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 silicon-metal , silicomanganese and ferromanganese 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 carbon or electrolysis can be used to break the European mix of energy sources. COremissions connected to coke 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 ferroalloy 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
-89-
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damages damages
caused caused
ferrosilicon ferrosilicon
In In
amount amount by by
been been the the
carbon carbon
the the ferrosilicon ferrosilicon
The The
bio-carbon bio-carbon
process. process.
dioxide dioxide
among among
covers covers
biological biological
pyrolysis, pyrolysis,
new new
and and
interested interested programme programme
wi wi
reducing reducing carbon. carbon.
There There $/tonne $/tonne
regions, regions,
Today Today bringing bringing
production production to to
The The
make make
Norwegian Norwegian
especially especially wood) wood)
a a
coal coal
been been
million million
km
material material
In In
In In
examples examples
production production
Looking Looking
II II
report report
most most
be be
addition addition
good good
2 2
baghouses, baghouses,
other other
processed processed
early early
threat threat
kg kg
not not
of of
use use
or or
found found
plants plants
done done
the the
a a
in in
are are
others others
by by
available available
dioxide dioxide
about about
homogeneous homogeneous
coke. coke.
all all
Si0
The The
formed formed
of of tonnes tonnes
Fix Fix
substantial substantial
regions regions
to to
used used
contribute contribute
practise practise
agents agents
But But
and and
of of
about about
the the
the the
development development
parties parties
regions regions
an an
a a
back back
of of
use use
sufficient sufficient
for for
plants plants
raw raw
of of
seventies, seventies,
as as
only only
of of
the the
2 2 and and
aspects aspects
for for
plants plants of of
Ferroalloy Ferroalloy
major major
and and
price price
Carbon). Carbon).
to to
bio-carbon,which bio-carbon,which in in
overexploitation overexploitation
increased increased
per per
possible possible
with with
Brazil Brazil
same same
a a
copper copper
the the
costs costs
this this
the the
is is
10 10
of of
in in
of of
silicon-metal silicon-metal
biological biological
environment environment
material, material,
this this
from from
source source
85 85
adding adding
to to
The The
from from
bio-carbons bio-carbons
because because
charcoal charcoal
in in
charcoal charcoal
kg kg
in in
to to
trees
and and
Norway Norway ferroalloys ferroalloys
today
for for
% %
production production
volatiles volatiles
district district
were were
ferroalloys ferroalloys some some
disposal disposal
% %
the the
project project
bio-carbons. bio-carbons.
the the
price price
Si. Si.
waste waste
to to
increase increase
Recovery Recovery
the the
of of
is is
bio-materials bio-materials
down down
these these
and and
of of
Norwegian Norwegian
for for
charcoal charcoal
trees trees
raw raw
forests forests
. .
FFF FFF
restrictions restrictions
the the
for for
an an
demand demand
Producers Producers
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the the
atmosphere. atmosphere.
of of
The The
neighbourhood neighbourhood
Peat Peat
to to
using using
considerably considerably
Typical Typical
the the
it it
silicon-metal silicon-metal metallurgical metallurgical
but but
chips chips
iron. iron.
is is
exception, exception,
materials materials
bag bag
alone alone
heating
range range
made made
biological biological
greenhouse greenhouse
product, product,
sources sources
are are
has has
specific specific
has has
greenhouse greenhouse
the the
Bio-carbon Bio-carbon
huge huge
a a
and and
is is
problem. problem.
for for
like like
and and
for for
Fix Fix
and and
(double (double
supplies supplies
considered considered
will will
more more
of of
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filters filters
of of
from from
industry industry
bio-carbon; bio-carbon; grown grown
supported supported
is is
for for
started started
been been
greenhouse greenhouse
of more more
from from
The The
charcoal charcoal
forests forests
finally finally as as
silicon silicon
silicon-metal. silicon-metal.
increased increased
silicon silicon
by-products by-products
the the
. .
amount amount
Carbon Carbon
Research Research
on on
Research Research
ferrosilicon ferrosilicon
a a
probably probably
(deciduous (deciduous · ·
charcoal charcoal
is is
addition addition
wood wood
expensive expensive
as as
imported imported
these these
A A
general general
emissions emissions
to to
materials materials
more more
advantageous advantageous
COz-emissions COz-emissions
reckoned reckoned
industry industry
higher higher
ferroalloys ferroalloys
But But
or or
than than
or or
eucalyptus eucalyptus
the the
C0
giving giving
a a
roasted roasted
precondition precondition
collect collect
effect, effect, of of
history, history,
to to
metal. metal.
