“Improving Productivity and Quality In the Hot Dip …...“Improving Productivity and Quality In...
Transcript of “Improving Productivity and Quality In the Hot Dip …...“Improving Productivity and Quality In...
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“Improving Productivity and Quality In the Hot Dip Galvanizing Process”
By Mike Ainsley
International Zinc Association (IZA)
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TOPICS Brief introduction to zinc production
Galvanizing Process
Galvanizing bath composition
Galvanizing residues ( dross and ash) Zinc ingots
Steel factors Galvanized product quality problems
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Zinc production
Most Zn is obtained from mining operations. The mines produce zinc “ore” which is around 5 -15% Zn content.
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Zinc ore is then processed to a “concentrate” of about 50% Zn content
Zinc production
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Metal extraction process
Zinc
concentrate
Zinc ingot (99.995%)
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The final process is Quality Control. Zinc samples are routinely sent to the laboratory for chemical analysis
Zinc production
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TOPICS Brief introduction to zinc production
Galvanizing process Galvanizing bath composition
Galvanizing residues ( dross and ash) Zinc ingots
Steel factors Galvanized product quality problems
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Galvanizing Process
Topics 1. Steel pre- treatment 2. Zinc bath and operating factors 3. Cooling 4. Passivation
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Pre-treatment
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Degreasing Pre-treatment
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Commonly used degreaser formulations
All solutions must be heated (approximately 80°C) for optimum performance.
COMMENTS
COMPOSITION
* Cheap
* Moderate cleaning ability
CAUSTIC SODA SOLUTION
Sodium Hydroxide - NaOH (60-100 g/L)
Use at 80oC
* Moderately cheap
* Good cleaning ability
CAUSTIC SODA (75 g/L)
Sodium Metasilicate (200 g/L)
Wetting Agent (5 g/L)
Use at 80oC
* More expensive
* Very Good cleaning ability
CAUSTIC SODA (60 g/L)
Sodium Phosphate (35 g/L)
Wetting Agent (5 g/L)
Use at 80oC
Sodium hydroxide ( caustic soda – NaOH) is still the most widely used in Asia
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Pre-treatment Degreasing
Caustic Soda solutions Must be heated to approx 80oC for best efficiency Steam heating is used but modern plants now use gas/oil fired immersion pipes. The technology is simple and maintenance is reduced
Acid degreasing solutions New development The main benefit is some cost saving as no water rinsing is required before the acid pickle and no heating is required
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Purpose is to remove residual degreasing solution Is it necessary? Yes Why? Because degreasing solution will consume acid if it is not removed Rinsing also ensures no grease/oil is carried across into the acid tank
Pre-treatment
Water rinsing after degreasing
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Single tank rinse is satisfactory but two rinse tanks are preferable
If the water is static (stationary) then best rinsing requires the steel to be moved up and down.
Pre-treatment Water rinsing after degreasing
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If using a single rinse tank it is better to use recirculating water and to introduce a “weir” to make the water flow more evenly across the surface of the tank
Outlet Weir
SIDE VIEW
Outlet
Inlet
Pre-treatment Water rinsing after degreasing
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A further improvement is to introduce a grease/oil trap
Water
Outlet
Weir
Baffle Floating
Oil/Grease
Layer
Pre-treatment
Water rinsing after degreasing
Water flow
Water flow
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Purpose To remove rust and oxidized scale without causing
significant attack of the steel surface
Acid types: Hydrochloric acid (HCl). Most galvanizers in Asia
use HCl
Sulphuric acid (H2SO4)
Pre-treatment
Acid Pickling
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Hydrochloric acid pickling
Since pickling is the slowest stage of the galvanizing process, the acid pickling conditions should be optimized. Optimum conditions are: 1. Acid concentration should be kept in the range 10% - 15% 2. Acid should be agitated (stirred). This accelerates pickling
