is reduced at the

reducing temperatures of two steps in the reduction treatment using the

rotary hearth furnace 1, and at this time, a first heating source for adjusting

a prescribed position in the furnace to the reducing temperature at the first

step and a second heating source for adjusting a prescribed position in the

furnace to the reducing temperature at the second step are provided.

Further, by controlling the amount of energy supplied to each heating source,

the temperature distribution inside the rotary hearth furnace 1 is controlled

so that an appropriate reduction reaction occurs.

In this manner, the temperature distribution inside the furnace is

controlled by providing the plurality of heating sources in the rotary hearth

furnace 1 used in the reduction treatment and controlling the amount of

energy supplied to each heating source, so that a treatment according to the

reduction degree of the mixture can be performed and the reduction reaction

effectively occurs, whereby the recovery rate of nickel to ferronickel metal

can be increased.

Further, such an aspect is particularly effective in the case of

performing a temperature maintenance step S34 described later. That is, the

temperature distribution inside the furnace is controlled by providing the

plurality of heating sources in the rotary hearth furnace 1 and controlling the

amount of energy supplied to each heating source, so that, for example, the

reduction treatment (reduction step S33) is performed in a first treatment

region heated by the first heating source and the temperature maintenance

treatment (temperature maintenance step S34) is performed in a second

treatment region heated by the second heating source.

According to this, after the reduced product formed by a mixed product

of a metal and slag is generated by the mixture being effectively subjected to

the reduction treatment in the first treatment region, a treatment in which the

reduced product is maintained at a high temperature in the second treatment

region to effectively coarsen the metal can be efficiently performed.

Incidentally, the treatment in the temperature maintenance step S34 (high

temperature maintenance treatment) will be described in detail later.

[Reduction Treatment in Rotary Hearth Furnace]

In the reduction treatment using the rotary hearth furnace 1, it is

preferable that nickel oxide, which is a metal oxide contained in nickel oxide

ore, is completely reduced as much as possible; meanwhile, iron oxide,

which is derived from iron ore or the like mixed as source material powder

with nickel oxide ore, is partially reduced such that ferronickel having a

target nickel grade is obtainable.

Specifically, the reducing temperature is not particularly limited,

but is preferably set in a range of 12000 C or higher and 15000 C or lower

and more preferably set in a range of 13000 C or higher and 14000 C or

lower. By performing reduction in such a temperature range, the

reduction reaction can uniformly occur, and metal (ferronickel metal) in

which variation in the quality is suppressed can be generated. Further, more preferably, when reduction is conducted at a reducing temperature

in a range of 13000 C or higher and 14000 C or lower, a desired reduction

reaction can occur in a relatively short time.

Further, in the reduction treatment, the mixture may be reduced at

reducing temperatures of two steps. For example, while the reducing

temperature at the first step is set to 12000 C or higher and 14500 C or lower

and the reducing temperature at the second step is set to 13000 C or higher

and 1500 0 C or lower, the mixture placed on the hearth of the rotary hearth

furnace 1 and transferred is subjected to the reduction treatment. In this

manner, when the mixture is subjected to the reduction treatment at the

reducing temperatures of two steps, first, the reduction reaction to the

mixture proceeds at the first step, and then the metal in the reduced

product generated at the second step can be coarsened while being settled.

Upon the reduction treatment, the internal temperature of the

reducing chamber in the rotary hearth furnace 1 is increased to a reducing

temperature in the aforementioned range, and after the temperature

increases, the temperature at this time is maintained. Further, as

mentioned above, in a case where the plurality of heating sources are

provided in the rotary hearth furnace 1, the temperature distribution inside

the furnace can be controlled by controlling the amount of energy supplied

to each heating source.

Further, in the reduction treatment, in order to prevent the mixture

sample from being difficult to recover when the mixture sample reacts with

the hearth and is not peeled off, a reaction suppressing material such as ash

may be spread on the hearth of the rotary hearth furnace 1 to be used and

the mixture sample may be placed on the reaction suppressing material.

For example, as the ash serving as the reaction suppressing material, ash

having SiO2 as a main component and containing a small amount of an

oxide such as A1203 or MgO as other components can be used.

