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The Art of Dross Management - ALTEK

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By Alan M Peel, Managing Director, <strong>ALTEK</strong> Europe Ltd.


• What is Melt Loss ?<br />

• Main generators <strong>of</strong> melt loss<br />

• Ways to minimise melt loss,<br />

• will focus on furnace stirring<br />

i<br />

• Dealing with the consequence – DROSS<br />

• Economics <strong>of</strong> dross<br />

• Conclusions


DROSS !!


• Looked upon as the unfortunate evil <strong>of</strong> the<br />

industry<br />

• Often, dross is at the bottom <strong>of</strong> the cast<br />

house priority list (LOW PERCEIVED VALUE)<br />

• <strong>The</strong> quality and amount <strong>of</strong> dross generated<br />

can be a good indicator <strong>of</strong> efficiency in the<br />

cast house


• More than 1 million tpy <strong>of</strong> dross is produced<br />

from aluminium cast houses as a consequence<br />

<strong>of</strong> melt loss<br />

• This equates to more than US$ 600 Million<br />

in available aluminium* within the <strong>Dross</strong> !!<br />

* Assuming 60% Al in dross and LME @ $2000/tonne


Cast House Melt Loss


Note 1. Taken from a study <strong>of</strong> Australasian smelter cast houses by Clarke


Scrap would be a much larger<br />

contributor in a re-melt furnace<br />

* Assumes a typical casting furnace in smelter cast house – ‘non re-melt’


• Implementing technology and processes to<br />

minimise melt loss and effectively deal with<br />

DROSS can move you towards industry<br />

BEST PRACTICE...<br />

• Best Practice – Less than 0.6% melt loss*<br />

* Siphoning, 99.9% Al (no alloying), no scrap additions - type <strong>of</strong> operation


• Liquid metal addition (from pot lines)<br />

• Scrap charging g and types <strong>of</strong> scrap addition<br />

• Burner settings and control<br />

• Alloy additions<br />

• Flux additions<br />

• Stirring techniques<br />

• Skimming practice<br />

• Furnace bath temperature control


• Pouring and cascading<br />

develops Al2O3<br />

• Siphoning Sp can reduce<br />

melt loss by > 70%<br />

... A Good Practice


• Most melt loss from<br />

scrap is developed<br />

when exposed to<br />

burners<br />

• Minimise door open<br />

time<br />

• Method <strong>of</strong> filling


Melt Loss - Scrap Type and Quality


Melt Loss - Light Gauge<br />

• Need to submerge/melt<br />

quickly<br />

• Keep away from the<br />

burners<br />

• Use vortex type<br />

charging systems if<br />

possible for light gauge g<br />

scraps<br />

....A Good Practice


• Several melt loss<br />

contributors:-<br />

• O2 mix too rich<br />

• Direct impingement i on the surface/scrap<br />

• Overheating/wicking<br />

<strong>of</strong> the Al


• How is the alloy<br />

added ?<br />

• Need to minimise<br />

i i<br />

door open time


• Skim at the right time<br />

• Minimise Al removal in the<br />

dross<br />

• Ensure consistency<br />

• Minimise i i door open time<br />

• Also minimise wall, sill<br />

damage etc.<br />

• Robotic/Automatic<br />

skimming<br />

.....A Good Practice


Managing g Bath Surface<br />

Temperature


782°C<br />

<strong>The</strong> Temperature <strong>of</strong> the metal is the single most controllable factor that<br />

determines dross generation in a furnace.