will will
using using
planted, planted,
yields yields
research research
triple) triple)
like like
of of
2 2
Brazilian Brazilian
sources sources
used used
many many
the the
and and
by by
produced produced
produce produce
than than
watersheds watersheds
100 100
is is
felling, felling,
will will
Association Association
effect effect
silica silica
Council. Council.
to to
than than
not not
term term
be be
respectively respectively
that that
coal coal
will will
charcoal charcoal
carbon carbon
ferroalloys ferroalloys
as as
the the
silica silica
is is
woods woods
to to
because because
it it
OOO OOO
Up Up
wood wood
cement cement
charcoal charcoal
95 95
now now
from from
in in
in in
cause cause
applications applications
we we
only only
be be
haulm haulm [6]. [6].
be be
from from
as as
industry industry
in in
what what
can can
at at
project project
dust dust
have have
for for
% %
to to
the the for for
to to
a a
"KLIMATEK"
charcoal charcoal
prodiiction prodiiction
the the
tonne tonne
we we
transportation, transportation,
assimilated assimilated
has has
dust dust least least
the the
for for
counted counted
are are
in in
nave nave
deforestation deforestation
of of
and and
Abo
m'lterial m'lterial
now now
and and
supply supply
be be
The The
and and
other other
silicon silicon
all all
collected collected
the the
one one
use use
in
bio-carbon
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
bio
The The
of of
and and
400 400
and and
[7]
the the
has has
for for
the the
b) b)
in in
in in
to to
in in
at at
a a
I I
, ,
. .
. .
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
.
coal. coal.
5 5
energy energy
the the
cement cement
For For
input input
cement. cement.
silicon-metal silicon-metal
development development
bag bag
. .
cement cement
kg kg
for for
as as use use
flow flow
the the
The The
to to
the the
in in
sixties sixties
of of
0 FeSi:
the the
the the
Si: Si:
approx. approx. of of
by by
36 36
If If
of of
to to
can can
a a
filters, filters,
this this
recover recover of of
electric electric
per per
off-gas off-gas
the the
natural natural
is is
1 1
C02 C02
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
-
weight) weight)
( (
of of
can can
above above
roughly roughly
sealed sealed
16 16
(8). (8).
energy energy
0.38*2.5) 0.38*2.5) silica silica
-
per per
6 6
replaced replaced
.
credit credit
which which
54 54
high high
for for
emission emission
c
24*2.5/0.75) 24*2.5/0.75)
heat heat
-
the the
instead instead
application. application.
about about
for for
Nm
.
gas gas
Nm
energy
oncrete. oncrete.
*)
silicon-metal silicon-metal
expect expect
gas gas
70 70
the the
70 70
emissions. emissions.
of of
The The 50 50
it it and and
50 50
tonne tonne
from from
ferroalloy: ferroalloy:
GJ GJ
. .
scrubbers) scrubbers)
heat heat gas gas
the the
heat heat
gas gas with with
dust dust
3
250 250
3
is is
% %
generation, generation,
% %
furnaces furnaces
/kWh /kWh
C02 C02
% %
/kWh /kWh
% %
is is
replacement replacement
is is
as as
will will
semiclosed semiclosed
for for
collect collect
proportional proportional
the the
20 20
per per
silicomanganese silicomanganese
equivalent equivalent
clean clean
for for
CO CO
. .
CO CO
equivalent equivalent
CO CO
solution solution
CO CO
used used
by by
or or
volume volume
a a
to to
* *
Energy Energy
of of
generation generation
FeSi FeSi
can can
800 800
huge huge
per per
°C. °C.
generation generation
this this
% %
It It
-
C02 C02
ferrosilicon ferrosilicon
increase increase
1000 1000
the the
tonne tonne
silica silica
for for
recover recover
in in
emission emission
and and
in in
[8]. [8].
in in
in in
coal coal
of of
has has
The The
tonne tonne
gas gas
replace replace
* *
Giving Giving
for for
Cooling Cooling
the the
means means
°C. °C.
off-gas: off-gas:
off-gas
produced, produced,
off-gas: off-gas:
off-gas: off-gas:
bag bag
amounts amounts
1000 1000
heat heat
-
and and was was
the the
kg= kg=
the the As As
emissions emissions
is is
will will
as as
dust dust
even even
containing containing
recovery recovery
Si. Si.
addition addition
generation generation
silica silica
to to
is is
furnaces furnaces
with with
to to
Cooling Cooling
input input
filters filters
ferroalloy: ferroalloy:
highly highly
up up
a a
the the
or or
generation. generation.