(4) Temperature Maintenance Step

Although not an essential aspect, the temperature maintenance step

S34 in which the reduced product obtained through the reduction step S33

is maintained in a prescribed high temperature condition in the rotary

hearth furnace may be performed. In this manner, when the reduced

product obtained by the reduction treatment at a prescribed reducing

temperature in the reduction step S33 is not cooled immediately but is

maintained in a high temperature atmosphere, a metal component

generated in the reduced product can be settled and coarsened.

In a case where the metal component in the reduced product is

small in the state of being obtained by the reduction treatment, for example, in a case where the metal component is a bulk-form metal having a size of about 200 pm or less, it is difficult to separate the metal and the slag in the subsequent separating step S4. Therefore, as necessary, by the reduced product being maintained at a high temperature over a certain time continuously after the reduction reaction is finished, the metal in the reduced product having a larger specific gravity than that of the slag is settled and aggregated to coarsen the metal.

Incidentally, in a case where the metal is coarsened to a level that does

not cause any problem in production by the reduction treatment in the

reduction step S33, particularly, this temperature maintenance step S34 is not

necessarily provided.

Specifically, the maintaining temperature of the reduced product in

the temperature maintenance step S34 is preferably set in a high

temperature of 1300 0 C or higher and 15000 C or lower. By maintaining the

reduced product at a high temperature in such a range, the metal component

in the reduced product can be efficiently settled to obtain coarse metal.

Incidentally, when the maintaining temperature is lower than 13000 C, since a

large part of the reduced product becomes a solid phase, the metal

component is not settled, or even if the metal component is settled, it takes

time for that, which is not preferable. On the other hand, when the

maintaining temperature is higher than 15000 C, reaction between the

obtained reduced product and a hearth material proceeds, so that there is a

case where the reduced product cannot be recovered or the furnace is

damaged.

Herein, the treatment in the temperature maintenance step S34 is

preferably performed in the rotary hearth furnace 1 used in the reduction step S33 continuously to the reduction treatment. In this manner, by continuously performing, using the rotary hearth furnace 1, the treatment in which the reduced product obtained through the reduction treatment is maintained at a prescribed temperature, the metal component in the reduced product can be efficiently settled and coarsened. Moreover, when the treatment in the reduction step S33 and the treatment in the temperature maintenance step S34 are not performed in separate furnaces but performed continuously using the rotary hearth furnace 1, heat loss between the respective treatments can be reduced and an efficient operation can be performed.

Specifically, when the reduction treatment and the temperature

maintenance treatment are performed in the same rotary hearth furnace 1,

the temperature distribution inside the furnace can be controlled by providing

the plurality of heating sources in the rotary hearth furnace 1 and controlling

the amount of energy supplied to each heating source. That is, the

temperature in the reduction step S33 (reducing temperature) and the

temperature in the temperature maintenance step S34 (maintaining

temperature) are controlled by each of different heating sources. According

to this, even in the case of the rotary hearth furnace 1 which does not have a

partition structure in an interior, the temperature can be accurately controlled

and an efficient treatment can be performed.

(5) Cooling Step

In the cooling step S35, the reduced product obtained through the

reduction step S33 or the reduced product maintained at a high temperature

over a prescribed time in the temperature maintenance step S34 is cooled to

a temperature at which the reduced product can be separated and recovered

in the subsequent separating step S4.

Since the cooling step S35 is a step in which the reduced product

obtained as mentioned above is cooled, the cooling step S35 is preferably

performed in the cooling chamber connected to the outside of the furnace of

the rotary hearth furnace 1. Incidentally, although Fig. 3 illustrates the

configuration example of the cooling chamber 40 connected to the rotary

hearth furnace 1, this cooling chamber 40 is provided to be connected to the

outside of the furnace of the rotary hearth furnace 1. In this manner, by

performing the cooling treatment in the cooling chamber 40 provided outside

the furnace of the rotary hearth furnace 1, the internal temperature of the

rotary hearth furnace 1 can be prevented from decreasing, and energy loss

can be suppressed. According to this, efficient ferronickel generation can be

conducted.

