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The Proceedings of INFACON 8

Co2-Emissions and the Ferroalloys Industry

Tor Lindstad

SINTEF Materials Technology Alfred Getz vei 2B, N-7034 Trondheim, Norway

Abstract Thermodynamfcal Premises

COrcmissions connected ·with :. the production of ferrosilicon, Metal oxides are the only raw materials for ferroalloys, except that -metal , silicomanganese and are discussed. scrap iron is often used to supply the iron part. The Gibbs energy The specific COz-emission is given for different ways for needed to decompose the oxides to metal and oxygen are so high generating electric power; hydro-/nuclear, natural gas, coal and a that only solid or electrolysis can be used to break the European mix of energy sources. COremissions connected to binding between the metal atom and oxygen, as the case is for production are included. Otherwise the paper has not taken into aluminium and silicon. For manganese and chromium oxides, part account the contribution to COz-emissions from mining raw of the oxygen (in the higher oxides) can also react with carbon material, or transport of raw materials and products. The use of bio­ monoxide or hydrogen. carbon as a source for carbon is discussed. Present and possible contributions to the global C0 2-balance by using by-products and Breaking the metal-oxygen binding by electrolysis is the process recovering energy from off-gases are discussed. used for production of aluminium, but is also theoretically possible for silicon and is used for the production of manganese metal. We will take a closer look on electrolysis as a possibility to reduce C0 2 Introduction emissions.

In the sixties, both the public and politicians became more aware of C02-emissions from the ferroalloys industry. Status environmental issues. New laws were passed in many countries, new regulatory agencies were established and public control of The sources for carbon dioxide - emissions are the reduction emissions and effluents were increased. Since then solving materials (coal and coke) and the power generation (if coal, oil or

environm~ntulproblems caused by our industry has been an gas is used). If coke is used, we should also include the emission of essential part of the rnerallurgist's work. One example is the si lica C02 from the coking process. Carbon dioxide generated from fumes evolved in production of forrosilicon and silicon-metal. After renewable carbon sources like charcoal is not included. The amount some years of research a process using bag filters to collect the of em issions depends on the processes and the technical standards. silica dust was developed. The large quantities of dust collected The numbers chosen for efficiency of the power plant, electric represented however a major disposal problem. A heavy research energy and carbon consumption per !onne are open for was started in the seventies to find applications for this waste discussion. The numbers in this paper are believed to represent product [ l ]. As we know many applications have been found, the good efficiencies. main one being the use as an additive to cement. To collect the silica dust in the off-gas it is necessary to cool the gas. This gives Power generation us the opportunity to recover huge amounts of energy, which directly has relation to the C0 2-problem. Table I. Power generation Energy source Process Thermal C0 2 - emissions We might say that until the last S years the industry's main efficiency, % kg C02/kWh environmental challenges have been to remove local and regional Natural gas Combined cycle so 0,40 pollution, dispose of waste products and use energy and other raw Coal Stearn turbine 33 0,98 materials in a reasonable way. The focus on greenhouse gases, C0 2 UCPTE-mix*) 0,40 in particular, changes dramatically the conditions for the ferroalloys Nuclear 0 industry.In this paper we will try to take a closer look on how the Hydroelectric 0 indu,iry can contribute, directly or indirectly to reduce C0 2 - crnis:~ions. *)UCPTE is abbrevi.ation for " Union pour la co-ordination de la production et du transport de electricite". The union consists of Belgium, Germany, France, Greece, Italy, Ex-Yugoslavia, Luxembourg, The Netherlands, Portugal, Switzerland and Spain. UCPTE-mix is 36.2 % nuclear power, l 5.2 % hydroelectric power, 9.5 % from gas, 9.6 % from oil and 29 % from coal [JO].

