J. Electroanal. Chem., 118 (1981) 375--380
375
Elsevier Sequoia S.A., Lausanne -- Printed in The Netherlands
CHALLENGES
W.E. Alcoa
FACING
THE A L U M I N U M
INDUSTRY
HAUPIN Laboratories,
New Kensington,
Today
Aluminum
PA
Company
(U~S.A.)
is a c h a l l e n g i n g
a time of opportunity~
time
for the a l u m i n u m
The a l u m i n u m
efficient
in the use of energy,
petroleum
coke.
proving
It must
as new t e c h n o l o g y
society.
that have
industry
to combat
not to c o m p r o m i s e In this paper the b u s i n e s s
to p r o m o t e
inflation.
one goal I will
because
concentrate
this
is where
Indeed,
the need to improve
Let's
through
industry
Each a d d i t i o n a l
is well
known
Productivity
improvement,
constructed. increases
to the square
pro-
part of
lies.
This
face no problems.
and p r o d u c t i v i t y
In the past
comes more
inflation density
extends
But today
struction
so high
that
with o l d e r plants
while
power heat
comes at the expense
provided
capital
has p u s h e d
at much
than the It
efficiency. generation
Therefore,
cells or larger
it is d i f f i c u l t
built
increases
the
in half.
difficult
density.
new technology
inflation
forty years
nearly
is an inhibitor.
density,
of c u r r e n t
the a d d i t i o n a l
and equipment.
compete
industry
requirements
to c u r r e n t
additional
In the past,
costs
increase
on the s m e l t i n g
efficiency
by this route
either
that e x c e e d e d
but
current
is p r o p o r t i o n a l
Thus,
to The
must be careful
of my e x p e r i e n c e
of the
however,
go further,
power e f f i c i e n c y
ductivity.
benefits
fabrication.
that l o w e r i n g
is p r o p o r t i o n a l creased
energy
It must
the i n d u s t r y
a
uses
fit this category.
mainly most
has cut its e n e r g y
We can still
and e c o n o m i c
those
another.
talk about e n e r g y efficiency.
aluminum
last.
sectors
and im-
It must m a i n t a i n
recycling~
Finally,
in a c h i e v i n g
is not to imply that other
from m i n i n g
social
more
energy
the environment,
It must promote
uses p a r t i c u l a r l y
but also
must become
this possible.
the g r e a t e s t
must continue
industryt
electrical
to p r o t e c t
environment.
Transportation
ductivity
makes
in d u s t r y
particularly
continue
safe and h e a l t h y w o r k i n g of a l u m i n u m
of A m e r i c a
in-
of pro-
cells must be productivity
cost of n e w plants equipment
and con-
for a new p l a n t
lower costs.
to
Improvements,
376
therefore,
that can be r e t r o f i t t e d to the present process,
avoiding
the high capital cost of e n t i r e l y new e q u i p m e n t and/or new plants, are highly desirable~ There is much that can be done along this line.
Just m a i n t a i n i n g
the e l e c t r o l y t e c o m p o s i t i o n and t e m p e r a t u r e at known o p t i m u m conditions could increase power e f f i c i e n c y at least 3-5%. as it may seem,
Incredible
the a l u m i n u m industry r o u t i n e l y operates its s m e l t i n g
cells w i t h o u t automatic t e m p e r a t u r e control;
and yet every degree
Celsius above the o p t i m u m o p e r a t i n g temperature costs at least onehalf p e r c e n t in current efficiency.
It is not that the a l u m i n u m
industry is in the dark ages; there is no known t e m p e r a t u r e sensor that will survive for long in the a g g r e s s i v e e n v i r o n m e n t of the smelting cell.
Solving this p r o b l e m is an important challenge.
A n o t h e r o p p o r t u n i t y is i m p r o v e d alumina c o n c e n t r a t i o n control. Most plants today use some form of a u t o m a t i c
feeding of alumina,
and there are many schemes based on the cell v o l t a g e - c u r r e n t - t i m e r e l a t i o n s h i p to sense the alumina c o n c e n t r a t i o n in the electrolyte. The c a l c u l a t i o n s g e n e r a l l y require the use of a computer.