an an
gas-temperature gas-temperature
the the
kg.= kg.=
to to
removal removal
removing removing
3 3
The The
that that
950 950
or or
for for
removing removing
be be
equivalent equivalent
: :
substitute substitute
ferrosilicon ferrosilicon
and and
650 650
to to
450 450
electric electric
kg kg
350 350
been been
250 250
furnace furnace
the the
established established
dust, dust,
capital capital
I I
the the
of of
strength strength
electric electric
electrical electrical
to to
FeSi FeSi
and and
800 800
15 15
kg kg
kg kg
we we
releases releases
cement. cement.
most most
still still
of of
wanted. wanted.
air air
kg kg
kg kg
produce produce
kg kg
are are
off-gas off-gas
kg kg
this this
where where
% %
volumetric volumetric
50 50 found found
of of
silica silica
silica silica
can can
cannot cannot
kg kg
from from
C0
is is
of of
C0
and and C0
C0
the the
the the
power power
0.8 0.8
as as
requirement requirement
has has
the the
economical economical
electricity, electricity,
for for
If If
to to
possible, possible,
power power
gas gas
2
to to
deduct deduct
2
the the
(compressive (compressive
2 2
electric electric
2
concrete concrete
and and
following following
energy. energy.
there there
vast vast
950 950
/tonne /tonne
dust dust 70% 70%
/tonne /tonne
-
dust dust
/tonne /tonne
/tonne /tonne
This This
following following
practice practice
a a
natural natural
from from
that that
an an
the the
electric electric
be be
l l
removing removing
in in
generation generation
silicon-metal silicon-metal
.O .O
down down
dust dust
silicon-metal silicon-metal
kg kg
enthalpy enthalpy
amounts amounts
will will
(10-30 (10-30
the the
exposed exposed
CO CO
is is
kg kg
part part
off-gas off-gas
has has
generation generation
gas gas
800 800
SiMn SiMn
SiMn SiMn
but but
the the
energy energy
FeMn FeMn
FeMn FeMn
per per
no no
will will
gas, gas,
we we
C0
off-gas off-gas
by by
for for
energy. energy.
use use
already already
remove remove
C0
can can
led led
to to
kg kg
of of
C0 flow, flow,
gives gives
open open
other other
tonne tonne
can can
2 2
% %
gain gain
the the
oil oil
wet wet
2
the the
and and
an an
of of
per per of of
of of
per per
the the
-
to to
to to
2 2 be be
is is
of of
of of
-
power power
FeMn FeMn
to to
FeMn FeMn
In In Net Net
FeSi FeSi
Si Si
FeSi75 FeSi75 Si-metal Si-metal SiMn SiMn
Si-metal Si-metal
FeMn FeMn
Energy Energy
Si Si
Si-metal Si-metal
FeSi75 FeSi75
SiMn SiMn
Recovery Recovery
FeSi75 FeSi75
SiMn SiMn Fe Fe Si-metal Si-metal
Fe Fe Si-metal Si-metal
FeSi FeSi
Ferroalloy Ferroalloy
Using Using
Using Using
can can
Silicon-metal Silicon-metal
We We Silicon-metal Silicon-metal
Ferrosilicon Ferrosilicon following following
Ferrosilicon Ferrosilicon
Situation Situation
;; ;;
0 0
.! .! ......
u u
N N
!}. !}.
s s
" "
"' "'
g g
......
~ ~
c c
c c
Mn Mn
Mn Mn
reduce reduce
Fig. Fig.
Mn Mn
Mn Mn
C02 C02
4000 4000
make make
6000 6000
will will
8000 8000
2000 2000
Fig
75 75
75 75
including including
sources sources
20 20
3 3
the the
recovery recovery
. .
-
the the
sum sum
3 3
COi-emissions. COi-emissions.
of of % %
where where
Table Table
to to
emissions: emissions:
off-gas off-gas
C0
C0
silica silica
net net
biu-carbun biu-carbun
production: production:
reduce reduce
production production
up up
2 2
production: production:
production: production:
taking taking
/Nuclear /Nuclear
-3000 -3000
-2000 -2000
Hydro-
-
1190 1190
1350 1350
present present
2 -310 -310
-250 -250
-450 -450
-950 -950
COi-emissions COi-emissions
-800 -800
-910 -910
-876 -876
704 704
Adding Adding
-emissions -emissions
present present
2000 2000
2050 2050
8. 8.