The temperature in the cooling step S35 (hereinafter, also referred

to as the "temperature at the time of recovering") is a temperature at which

the reduced product is handled substantially as a solid, and the temperature

is preferably a high temperature as much as possible. By increasing the

temperature at the time of recovering as much as possible, even when the

hearth, which rotationally moves, of the rotary hearth furnace 1 returns to

the connect place with the preheating chamber 30 in which the preheating

step S32 is performed, energy loss can be reduced, and energy required for

reheating can be still more saved.

Specifically, the temperature at the time of recovering is preferably set

to 6000 C or higher. By setting the temperature at the time of recovering to a

high temperature in this manner, energy required for reheating can be

considerably reduced, and an efficient smelting treatment can be performed at

low cost. Further, by decreasing a difference in temperature inside the rotary

hearth furnace 1, thermal stress to be applied to the hearth, the furnace wall, or the like can be decreased, and the life span of the rotary hearth furnace 1 can be largely expanded. Furthermore, failures during operation can also be considerably decreased.

<2-4. Separating Step>

In the separating step S4, the metal (ferronickel metal) is separated

and recovered from the reduced product generated in the reduction treatment

step S3. Specifically, in the separating step S4, the metal phase is separated

and recovered from a mixed product (reduced product) which contains a metal

phase (metal solid phase) and a slag phase (slag solid phase) which is

obtained by the reduction and heat treatment of the mixture.

As a method for separating the metal phase and the slag phase from

the mixed product which is composed of the metal phase and the slag phase

and is obtained as a solid, for example, methods such as separation by specific

gravity and separation by magnetic force can be utilized in addition to removal

of unnecessary substances by sieving. Further, the metal phase and the slag

phase thus obtained can be easily separated since these exhibit poor

wettability, and it is possible to easily separated the metal phase and the slag

phase from the mixed product by imparting an impact to the large mixed

product, for example, falling down the large mixed product at a prescribed

falling distance or applying a prescribed vibration to the large mixed product at

the time of sieving.

The metal phase is recovered by separating the metal phase and the

slag phase in this manner, and thus a product of ferronickel can be obtained.

EXAMPLES

Hereinafter, the present invention will be described in more detail by

means of Examples, but the present invention is not limited to the following

Examples at all.

(Mixing Treatment Step)

Nickel oxide ore serving as a source material ore, iron ore, silica sand

and limestone which are flux components, a binder, and coal powder which is a

carbonaceous reducing agent (carbon content: 85% by weight, average

particle diameter: about 190 pm) were mixed using a mixer while adding an

appropriate amount of water to obtain a mixture. Incidentally, the

carbonaceous reducing agent was contained in an amount corresponding to

the amount of carbon of 33% when the total value of a chemical equivalent

required for reducing nickel oxide and iron oxide (Fe203) into metal without

being in excess or short was regarded as 100%.

Then, the mixture obtained by mixing with the mixer was kneaded

by a biaxial kneader.

(Reduction Charging Pretreatment Step)

Then, the mixture obtained by kneading was classified into nine,

and each mixture sample was molded using a pan granulator into a

spherical pellet of (p19 ±1.5 mm. (Reduction Treatment Step)

Then, the respective mixture samples classified into nine were

subjected to a reduction treatment using a reduction hearth furnace 1 as

illustrated in Fig. 3 while treatment conditions were changed. As the rotary

hearth furnace 1, as illustrated in Fig. 3, a rotary hearth furnace, the rotary

hearth having a hearth that rotates and not having a partition structure in an

interior, was used. Further, in this rotary hearth furnace 1, a drying chamber

drying the pellet, a preheating chamber 30 provided continuously to the

drying chamber 20, and a cooling chamber 40 cooling a reduced product obtained by the reduction treatment in the furnace are connected to the outside of the furnace.

Specifically, nine pellet samples were charged into the drying

chamber 20 connected to the outside of the furnace of the reduction hearth

furnace 1 and then subjected to a drying treatment. The drying treatment

was performed in a nitrogen atmosphere substantially not containing oxygen

by blowing hot air set at 250 0 C to 350 0 C to the pellets such that the solid

content in the pellet would be about 70% by weight and the moisture would

be about 30% by weight. The solid content compositions (excluding

carbon) of the drying-treated pellet are presented in the following Table 3.