Still,
even the best c o n t r o l l e d cells frequently e x p e r i e n c e anode effects-a c o n d i t i o n i n d i c a t i n g i n s u f f i c i e n t alumina concentration. effect,
At anode
c e l ~ voltage rises 6 to 7-fold, w a s t i n g energy and g e n e r a t i n g
carbon tetrafluoride.
A l t h o u g h carbon t e t r a f l u o r i d e is nontoxic and
does not cause ozone depletion,
as c h l o r o f l u o r o c a r b o n s
do, it still
r e p r e s e n t s a loss of fluoride.
On the other hand, e x c e s s i v e
feeding
causes some alumina to settle u n d i s s o l v e d under the m o l t e n a l u m i n u m at the b o t t o m of the cell, where it acts as an e l e c t r i c a l raising the cell voltage.
insulator,
Improved alumina sensing and feeding
m e c h a n i s m s that will handle equally well alumina from d i f f e r i n g sources,
offer c h a l l e n g e s with big p o t e n t i a l payoffs.
The c a l c i u m fluoride c o n c e n t r a t i o n and ratio of sodium fluoride to a l u m i n u m fluoride in the e l e c t r o l y t e change slowly enough that p e r i o d i c sampling,
coupled w i t h a u t o m a t e d analysis,
good control of these variables.
However,
can p r o v i d e
good sampling p r a c t i c e
must be e s t a b l i s h e d and adhered to, and a u t o m a t e d a n a l y t i c a l equipment must be checked frequently. R e p l a c i n g the p r e s e n t carbon c a t h o d e s with r e f r a c t o r y h a r d metals, such as t i t a n i u m diboride,
is a r e t r o f i t we think could save up to
25% of the electrical energy p r e s e n t l y used by H a l l - H e r o u l t cells. This b e n e f i t results from r e d u c i n g the cathode voltage loss and by stabilizing the cathode surface,
thereby a l l o w i n g closer anode-
377
cathode novel
spacing.
cathode
needed.
designs
Refractory
very easily. this
Refractory
hard metals
are r e q u i r e d
hard m e t a l s
Improved
to reduce
the amount
also are brittle
fabricating
techniques
hence,
of m a t e r i a l
and tend to crack
are n e e d e d
to o v e r c o m e
limitation.
Inert anodes greater
have p o t e n t i a l
potential
trode,
fluoride
decomposition effect
potential
of carbon
0.5 volt
for carbon
in area
by the
increase greater
full cross
as they are consumed.
share
While
overall
of the load.
energy
energy--and
process.
represents
I mentioned
current
cathode.
higher enters
in Figure cathode,
surface
an anode. mately
cases,
i.
the r e m a i n d e r
strides
anode
efficiency.
at a terminal these
two terminal
flows
of each plate
becomes
a cathode
a cell with
ii b i p o l a r
as much a l u m i n u m
a number
plates
intermediate and the
plates
is one
electrode
at a terminal
from terminal
these
it
problems.
electrodes
isolated
through
Hence,
literature
for the Hall-
unsolved
electrodes,
it passes
12 times
the elec-
in recent years
and exits
but e l e c t r i c a l l y As c u r r e n t
can be used
In a b i p o l a r
anode
is petro-
and i m p l e m e n t i n g
that the use of b i p o l a r energy
it is an
represents
inert anode
still
of
are p l a c e d
anode
to
plates. second
would produce
as a c o n v e n t i o n a l
their
spacing.
carbon
Patent
been made
this d e v e l o p m e n t with many
carry
plant producing
processes. have
is
of the i n c r e a s e d
oxygen w h i c h
of the power
area
standoff,
of carbon
because
inert
decrease
a process
anode-cathode
energy
consumption source
no e f f e c t i v e anodes,
about
since
anodes
the new anodes
of a s a t i s f a c t o r y
conductive
terminal first
great
earlier
as shown
is com-
area,
carbon
carbon
also p r o d u c e
challenge
In b e t w e e n
electrically
cold before
other c o m b u s t i o n
Refining
another
way to achieve cell,
energy
the d e v e l o p m e n t
Heroult
voltage
0.i volt versus
anode
while
in an e l e c t r i c a l
efficiency
indicates
average
for by n a r r o w e r
Inert anodes
boiler
or improve
(Ref~. 1-8) toward
In most
saving because
leum derived.
tricity
result
a critical
to increase
the
caused by inert anodes,
Additionally,
setting of large
can be c o m p e n s a t e d
this w o u l d
elec-
raise
the d e p o l a r i z i n g
(about
section
that can take eight or more hours
voltage
into a b i p o l a r
inert anodes
increased
overvoltage
0.45 volt
their
lost by the daily
W hi l e
some of this
anodic
is r e c o v e r e d
maintain
cell.
but even
anodes).