because it keeps fresh acid at the surface of the steel. Most effective agitation is by “sparging” with compressed air through a
rubber hose. If sparging is not done, then the steel should be moved up and down sometimes
Pre-treatment
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Hydrochloric acid pickling
Since pickling is the slowest stage of the galvanizing process, the acid pickling conditions should be optimized
3. The iron ( Fe) content in the acid tank should not exceed 120 grams per litre The higher the Fe content the slower is the pickling rate At an Fe content of 120gm/litre the acid cannot absorb any more Fe. Therefore pickling stops
Max Fe solubility
= 120 g/L
50 0 100 150 200 250
Iron Concentration (g/L)
Pre-treatment
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0
5
Time
Acid
Co
ncen
trati
on
(%)
Iro
n C
on
ten
t g
/L)
10
15
Fe
Content
120 g/L
No further
acid additions
Fresh Acid
Addition
Acid
Content
Optimum acid tank control
Pre-treatment Hydrochloric acid pickling
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Optimum HCl acid tank control
0
5
Time
Acid
Co
ncen
trati
on
(%)
10
15
Fe
Content
Fresh Acid
Addition
Acid
Content
Acid used
for zinc stripping
Never do zinc stripping in a working pickling tank because the zinc contamination in the acid will significantly slow the acid’s pickling speed
Pre-treatment
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Additives to acid tanks
1. Inhibitors. These chemicals ensure the acid only removes the rust or oxide scale on the steel surface. The acid is prevented from attacking the steel surface. 2. Fume control chemicals: These form a layer of “froth” on the surface of the acid which prevents acid fume escape
Chemical suppliers to the galvanizing industry and steel manufacturing industry can supply these additives.
Pre-treatment Hydrochloric acid pickling
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Single tank rinse is satisfactory but two rinse tanks are preferable. Good rinsing is important to reduce acid (+Fe)
contamination of the flux
If the water is static (stationary) then best rinsing requires the steel to be moved up and down.
Pre-treatment
Water rinsing after acid pickling
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Sometimes called preflux
Purpose To assist the molten zinc to react with the steel surface to form the galvanized coating.
Flux composition Zinc ammonium chloride (ZnCl2.3NH4Cl) in water - - can be purchased already made - - or can be made by mixing zinc chloride (ZnCl2) and - ammonium chloride (NH4Cl) according to the ratio -
ZnCl2 : NH4Cl = 1 : 1.13 by weight
Fluxing Pre-treatment
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Optimum flux conditions
1. Flux concentration
200-300 g/L. ( grams/litre)
Below 200 g/L there is a risk of “black-spots” on the galvanized steel where the coating has not formed. Controlling the flux concentration can be done using - monthly chemical analysis by a laboratory
- simple Specific Gravity (SG) measurement then referring to the SG vs concentration graph.
Pre-treatment
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25 SG measured when flux is cool
ZAC = Zinc Ammonium Chloride flux solution
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Optimum flux conditions
2. Flux temperature
Flux should be hot (60 – 80oC) to assist later drying.
Galvanizers now using gas/oil fired immersion tube burners. More cost effective than steam heating
Pre-treatment
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Optimum flux conditions
3. Control the iron (Fe) contamination
Flux
Acid + Fe
Carryover
Fe carryover
to zinc bath
Pre-treatment
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Optimum flux conditions
3. Control the Iron (Fe) concentration
Understanding the type of iron contamination in the flux
Fe is present in the flux as:
1. Soluble Fe ( cannot see it). This Fe contaminates the flux layer and therefore is carried into the molten zinc where it forms dross
2. Insoluble Fe. This is the brown coloured particles in the flux. This Fe settles to the bottom as a “mud”. It does not significantly contaminate the flux layer on the steel
Pre-treatment
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Control the soluble Fe concentration
Should be <5 g/L ( maximum 10 g/L )
Achieve by:
Good acid rinsing practice to minimise iron carryover. Regular flux chemical treatment using small quantities of hydrogen peroxide (H2O2). This instantly converts soluble Fe to insoluble Fe Correct pH control.