-87 - r The Proceedings of INFACON 8

18000 Coke production 16000

~14000 A typical coke for ferroalloys production contains 90 % C (78 % 'ii fix C). Assuming the content of volatiles in the coals to be 35 % ~ 12000 • Hydro-/Nuclear and in the coke to 12 % we have calculated the C0 2 - emissions ti!! 10000 • Natural gas from production of coke to be 1,0 kg C0 2 per kg coke. c Coal ~8000 ;:;. Ill UCPTE-mlx 0 6000 Ferroalloys production u .. 4oo6" ...: The relative amount of coal or coke used will vary from plant tc 2000 plant. If we, however, include the carbon dioxide emissions from

coke production, the specific C0 2 -emissions will be fairly constant FeSl 75 Si-metal SiMn FeMn for each type of ferroalloy, when good efficiencies are presumed for Ferroalloy all. This way of thinking will be correct on a global base, but is difficult when national quotas for emissions are on the agenda.

Figure 1 Total C0 2-emissions Table 2. COr emissions per tonne ferroalloy from electric furnace, including coke production 100,00

Ferroalloy From reduction From electrodes, From ore and Total 90,00 materials, kg C0 kgC0 flux, kg C0 2 2 2 kgC0 2 80,00 F<0Si75 4200 180 4380 70,00 Si-metal 4100 450 4550 60,00 • Hydro-/Nuclear Si Mn 1800 100 150 2050 • Natural gas- % 50,00 FeMn 1800 50 150 2000 0 Coal 40,00 Cl UCPTE-mix To evaluate the total carbon dioxide emissions caused by ferroalloy 30,00 production we add the emissions caused by power generation 20,00 (Table 3) times the power consumption, to the emissions from the 10,00

furnace including the coking process (Table 2) and get Table 4. 0,00 FeSi 75 Si-metal SIMn Fe Mn Ferroalloy The figures in Table 4 are visualised in Fig. 1, where the total COr emissions are plotted. ', Figure 2 -emissions as % of emissions with coal-power In Fig. 2 we have compared the different ways for power generation C0 2 by plotting the total C0 2 - emissions relative to the total emissions where coal is used for power generation (100 %),

Table 3. COi-emissions from the generated power used per tonne ferroalloy,

Ferroalloy Electric energy Electric power generated by: consumption kWh Hydro-/Nuclear Natural gas Coal UCPTE-mix FeSi 75 8800 0 3520 862 3520 Si-metal 12500 0 5000 12250 5000 SiMn 4500 0 1800 4410 1800 FeMn 2700 0 1080 2646 1080

Table 4, Total COremissions per tonne ferroalloy

Ferroalloy Electric energy Electric power generated by: consumption kWh Hydro-/Nuclear Natural gas Coal UCPTE-mix FeSi 75 8800 4380 7900 13004 7900 Si-metal 12500 4550 9550 16800 9550 SiMn 4500 2050 3850 6460 3850 FeMn 2700 2000 3130 4646 3130

-88- r The Proceedings of INFACON 8

Methods or ways to reduce C02-emissions manganese is low, of the order of 65 %. Since rather high cell voltages are used, about 5 V, the energy consumption is so high as In this discussion we will include credits the industry should have, 8.5 kWh/kg [2]. The costs for electrolytic manganese are if our industry's efforts to recover energy or by-products contributes substantially higher than for manganese in ferromanganese. to a reduction of C0 2 - emissions in other areas of activity. According to Metal Bulletin [3], the prices on June 12/13 1997 were:. I. More efficient production will of course contribute to a reduction, connected to both the use of less carbon and less Table 5. Prices for manganese in electrolytic manganese and electrical energy. Strong economic incentives support this trend, ferro manganese and are not necessary to comment further. In ferrosilicon production the typical electric energy consumption has been %Mn %C $/tonne $/tonne Mn reduced from 9800 kWh per tonne in 1977 to 8800 kWh per tonne Electrolytic manganese 99.7 1280-1380 1284-1384 in 1997. Ferromanganese standard 78 7.5 480- 500 615- 640 Ferromanganese medium C 80 <1.5 947- 991 1184-1238 2. Electrolysis is a possibility, but much more electrical energy is needed than in the submerged arc furnace. How the electricity is These differences in prices tell us why ferromanganese and not produced is important. manganese metal is used for alloying steel. At least that is the case when standard ferromangancse can be used.The next question is: 3. Bio-carbon. It is accepted that using carbon from natural sources Will a transition from ferromanganese to electrolytic manganese does not contribute to the greenhouse effect, because carbon give a reduction in C02 -emissions? The answer to this question dioxide formed by the oxidation of endogenous carbon are depends on the way the electricity is generated.The electric energy assimilated by new plants and trees. consumption for the production of ferromanganese is 2700 kWh/tonne FeMn (see previous chapter), which is equivalent to 4. Recovery of by-products. Silica dust can replace some of the 3460 kWh/tonne Mn. If the energy in the off-gases is recovered and cement in concrete. Since much C0 2 also is emitted in cement used for the production of electric energy, about 15 % of the input production, such a replacement might give a total reduction in COi­ electricity can be recovered (see chapter Energy Recovery). This emissions, and should consequently be recognised in an EPI­ reduces the net electric energy consumption to 2295 kWh/tonne indicator. FeMn, being equivalent to 2940 kWh/tonne Mn.