Of the r e m a i n i n g 0.2 volt
application
about one volt because
is lost,
for by lower
anodes
for r e t r o f i t
if they can be i n c o r p o r a t e d
electrolysis
pensated
full
are very expensive;
The
surface approxi-
cell w i t h m o n o p o l a r
378
II F i g u r e 1 - B i p o l a r E l e c t r o d e Cell Used in A l c o a S m e l t i n g Process, U.S. Pat. 4133727
electrodes,
o p e r a t i n g at the same current.
of such a cell
the anodes
should not be consumable.
In d e s i g n i n g the A l c o a
S m e l t i n g Process,
c h l o r i d e e l e c t r o l y t e and the e l e c t r o l y s i s o r d e r to avoid c o n s u m a b l e anodes. at the anode.
Obviously,
we chose a less a g g r e s s i v e
of a l u m i n u m c h l o r i d e
Aluminum chloride produces
in chlorine
E l e c t r i c a l l y c o n d u c t i v e m a t e r i a l s r e s i s t a n t to hot
c h l o r i n e are available.
However,
this r e q u i r e d that the a l u m i n a
first had to be c o n v e r t e d to a l u m i n u m c h l o r i d e b e f o r e b e i n g fed to the A l c o a
S m e l t i n g P r o c e s s cell.
Chlorine
from the cell is r e c y c l e d to an a d j a c e n t c h e m i c a l p l a n t
to p r o d u c e m o r e a l u m i n u m c h l o r i d e
for the cell.
This cell
saves
379
over thirty percent of e l e c t r i c a l energy r e q u i r e d by our best HallHeroult cells.
Also, being c o m p l e t e l y enclosed,
it is e n v i r o n m e n t a l l y
more acceptable than H a l l - H e r o u l t cells. A n o t h e r p o s s i b l e way to c i r c u m v e n t the need for scarce p e t r o l e u m coke is through the use of solvent refined coal. fications,
the SRC process is able to produce not only anode q u a l i t y
coke, but also a solid, sulfur,
With various modi-
sulfur-free
fuel, both light and heavy oils,
and fuel gas.
Alcoa, w i t h U.S. g o v e r n m e n t assistance,
is looking at direct carbo-
thermic r e d u c t i o n of low grade bauxite and clay as another p o s s i b l e method for p r o d u c i n g both fuel gas and aluminum.
It is a n t i c i p a t e d
that little e l e c t r i c a l power will be r e q u i r e d by the process and, if successful,
it will produce large q u a n t i t i e s of carbon m o n o x i d e
for fuel or other chemical processes,
a l u m i n u m - s i l i c o n alloys suitable
for castings,
ferrosilicon which can be used
and a l u m i n u m - c o n t a i n i n g
by the M a g n e t h e r m Process to produce m a g n e s i u m from dolomite. The greatest energy and raw m a t e r i a l s saving, however, able through recycling.
is avail-
Recycled a l u m i n u m requires less than 5% of
the energy needed to produce virgin metal. to be d o w n g r a d e d w i t h r e p e a t e d recycling.
The metal,
to restore the metal to its original purity. challenge to the a l u m i n u m industry.
however,
This r e p r e s e n t s another
Much of the world,
larly the United States, has become a t h r o w a w a y society. tant but n o n - m e t a l l u r g i c a l
challenge
tends
Techniques are being studied
and particuA concomi-
is to work to generate a cultural
change from a t h r o w a w a y society to a c o n s e r v i n g society that will recycle its scrap. E n v i r o n m e n t a l concern is not new to the a l u m i n u m industry.