4550 4550
4380 4380
emission emission
the the
0 0
0 0
0 0
O O
instead instead
dust: dust:
Possible Possible
C0
different different
credit credit
The The
2 2
and and
in in
and and
-
up up
: :
of of
per per
2800 2800
emissions emissions
pruducliun pruducliun
Ferroalloy Ferroalloy
2000 2000
3000 3000
for for
different different with
4200 4200
reductions reductions
possible possible
possible possible
coal coal
possible possible
Proceedings Proceedings
contributions contributions
Natural Natural
tonne tonne
-3000 -3000
-2000 -2000
4690 4690
4224 4224
2480 2480
2990 2990
present present
-250 -250
-450 -450
7900 7900
3130 3130
3850 3850
9550 9550
-950 -950
-800 -800
-876 -876
-910 -910
are are
gas gas
kg kg
kg kg
kg kg
0 0
0 0
0 0
O O
is is
kg kg
C0
plotted plotted
equivalent equivalent
C0
C0
ferroalloy: ferroalloy:
C0
and and
C0
contributions contributions
contributions contributions
of of
2
and and
in in
2 2
2
/tonne /tonne
2
/tonne /tonne
2 /tonne /tonne
FeSi FeSi
greenhouse greenhouse
/tonne /tonne
-contributions -contributions
C0
power power
for for
possibl'e possibl'e
10740 10740
-4200 -4200
-2800 -2800
the the
16800 16800
3896 3896
5400 5400
8528 8528
13004 13004
4646 4646 -350 -350
-650 -650
6460 6460
-950 -950
-800 -800
-910 -910
-876 -876
Coal Coal
2 2
0 0
0 0
0 0
O O
and and
different different
-
to to
FeSi FeSi
ferroalloys ferroalloys
FeSi FeSi
Si Si
emissions emissions
Si Si
of of
sources sources
removing removing
Si-metal Si-metal
contributions contributions
are are
INFACON 8 INFACON
effects
• •
• •
c c
UCPTE-mix UCPTE-mix
Hydro-/Nuc:] Hydro-/Nuc:]
electric electric
not not
UCPTE·mix UCPTE·mix
-3000 -3000
-2000 -2000
Natural Natural
4690 4690
4224 4224
2480 2480
2990 2990
-250 -250
-450 -450
7900 7900
3130 3130 -950 -950
3850 3850
-800 -800
9550 9550
-876 -876
-910 -910
industry industry
the the
0 0
0 0
. . 0 0
O O
included: included:
-91-
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
,
Electric
Saur,
Producers
a been has
INFACON
the
Stiftelsen
,
fiir
Silicon-metal
private
"Disposal
Outlooks"
Energiesy
2
"Current
furnace
in
and
895-900.
.
off-gas
die
"Principles
T
"The
und
No.
Ed.,
1
H.
a
.
in
Lindstad,
and
et.al.
Bytownite-Cryolite Z
Furnace
of
Schweiz.
Electric
Lerche
the
.
8193,
den
communic
Liu New
0stfoldforskning,
Brazilian
financially
;
Acknowledgement
.),
Norway
8, of
and
Research
it
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s
of
,
Norwegian
:
temen
:
Proc.
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caused
is
Trondheim
we
"Preparatio
.
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York,
tus
References
7
and
Ra
of
INFACON
Proceeding
Furnace
possible
H
recover
July
Bunde
see
.
Extractive
of
adal
Tveit
INFACON
und
Ferr
a
Ferro
age
tion
from
Ferroalloy
(NFR).
by
1983,
that
1997.
s
Association
and
von
Ferro
den upported
sa os
n
,
ferroalloy
Proceedings
,
to
M
:: with
by-product
a
fiir
mtes
ilic
by
Submerged
1995
lloy
s, Melt",
E
445.
~
.
Energiesystemen
Einbezug
get
Bruno
Fredrikstad,
·
.
o
den
metallurgy",
Erstad:
1975,
using
Alloy
Th
Pure
author,
s
n
8
8
fiir
s
,
a
,
Industry
Production"(In
ey
165-177
Emission
Trondhe
ok
usata reduction substantial
Metal!.
by
production
Energiewirthsch
and
Silicon
Vol
partly
Industry
lo
are
(FFF)
"Increa
Vol.
(silica-dust)
gisc NTNU,
von
The
Arc
L.N
33
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.
I
im,
both
Tran
h
McGraw
996.
Current
(20
33,
,
Furnaces
Control"
by
y en
Norwegian
pp
gaard:
se
"
and
in
,
.
1995
July
d
1975
s.
%
39-46.
greatly
Use
)
B,
,
,
bio
The
and
af
,
,
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