5. Energy recovery. We will discuss how energy recovered as heat Table 6 shows the changes in electricity consumption and C0 2 - or electrical energy should be assessed in an environmental emissions for a transition from ferromanganese to electrolytic performance indicator (EPI) for the plant. manganese.

The conclusion is that unless one has a lot of available hydroelectricity. it

Electrolysis is not even from an environmental point of view a good idea to ~hange from ferromanganese to electrolytic manganese. Manganese

Manganese metal is produced in an aqueous electrowinning process. Its standard reduction potential is 1.18 volts more negative than hydrogen. Manganese electrolysis is made possible by the high hydrogen overvoltage on manganese. The current efficiency for

Table 6. C0 2 -emissions for the production of ferromanganese and electrolytic manganese. Ail values given for a production of 1000 kg ( 1 tonne) Mn

FeMn: Electricity generated by: Hydro- Natural gas Coal UCPTE-mix Electric energy, kWh: 2940 2940 2940 2940

C0 2 emissions from el.gen., kg: 0 l 176 2881 1176

C0 2 emissions from C-red., kg: 2000 2000 2000 2000

C0 2 emissions sum. kg: 2000 3176 4881 3176

Electrolytic Mn: Electricity generated by Hydro- Natural gas Coal UCPTE-mix Electric energy, kWh: 8500 8500 8500 8500 C0 2 emissions·from el.gen., kg: 0 3400 8330 3400 C0 2 emissions sum, kg: 0 3400 8330 3400

Change in C0 2 emissions, kg: ~2000 224 3449 224

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amount amount by by

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process. process.

dioxide dioxide

among among

covers covers

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interested interested programme programme

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There There $/tonne $/tonne

regions, regions,

Today Today bringing bringing

production production to to

The The

make make

Norwegian Norwegian

especially especially wood) wood)

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examples examples

production production

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by by

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about about

homogeneous homogeneous

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regions regions

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Ferroalloy Ferroalloy

major major

and and

price price

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per per

possible possible

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Brazil Brazil

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source source

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Norway Norway ferroalloys ferroalloys

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% %

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district district

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project project

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price price

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silicon silicon

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amount amount

Carbon Carbon

Research Research

on on

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ferrosilicon ferrosilicon

a a

probably probably

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expensive expensive

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imported imported

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materials materials

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reckoned reckoned

industry industry

higher higher

ferroalloys ferroalloys

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triple) triple)

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sources sources

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and and

by by

produced produced

produce produce

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Association Association

effect effect

silica silica

Council. Council.

to to

than than

not not

term term

be be

respectively respectively

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coal coal

will will

charcoal charcoal

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ferroalloys ferroalloys

as as

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silica silica

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woods woods

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Up Up

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cause cause

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dust dust

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a a

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charcoal charcoal

prodiiction prodiiction

the the

tonne tonne

we we

transportation, transportation,

assimilated assimilated

has has

dust dust least least

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for for

counted counted

are are

in in

nave nave

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of of

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m'lterial m'lterial

now now

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supply supply

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other other

silicon silicon

all all

collected collected

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one one

use use

in

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is is

(about (about

to to

the the

Norwegian Norwegian

have have

and and

resulted resulted

the the

(FFF) (FFF)

excluding excluding

ferroalloy ferroalloy temperate temperate

90 90

· ·

estimated estimated

started started

are are

,

the the

per per

l,!t.15000 l,!t.15000

aimed aimed plants plants

0.24 0.24

obtained obtained

concrete concrete

compete compete

charcoal charcoal

possibil" possibil"

thinning thinning

erosion. erosion.