Optimum flux conditions Pre-treatment
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Control the insoluble iron concentration
This is not as important as controlling the soluble Fe content but it is still good practice
Achieve by:
Removing the bottom “mud” when it becomes too thick Filter the flux
Optimum flux conditions Pre-treatment
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Flux Filter Equipment
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4. Control the pH value (pH = acidity content)
Requires pH = 4.0 - 5.0 To increase pH above 4.0 add ammonia solution NH4OH ( also called ammonium hydroxide) To reduce pH below 5.0 add hydrochloric acid
Optimum flux conditions
If pH is low this causes more soluble Fe If pH is too high ( > 5.5) the zinc chloride in the flux can decompose and become non-effective
Pre-treatment
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Fe converts from insoluble Fe to soluble Fe as the pH becomes lower
pH 4.0 pH 5.0 Soluble Insoluble Fe Fe pH should not exceed 5.5 as this can cause problem with decomposition of zinc chloride
Optimum flux conditions Pre-treatment
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5. Additives to flux
Liquid “ detergent” ( soap). This results in less flux solution on the steel as it comes out of the flux tank. Drying is therefore quicker and less splashing/ bubbling during dipping in molten zinc. This reduces ash formation
Hang 3 or 4 pieces of zinc ingot from the side of the flux tank. This will help neutralize acid carryover. The zinc slowly reacts with the acid to produce zinc chloride which is required in flux
Optimum flux conditions Pre-treatment
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Steel should be dried as much as possible before entering the bath
Why? for safety ( less zinc splashing) reduces as formation on the zinc bath surface enables faster dipping speeds which saves time and for some items reduces the risk of steel distortion
Pre-treatment Drying
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Zinc bath and operating
factors
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Steel
Molten
Zinc
Zn migration
into the steel
surface
Steel
Zinc – Iron Alloy Layer
Molten Zinc
Zinc “diffuses” into the steel surface and combines with the iron component. This results in the formation of a Zinc – Iron alloy
layer
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How does the coating form ?
Zinc bath
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When the steel reaches 450oC the formation of the Zn-Fe alloy layer
occurs very rapidly (under 1 minute) The reaction then slows
down and dipping for longer will not further increase the alloy layer thickness Dipping Time
Co
ati
ng
Th
ickn
ess
Dipping time in zinc
Boiling slows down
Zinc bath
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As the steel emerges from the molten metal, a layer of pure zinc metal solidifies on top of the zinc - iron alloy layer
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STEEL
Zinc- iron
alloy
Zinc metal HDG
COATING
How does the coating form ? Zinc bath
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Cross-section through an actual galvanized coating at high magnification
Steel base
Zn-Fe
alloy
layer
Zn layer
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How does the coating form ? Zinc bath
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Zinc bath
Operational factors
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Zinc bath
1. Zinc temperature 445 – 455oC is satisfactory. 448 – 452oC
usually considered best << 445oC risk of non-smooth coatings because of low zinc fluidity >> 460oC risk of short kettle life due rapid attack by molten zinc
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Zinc bath
2. Zinc temperature stability
Temperature should be as stable as possible
+/- 2oC is acceptable more than +/- 2oC causes extra dross
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1 metre/minute is regarded as the best speed and 1.5 metres/minute as the maximum speed
Slow speed allows excess molten zinc to drain back
into the bath. If speed is too fast, the zinc layer in the coating is too thick (wasting zinc)
Dual speed crane is best. High speed for steel entry, low speed for steel withdraw
3. Speed of withdrawal from bath
Zinc bath
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Zinc Layer
Zinc-Iron Alloy Layer
Steel Base
Slow
speed
Zinc Layer
Zinc-Iron Alloy Layer
Steel Base
Fast
speed
Speed of withdrawal from bath
Zinc bath
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4. Skimming technique Zinc bath
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Skimming technique
Zinc bath
Some companies consider the skimmer to be the most important person because he controls the appearance of the galvanized steel !!!
Skimming should be done just in front of the steel as it emerges from the zinc ( instead of skimming the whole bath surface before the steel emerges)
Skimming operation should be slow and gradual. Avoid
“paddling” with the skimming tool as this creates more ash and produces ash-marks occur on the coating
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Cooling
Operational factors
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Cooling
Cooling
Water cooling ( quenching) is the normal method. Water cooling should NOT be used if there is a risk it will cause distortion of the steel. In this situation the steel should be allowed to cool slowly to 200 - 250oC before water cooling
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Passivation
Operational factors
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Passivation
Most galvanizers add a “passivation” chemical to the cooling water.