Alcoa
started i n s t a l l i n g fluoride p o l l u t i o n control e q u i p m e n t at its smelting plants improved, equipment.
four decades ago.
Many of our older plants,
as t e c h n o l o g y
are in the second or third g e n e r a t i o n of fluoride control The o r i g i n a l equipment,
e l e c t r o s t a t i c precipitators,
c o n s i s t i n a of wet scrubbers and
has been largely r e p l a c e d by dry scrubbers
that are both more e f f i c i e n t and return the c a p t u r e d fluoride to the smelting cells.
Fluxing of metals,
once a p o l l u t i o n generator,
been c o n v e r t e d to fumeless fluxing methods.
has
Alcoa'has developed a
"Thermopure" water t r e a t m e n t system that uses waste heat to p u r i f y waste water by low temperature distillation.
The industry is con-
t i n u a l l y striving to do a better, more e f f i c i e n t job in e n v i r o n m e n t a l control. dust.
A l c o a is w o r k i n g on sealed ore buckets to reduce fugitive
We are also trying to improve our methods for used p o t l i n i n g
380
disposal.
Fluoride
emission
of the cost of an a l u m i n u m cost,
based on a cost
Institute
(Ref.
Some people much e l e c t r i c
control
smelting
study by the
have c r i t i c i z e d
quired
in the d e s i g n energy
to produce
aluminum
I would
of an a u t o m o b i l e
vehicles
the v e h i c l e s
the a l u m i n u m
produced
like
lifetime
inflation,
plants
modernization centive
make one
to modernize.
a cost e f f e c t i v e resist
efficiency governments
the easy route
to balance
the vicious
required
my concern
has
forced
lifetime
of re-
the a l u m i n u m
used
save more
to make
When
break
all of
their budgets
to incosts
for the more that
is little
cycle.
We must
in-
We must
incorporate
into all m o d e r n i z a t i o n . productivity
and
stop d e f i c i t
Perhaps
our
financing
Together this
We
to gain e n e r g y
We must also e n c o u r a g e
productivity.
cycle.
adds
in advance
there
this vicious
productivity.
control.
control
inflation.
new c o n s t r u c t i o n
one knows
increase
about
no longer pay
of s a c r i f i c i n g
inflationary
substituted
last year.
while we do our part by i n c r e a s i n g break
In fact,
less competitive,
productivity
it uses
the energy
last year will
gain will
We must
because
times
and e n v i r o n m e n t a l
to increase
or e n v i r o n m e n t a l
i0).
than was
in turn,
and equipment.
will
all work d i l i g e n t l y
must
8-12%
an energy bank
of a l u m i n u m
three
by r e s t a t i n g
so high that the p r o d u c t i v i t y efficient
(Ref.
in the U.S.
to c o n c l u d e
industry
saves over the
to over
in the U.S.
The high cost of both e n e r g y flation while
about
Primary A l u m i n u m
represents
Each pound
equivalent
the a l u m i n u m
in land and marine energy over
International
the a l u m i n u m
Actually
that can be used over and over. for steel
represents
and 1-3% of its o p e r a t i n g
9).
power.
the a u t o m o b i l e
alone p la n t
we can
is our g r e a t e s t
challenge.
REFERENCES 1 2 3 4 5 6 7 8 9
B. Marincek, U.S. Patent 3,562,135 (1971). B. Marincek, U.S. Patent 3,692,645 (1972). K. Yamada et al, German Patent a p p l i c a t i o n 2,547,168 (1976). K. Yamada et al, British Patent 1,461,155 (1977). H. Klein, U.S. Patent 3,718,550. H. Alder, U.S. Patent 3,960,678 (1976). H. Alder. U.S. Patent 3,930,967 (1976). H. Alder, U.S. Patent 4,057,480 (1977). I n t e r n a t i o n a l P r i m a r y A l u m i n u m Institute E n v i r o n m e n t a l C o m m i t t e e Report, "Fluoride E m i s s i o n Control: Costs for New A l u m i n u m R e d u c t i o n Plants," April 1975. i0 A l u m i n u m A s s o c i a t i o n Report TI2, "Use of A l u m i n u m in A u t o m o b i l e s - Effect on the Energy Dilemma," April 1980.