[Table 3]

Composition of solid content in dried pellet [% by mass]

Ni Fe203 SiO2 CaO A1203 MgO Others Binder, 1.6 53.3 14.0 5.4 3.2 5.7 carbonaceous reducing agent

Subsequently, the drying-treated pellet was transferred to the

preheating chamber 30 provided continuously to the drying chamber 20 and

the pellet was subjected to a preheating treatment while the temperature in

the preheating chamber 30 was maintained in a range of 7000 C or higher and

1280 0C or lower.

Subsequently, the preheating-treated pellet was transferred to the

inside of the rotary hearth furnace 1 and subjected to a reduction treatment

and a temperature maintenance treatment. Specifically, regarding the rotary

hearth furnace 1, the temperature of the reduction treatment and the

temperature of the high temperature maintenance treatment were

differentiated from each other by providing two heating sources and

controlling the amount of energy supplied to each heating source.

Further, in the hearth of the rotary hearth furnace 1, in order to

prevent the sample from being difficult to recover when the sample reacts with

the hearth and is not peeled off, from the viewpoint of suppressing the

reaction between the hearth and the sample as much as possible, the hearth

was paved in advance with ash (having SiO2 as a main component and

containing a small amount of an oxide such as A1203 or MgO as other

components).

Incidentally, in Examples in the aspect in which the treatment of

maintaining the reduced product at a high temperature is not performed, the

temperature of the high temperature maintenance treatment was set to 0°C.

Further, the reduced product obtained through the reduction treatment or the

reduction treatment and the temperature maintenance treatment was

transferred to the cooling chamber connected to the rotary hearth furnace 1,

cooled rapidly to room temperature while allowing nitrogen to flow, and then

taken out into the air. Incidentally, the recovery of the reduced product from

the rotary hearth furnace was performed in the form of the reduced product

being transferred to the cooling chamber 40, and the reduced product was

recovered along a guide installed at the cooling chamber 40 by the guide.

Conditions of the reduction treatment and the temperature

maintenance treatment in the reduction treatment step are presented in the

following Table 4.

Further, the nickel grade of the sample taken was analyzed by an ICP

emission spectroscopic analyzer (SHIMAZU S- 8100 model) and the metallized

rate of nickel and the nickel content rate in the metal were calculated,

respectively. Incidentally, the metallized rate of nickel was calculated by the

following Equation (i) and the nickel content rate in the metal was calculated

by the following Equation (ii). Metallized rate of nickel = amount of metallized

Ni in pellet + (amount of entire Ni in pellet) x 100 (%) -- (i) Nickel content

rate in metal = amount of metallized Ni in pellet + (total amount of metallized

Ni and Fe in pellet) x 100 (%) --- (ii)

Further, the recovered samples were pulverized by wet treatment and

then the metal (ferronickel metal) was recovered by magnetic separation.

Then, the recovery rate of Ni metal was calculated from the Ni content rate

and the charged amount of the nickel oxide ore charged, and the amount of

the recovered Ni. Incidentally, the recovery rate of Ni metal was calculated

from the following Equation (iii).

Recovery rate of Ni metal = amount of recovered Ni + (amount of ore

charged x proportion of Ni contained in ore) x 100 - - Equation (iii)

[Table 4]

HighCotnofRcvr Reducing Reducing temperature Metallized Cotentof Recovery Sample temperature time maintaining rate ofNi Niinmetal rateof temperature (/o) (/) metal (°C) (Min.) 0 ( (%)

1 1205 55 0 98.0 18.1 90.0 2 1255 45 0 98.3 18.3 90.1 3 1300 35 0 98.7 18.4 90.3 4 1350 18 0 99.3 18.6 90.5 5 1390 14 0 99.6 18.7 90.6 6 1440 8 0 99.7 19.0 90.8 7 1240 50 130 99.4 18.6 90.6 8 1240 50 140 99.7 18.9 91.4 9 1240 50 149 99.9 19.4 92.3

As understood from Table 4, by the mixture containing the source

material ore being subjected to the reduction treatment step having at least

the drying step, the preheating step, the reduction step in which the reduction

is conducted using a rotary hearth furnace, a hearth of which rotates, and the cooling step in which the obtained reduced product is cooled, ferronickel of a high nickel grade could be obtained, and nickel at a high recovery rate of 90% or more as the recovery rate could be recovered.