This is to prevent or minimize white rusting of the galvanized coating during storage
Passivator chemicals - Chromate (traditional method) - Soluble polymer (new method)
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Passivation
Chromate Passivation Normally 0.1% - 0.15% sodium dichromate content. Higher content can cause green- yellow colour on the coating, especially on thick steel items Keep chromate water temperature preferably below
70oC. This will prevent excessive green-yellow colour on the coating. An external heat-exchanger
may be required to control temperature
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Chromate passivation If using one cooling tank, the chromate water will become contaminated with chloride ( from ash/flux carryover on the steel). Chloride contamination in the water destroys chromate
passivation. To avoid this problem, many galvanizers use two water
cooling tanks. 1st tank: Water only. This absorbs the chloride and prevents the chromate tank from overheating.
2nd tank: Water + chromate.
Water from 1st tank can be used for the acid pickling tanks
Passivation
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Passivation using water soluble polymer Chromate is under environmental pressure to be
banned due to its very toxic nature
Galvanizers have now started to change to (non toxic) water soluble polymers . The polymer film is invisible
2 tank process MUST be used. 1st tank is water. 2nd tank is water + soluble polymer. This is because the steel must be partially cooled before entering the polymer tank.
Passivation
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TOPICS Brief introduction to zinc production
Galvanizing process Galvanizing bath composition
Galvanizing residues ( dross and ash) Zinc ingots
Steel factors Galvanized product quality problems
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Zinc bath
Galvanizing bath composition
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Zinc bath
Bath additives are:- Lead (Pb)
Aluminium (Al)
Nickel (Ni)
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Zinc bath
Lead (Pb) Most galvanizers operate with a 100mm molten Pb layer on the bottom of the bath. This has two purposes: Helps in drossing operations because the dross floats on the Pb, making it easier to lift out Gives protection to the bath ( kettle) bottom corner welds. Zinc in contact with these welds is considered to be a risk due to rapid zinc attack. True or false ??
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Zinc bath
Lead (Pb)
Some Pb from the bottom layer is absorbed into the molten zinc. The Pb content in the zinc will usually stabilize around 0.6 - 0.8% Pb content Pb is progressively “lost” from the bottom layer and must be replaced from time to time. This loss is due to
a) absorption into the molten zinc b) unavoidable removal of some Pb during the drossing operation
The thickness of the Pb layer must be regularly checked. An L shape metal bar can be used to do this
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Zinc bath
Pb Dross
Zinc
Measuring Pb layer thickness
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Zinc bath Lead (Pb)
“Pb - free” galvanizing
Some baths operate Pb-free for environmental reasons. Certain project specifications may require Pb-free coatings, or export customers may request it
Changing to Pb - free galvanizing means:
Pumping out the bath and Pb layer and replacing with pure zinc. Just pumping out the Pb layer will not result in Pb-free due to the Pb already absorbed into the zinc
Modifying the furnace chamber so that the lower 150mm of the bath is insulated. This prevents the dross layer from becoming “ hardened” and difficult to remove 61
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Zinc bath
Aluminium(Al)
Al is added to make the coating “shine”
Optimum Al content is 0.002 – 0.005%
Al content > 0.01% can cause “black spots” on the coating where the coating has not formed. This is because Al reacts with flux on the steel surface and reduces flux effectiveness Simple method to establish if Al content is satisfactory (discussed later)
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Zinc bath Aluminium(Al) Method of adding aluminium to the bath 1. Adding pieces of pure Al or scrap Al (wire) Advantage: cheap to purchase Disadvantage: Poor control of Al content in the bath, because :- a) Aluminium does not melt into the zinc. The molten zinc only “ absorbs” the Al very slowly. It is not possible to control this speed of this. b) The Al floats on the bath surface. Absorption of Al by the zinc is confined to the bath surface. Most of
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Zinc bath
Method of adding aluminium to the bath
2. Using Zn-Al pre-alloy ( eg, Padaeng DA3 alloy).
Advantage: - Does not float and it melts rapidly. The Al is therefore uniformly distributed within the bath and this occurs rapidly.