Flue Losses<br />

Heat Repelled by Bath:<br />

• Higher Flue Losses<br />

• Higher Refractory Temp.<br />

Total Heat<br />

Supplied<br />

Wall Losses<br />

Radiation<br />

Q_rad_wall<br />

Q_rad_gas<br />

Q_rad_reflected<br />

To Bath<br />

Conduction + convection


Bath Heat Transfer – <strong>The</strong>rmal resistance<br />

<strong>The</strong>rmal Resistance vs Residence Time<br />

<strong>The</strong>rmal Re<br />

sistance [C/W W]<br />

20<br />

16<br />

12<br />

8<br />

4<br />

Increase Bath<br />

Circulation<br />

0<br />

0 5 10 15 20 25 30 35<br />

Residence Time


• <strong>The</strong>re are many ways to circulate a furnace:-<br />

• Skimming tool<br />

• Porous plugs<br />

• Mechanical pumps<br />

• Electro-magnetic pumps and stirrers<br />

• Permanent Magnet Pumps<br />

Awareness has grown exponentially in the past decade !<br />

<strong>The</strong>y all have different +ve’s and –ve’s


EM Pumps and Stirrers - Market Growth<br />

600<br />

500<br />

EM Side Stirrer - Air<br />

400<br />

PM Pumps<br />

No. <strong>of</strong> units<br />

300<br />

200<br />

100<br />

EM Bottom Stirrer - Air<br />

EM Stirrer (China)<br />

EM Stirrer - Channel<br />

Port Type Stirrer<br />

EM Bottom Stirrer -<br />

Water<br />

EMP System<br />

0<br />

pre 1996 1999 2001 2004 2008<br />

Years


• Non contact<br />

• Ability to move the dross to<br />

assist skimming<br />

• Can switch it on/<strong>of</strong>f as<br />

required during the cycle


• Easy to retr<strong>of</strong>it if there is no<br />

basement<br />

• Similar results to the bottom<br />

• Similar results to the bottom<br />

mounted stirrer


Working through 700mm<br />

Refractory and steel !<br />

HULAMIN, South Africa: 5182 Alloy – 4.5% Mg alloying


• With scissor lift and<br />

electrically driven<br />

trolley serving 2<br />

furnaces with one<br />

bottom mounted EM<br />

stirrer<br />

• Start up May 2011<br />

HYDRO Ardal, Norway: Al Si13 Alloys – 13% Si alloying


Melting Energy Cons. (kWh/T sol .chg)<br />

1000<br />

950<br />

900<br />

850<br />

800<br />

Stirrer<br />

No<br />

750 Yes<br />

700<br />

650<br />

600<br />

550<br />

0 1/6 2/6 3/6 4/6 5/6 1<br />

16% Reduction in energy consumption with EM Stirring


Melting Rate (T solid charge)<br />

17<br />

16<br />

15<br />

14<br />

13<br />

12<br />

Stirrer<br />

No<br />

Yes<br />

11<br />

10<br />

9<br />

0 1/6 2/6 3/6 4/6 5/6 1<br />

20% Increase in melt rate with EM Stirring


Dealing with Cast House<br />

<strong>Dross</strong>


• Maximise in-house metal recovery<br />

• Maximise content <strong>of</strong> aluminium<br />

• Maximise size <strong>of</strong> aluminum particles


Two extremes !!