Further, by performing the reduction treatment or the reduction

treatment and the temperature maintenance treatment using the rotary hearth

furnace, the internal temperature ofthe rotary hearth furnace could be

maintained to a high temperature, energy required for reheating was

suppressed, and an efficient smelting treatment could be performed.

Furthermore, by using the rotary hearth furnace which does not have a

partition structure in an interior, the internal temperature could be uniformly

maintained, and further, the initial cost and the maintenance cost could also

be effectively reduced.

Throughout this specification and the claims which follow, unless the

context requires otherwise, the word "comprise", and variations such as

"comprises" or "comprising", will be understood to imply the inclusion of a

stated integer or step or group of integers or steps but not the exclusion of

any other integer or step or group ofintegers or steps.

The reference in this specification to any prior publication (or

information derived from it), or to any matter which is known, is not, and

should not be taken as, an acknowledgement or admission or any form of

suggestion that that prior publication (or information derived from it) or known

matter forms part of the common general knowledge in the field of endeavour

to which this specification relates.

EXPLANATION OF REFERENCE NUMERALS

1 ROTARY HEARTH FURNACE

REGION DRYING CHAMBER PREHEATING CHAMBER COOLING CHAMBER

Claims

CLAIMS 1. A metal oxide smelting method comprising a reduction treatment step including: a drying step in which a mixture obtained by mixing a metal oxide and a carbonaceous reducing agent is dried at a temperature of 5000 C or lower by blowing hot air to the mixture, the metal oxide being a nickel oxide ore; a preheating step in which the dried mixture is preheated at a temperature of 600 0 C or higher and 12800 C or lower; a reduction step in which the preheated mixture is reduced using a rotary hearth furnace, the rotary hearth having a hearth that rotates and not having a partition structure in an interior; and a cooling step in which the obtained reduced product is cooled.
2. The metal oxide smelting method according to claim 1, wherein in the drying step, the mixture is dried by blowing hot air set at 2500 C to 3500 C to the mixture.
3. The metal oxide smelting method according to claim 1 or 2, wherein the reduced product obtained through the reduction step is subjected to a temperature maintenance step in which the reduced product is maintained at a prescribed temperature in the rotary hearth furnace, and after maintained for a prescribed time, the reduced product is supplied to the cooling step.
4. The metal oxide smelting method according to claim 3, wherein a treatment in the reduction step and a treatment in the temperature maintenance step are performed using the same rotary hearth furnace.
5. The metal oxide smelting method according to any one of claims 3 or 4, wherein the reduced product is maintained at a temperature of 13000 C or higher and 1500 0 C or lower in the temperature maintenance step.
6. The metal oxide smelting method according to any one of claims 1 to , wherein in the reduction step, reduction is performed while a reducing temperature is set to 12000 C or higher and 15000 C or lower.
7. The metal oxide smelting method according to claim 6, wherein in the reduction step, the mixture is reduced at reducing temperatures of two steps, the reducing temperature at the first step is 12000 C or higher and 1450 0C or lower, and the reducing temperature at the second step is 13000 C or higher and 1500 0C or lower.
8. The metal oxide smelting method according to claim 7, wherein the rotary hearth furnace includes a plurality of heating sources, and a temperature distribution inside the rotary hearth furnace is controlled by controlling an amount of energy supplied to each heating source.
9. The metal oxide smelting method according to any one of claims 1 to 8, wherein the mixture to be dried in the drying step is obtained through a mixing treatment step in which at least a metal oxide and a carbonaceous reducing agent are mixed to obtain a mixture, and a pretreatment step in which a treatment of forming the obtained mixture into a lump product or a treatment of filling the mixture in a prescribed container is performed.
10. The metal oxide smelting method according to any one of claims 1 to 9, further comprising a separating step in which the reduced product cooled in the cooling step in the reduction treatment step is separated into a metal and slag and the metal is recovered.
11. The metal oxide smelting method according to any one of claims 1 to , wherein the reduced product contains ferronickel.