- Easy to control the Al content in the bath. For example, one ingot of DA3 alloy with each one tonne of zinc added will achieve the desired Al% in the bath ( after allowing for Al consumption during galvanizing). 64
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Zinc bath
Zn-Al pre-alloy (eg, Padaeng DA3 alloy)
Advantage: More economic to use than pure Al pieces because …. 100% of the Al in DA3 alloy is absorbed into the zinc bath. purchasing pure Al may appear cheaper BUT most of the aluminium is “lost” to oxidation at the bath surface. 65
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Pure Al
Zn-Al alloy
Comparing Al dispersion efficiency
Molten Zinc
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Zinc bath
Nickel (Ni)
Nickel is increasingly being used by galvanizers in Europe, North America and Asia
An advantage of using nickel is improved molten
zinc fluidity. This contributes to
reduced zinc consumption of 5 -15% more smoother coatings
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Zinc bath Nickel (Ni)
Another advantage of using nickel is to modify the galvanizing reaction between zinc and steel
resulting in a coating structure that: Is more uniform in coating appearance ( less grey
colour). This applies especially to coatings on thicker steel sections and steels with higher silicon and phosphorous content
Gives less problems with coating cracking or loss
of adhesion (flaking) on thicker steels or steels with higher silicon or phosphorous content
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Zinc bath Nickel (Ni)
Optimum Ni content in the bath is 0.05 - 0.06% Ni is added to the bath using Zn-Ni pre-alloys. Padaeng produces two pre-alloys as follows: ZnNi0.15 alloy (0.15%Ni content) Using only this alloy for bath additions will result in an 0.05 -0.06% stabilized Ni content in the bath
ZnNi0.5 alloy (0.5%Ni content) Used in the addition ratio of 1 tonne alloy with 2 tonnes pure zinc to achieve the stabilized 0.05 – 0.06% Ni content in the bath. 69
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TOPICS Brief introduction to zinc production
Galvanizing process Galvanizing bath composition
Galvanizing residues ( dross and ash) Zinc ingots
Steel factors Galvanized product quality problems 70
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Galvanizing Residues
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Bottom dross
Top Ash
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Steel “kettle”
Top ash layer
Bottom dross layer (Zn-Fe compound)
Molten Zn
Pb layer
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Galvanizers “bottom dross”
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It forms as a result of a chemical reaction between molten Zn and Fe impurity
During galvanizing, some Fe is constantly
transferring into the molten Zn Molten zinc can only dissolve a small amount of Fe
(about 0.04% maximum). As more Fe transfers into the molten zinc, the “surplus” Fe combines with zinc to form very tiny dross particles. The reaction is
Fe + 13 Zn Fe Zn13
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Dross
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Close-up view of dross
Needle - like dross crystals can be seen
Dross
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The dross particles are slightly denser than molten zinc and so gradually settle to the bottom of the bath as a layer
In this bottom layer the dross particles mix with
molten zinc. Dross particles form 50% of the layer and molten zinc forms 50%
Therefore since dross particles have the ratio Fe:Zn = 1:13 , then in the dross layer the ratio is Fe : Zn = 1: 26 The composition of the dross layer is therefore about 4%Fe + 96% Zn
Dross
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Dross
Dross formation is therefore extremely sensitive to the amount of Fe dissolving into the molten zinc. One part by weight of iron combines with nearly 26 times its weight of zinc to form dross Since dross is a waste product it is therefore extremely costly in terms of zinc loss
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Cross section of bottom dross layer viewed in microscope
Dross
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Dross formation is approx 7 -11 % of zinc consumption
Dross has a very high zinc content but it is not possible for galvanizers to recycle their dross to recover some of the zinc
Dross is purchased by recyclers. Dross sells at 65-75% of zinc price
Recycled dross is used to make pure zinc oxide
Dross
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How can dross be reduced ? Use pure zinc which has a very low Fe content ( SHG 99.995% Zn)
90% of all dross is produced from Fe absorption mostly
from the steel products being galvanized. Lower zinc temperatures mean less absorption of Fe from steel.