Advantages<br />

• Improvement on doing nothing!<br />

• Very low tech. No equipment required<br />

Disadvantages<br />

• A long way from potential recoveries<br />

• Dusty & Hazardous to environment<br />

• Hazardous to plant personnel<br />

• Relies on operators<br />

O ll R i<br />

Overall Recoveries<br />

• 20 – 30 %


Latest Technology<br />

Advantages<br />

• Provides good in-house drain (10 – 30%)<br />

• Agglomerates the drops <strong>of</strong> aluminum<br />

• Cools quickly<br />

• Supports logistics <strong>of</strong> skimming many<br />

furnaces<br />

Disadvantages<br />

• One press is not set-up to handle large<br />

fluctuations in dross generation, need size<br />

number to requirements<br />

Recoveries<br />

• 60 – 70 % range


• Today’s dross press<br />

bears little resemblance<br />

to early systems<br />

• Amalgamation <strong>of</strong> the<br />

two leading dross press<br />

technologies in the<br />

world<br />

• Provides the highest<br />

metal recoveries


• <strong>Dross</strong> is skimmed into pans<br />

that are designed to cool<br />

dross and maximize metal<br />

drain<br />

• Placed into dross press where<br />

the free metal is squeezed<br />

into pan below<br />

• Press head remains in the<br />

dross to further cool the<br />

dross to desired temperature


Metallic Size in<br />

Uncompressed<br />

<strong>Dross</strong><br />

Metallic Size in<br />

Pressed <strong>Dross</strong><br />

• Consolidates the fine<br />

particles remaining<br />

within the dross<br />

• Migrate to the outside<br />

surface <strong>of</strong> the dross in<br />

plates<br />

• <strong>The</strong>se plates or skin<br />

encapsulates the dross<br />

preventing further<br />

oxidation <strong>of</strong> dust and<br />

fuming<br />

• Significantly ifi improves<br />

recovery by 5 – 10%


At 1300°C


Immediately after pressing<br />

Prior to pressing at 1300°C<br />

After 5 hours


After 15 minutes<br />

After 3 hours


• Rapid sealing <strong>of</strong> the slag to stop funing<br />

• Capturing all aluminium units to minimise any<br />

further Al losses through continued burning<br />

• Cooled skull (surface to 400°C) after 3 hours<br />

• Easily breaks up due to oxide/Al interfaces in<br />

skull<br />

• Massive reduction in slag cooling time<br />

• Stops fuming and dburning


• Produces approximately 200T/month <strong>of</strong> dross<br />

• Installed a relatively small dross press<br />

• <strong>Dross</strong> pan capacity <strong>of</strong> 250 kg<br />

• Before Press installation:<br />

• In-house recovery: 3%<br />

• Secondary recovery: 35%<br />

• After Installation:<br />

• In-house recovery: 8 - 12%<br />

• Secondary recovery: 40 – 42%


Without <strong>ALTEK</strong> Press:<br />

• In-house Recovery = 3%<br />

• 6 T / Month<br />

• $15,000 / Month $184,750<br />

• Secondary Recovery = 35% ($51,216)<br />

• 67.9 T / Month<br />

$133,534<br />

• $169,750 / Month<br />

With <strong>ALTEK</strong> Press:<br />

• In-house Recovery = 8 - 12%<br />

• 20T/Month<br />

• $50,000 / Month<br />

$234,500<br />

($47,520)<br />

• Secondary Recovery = 40 - 42%<br />

$186,980<br />

• 73.8 T / Month<br />

• $184,500 / Month<br />

$53,446 /month<br />

$641,352<br />

Annually<br />

10%<br />

Improvement


• Production <strong>of</strong> 500 T/month <strong>of</strong> dross<br />

• Customer melts a variety <strong>of</strong> aluminum scrap<br />

• Installed a medium sized dross press<br />

• <strong>Dross</strong> pan capacity <strong>of</strong> 700 Kg<br />

• Before Press installation:<br />

• In-house recovery: 0%<br />

• Secondary recovery: 25%<br />

• After Installation:<br />

• In-house recovery: 5 - 10%<br />

• Secondary recovery: 30 – 37%


Without <strong>ALTEK</strong> Press:<br />

• In-house Recovery = 0%<br />

• 0 T / Month<br />

• $0 / Month $312,500<br />

• Secondary Recovery = 25% (132,000)<br />

• 125 T / Month<br />

$180,500<br />

• $312,500 / Month<br />

With <strong>ALTEK</strong> Press:<br />

• In-house Recovery = 5 - 10%<br />

• 37.5T/Month<br />

• $93,750 / Month<br />

$481,000<br />

($122,100)<br />

• Secondary Recovery = 30 - 37%<br />

$358,900<br />

• 154.9T / Month<br />

• $387,250 / Month<br />

$178,400 /month<br />

$2,140,800<br />

Annually<br />

13% Improvement


Skim Efficiently<br />

Cool immediately to maximise recovery<br />

Process the <strong>Dross</strong> Skull efficiently<br />

i To maximise<br />

Aluminium return<br />

Use a Tilt Type<br />

Rotary Furnace


After the Cast House<br />

....<br />

<strong>The</strong> Secondary <strong>Dross</strong><br />

Processor


<strong>Dross</strong> Skulls need to<br />

be recycled in a Tilt<br />

Type Rotary Furnace<br />

<strong>ALTEK</strong> 16 MT Tilt<br />

Type Rotary Furnace


Materials handling and<br />

segregation<br />

Quality <strong>of</strong> input<br />

Oxide/Al content<br />

Flux considerations<br />

- Salt process<br />

- No salt process<br />

All affect the Aluminium recovery from the dross


Handling the residues/<br />

by-products<br />

Corporate responsibility<br />

<strong>of</strong> the dross generator<br />

- No landfill<br />

- Markets for by yproducts<br />

- Cement<br />

- Steel<br />

- Construction<br />

- Flux


• Look at the whole process <strong>of</strong> melt loss to dross<br />

generation to dross recovery<br />

• <strong>The</strong>re is a breadth <strong>of</strong> products to support a correct focus<br />

on Total <strong>Dross</strong> <strong>Management</strong> at each step..<br />

• It starts in the furnace but every step is important..<br />

• Its is very important to understanding the whole process<br />

• <strong>The</strong>re are HUGE financial and environmental<br />

consequences from ignoring effective dross management


• 430 <strong>Dross</strong> Presses<br />

• 45+ Tilt Type Rotary Furnaces<br />

• 48 Electromagnetic Stirrers<br />

• 1000+ dross pans and castings


REMEMBER – <strong>The</strong>re is BIG value in your DROSS !!

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