for for

process. process.

this this

of of

project project

t:

of of

several several

carbon carbon

severe severe

for for

% %

wood

used. used.

same same

extra extra

year, year,

used, used,

have have

as as

than than

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The The

of of

and and

400 400

and and

[7]

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has has

for for

the the

b) b)

in in

in in

to to

in in

at at

a a

I I

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r , ,

furnace furnace

emissions: emissions: expect expect

or or

the the

Using Using

approx. approx.

instead instead

channels channels

reduced reduced

the the acceptable acceptable heat heat

minimisation minimisation

baghouse baghouse

furnace furnace

The The

a a

Ferrosilicon Ferrosilicon

temperatures temperatures

FeMn-production, FeMn-production,

SiMn-production, SiMn-production,

Using Using

FeMn-production, FeMn-production, following following

emission emission

instead instead

SiMn-production, SiMn-production,

Typically Typically

Using Using

the the

The The

uses uses

scrubbing scrubbing used used

in in Ferromanganese Ferromanganese

for for

*)For *)For

tonne tonne the the

production production 2 being being

kg kg

In In

strength. strength. tensile) tensile)

cement cement

gas gas

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coal. coal.

5 5

energy energy

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cement cement

For For

input input

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silicon-metal silicon-metal

development development

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kg kg

for for

as as use use

flow flow

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to to

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in in

sixties sixties

of of

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Si: Si:

approx. approx. of of

by by

36 36

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of of

to to

can can

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recover recover of of

electric electric

per per

off-gas off-gas

the the

natural natural

is is

1 1

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we we

of of

natural natural

synthesis synthesis

major major

the the is is

is is

temperature temperature

mixing mixing

(Venturi (Venturi

of of

4 4 off-gas off-gas

GJ GJ

production production

C02 C02

gas gas

kg kg

gas gas

the the

the the

Thus Thus

be be

as as

for for

( (

energy energy

and and

specific specific

tonne tonne

-

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(8). (8).

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6 6

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.

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54 54

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24*2.5/0.75) 24*2.5/0.75)

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.

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*)

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950 950

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following following

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natural natural

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75 75

75 75

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Table Table

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off-gas off-gas

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1350 1350

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2 -310 -310

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704 704

Adding Adding

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present present

2000 2000

2050 2050

8. 8.

4550 4550

4380 4380

emission emission

the the

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0 0

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credit credit

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2 2

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2800 2800

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pruducliun pruducliun

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4200 4200

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possible possible

possible possible

coal coal

possible possible

Proceedings Proceedings

contributions contributions

Natural Natural

tonne tonne

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4690 4690

4224 4224

2480 2480

2990 2990

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7900 7900

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3850 3850

9550 9550

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10740 10740

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16800 16800

3896 3896

5400 5400

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Coal Coal

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INFACON 8 INFACON

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industry industry

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0 0

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Coal Coal gas gas Comparing energy carbon

The

This

Ferroalloy

in

acknowledged. Research

2. Hill

Energiesy Bio-carbon 5

Situation 76-79.

6. Europe", Norwegian)

3

7.

4. TSS-AIME, 9.

Proceedings

8. Okobilanzen Vergleich "Energy Electrowinning

-

Nov

I

115-7.

1996

1997.

10

. .

.

E

J the

T

A l

92

L.Kolbeinsen,

Metal

J

R.A.Person: .

.

.

.

R

Fageras

.

Thonstl)d

.

R.Stubergh

.

.

Book

Hallgren:

Rosenqvist:

D

,

.

1993.

work

Proceedings

total

-

vol.

Frischknecht

.

from

Melgaco:

in

Recovery

Bulletin

ISS-AIME

and

s

Co.,

von

Council

27B,

temen

COi-emissions

the

Figs.

in

,

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Saur,

Producers

a been has

INFACON

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Stiftelsen

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"Disposal

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furnace

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.

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Brazilian

financially

;

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.),

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1997.

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Proceedings

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445.

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Fredrikstad,

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o

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metallurgy",

Erstad:

1975,

using

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author,

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996.

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.

1995

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1975

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39-46.

greatly

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