Maintain bath temperature at 445 - 455oC. Do not exceed 465oC
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Dross
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Zinc bath
How can dross be reduced ? Temperature should be as stable as possible
+/- 2oC is acceptable more than +/- 2oC causes extra dross
Zinc temperature
Maximum Fe absorption by molten zinc
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How can dross be reduced ?
Maintain a very low Fe content in the flux since Fe
from the flux is carried across into the zinc bath. Upto 10% extra dross can be produced due to Fe in the flux
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Dross
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Dross needs to be removed regularly.
Why is it important to regularly remove dross?
Answer: Unless regularly removed the dross layer will thicken. Since dross is a poor conductor of heat a “hot-spot” can develop at the kettle wall next to the dross. This hot spot can result in a hole in the kettle wall.
Drossing procedure Dross
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Drossing procedure Maintain Pb layer at about 100mm deep . Depth of Pb layer can easily
be measured using an L shape steel bar Best drossing temperature is 450oC - 455oC. If < 445oC the molten
zinc becomes less “fluid” so more molten zinc remains in the dross as it comes out of the bath. This is wasted zinc
If using a dross shovel do not always remove the dross using the same
direction. This prevents dross accumulating at one end of the kettle Drossing should be done at least every 2 weeks. Do not allow dross to
accumulate for more than 4 weeks as this is dangerous for the kettle
Dross
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Where does bottom dross go after it leaves the galvanizing plant ? Answer It is used by recyclers who extract the zinc Due to the high % of zinc content in dross ( approx 96%Zn) and
the fact that dross sells at approx 75% of the market price of SHG zinc, it is economically attractive to extract zinc from dross
Dross
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How is the zinc extracted from the dross ? Answer The only practical method to “extract” all the Zn is
to melt the dross at 1000oC
The Zn is then released as a Zn vapour. The vapour burns in contact with air to produce very pure zinc oxide which is a white powder
Dross
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Furnace using dross to produce Zinc oxide
Dross
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Zinc oxide powder
Some zinc oxide applications
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Zinc ash
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What is ash?
Answer Ash forms due to natural oxidation of zinc in contact with air due to the reaction
Zinc + oxygen = Zinc oxide (impure)
Ash also contains about 10 - 25% of zinc lumps and some iron oxide, aluminium oxide and flux residues.
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Ash (on the surface of the zinc bath)
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Ash formation is normally approx 15 - 20% of Zn consumption.
Total Zn content in ash is about 70 - 80%. It is
therefore important to reduce ash as much as possible during galvanizing
Ash is purchased by recyclers. Ash sells for 35% - 45%
of zinc price.
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Ash (on the surface of the zinc bath)
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Dry the steel as best as posible to avoid turbulence or splashing during dipping of the steel item into the molten Zn. Avoid using zinc ingots that are wet or damp. It is also desirable to avoid white rusted zinc ingots, therefore zinc should be stored under-roof
Skimming tools should be correctly used. Do not “paddle” when using the tool. Slow, steady motion is best.
Bath aluminium additions should be maintained at the correct level. Aluminium slows down the rate of oxidation of the bath surface.
How to reduce ash formation Ash
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Caution: Ash should not be allowed to “build-up” on the kettle wall above the zinc surface. This build-up must be removed every few days This can cause a “hot-spot” on the kettle wall beneath the ash and rapid localized erosion of the kettle wall ( see picture)
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Can some of the zinc in ash be recovered at the galvanizing plant? Answer: Yes. Various methods are used which give different recoveries
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Ash (on the surface of the zinc bath)
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Ash can be treated by galvanizers to recover some zinc
Treatment method 1 Accumulate the ash at bath end where it is “chopped”
Zinc recovery is very low (5 -10% recovery)
Ash
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Treatment method 2: The box method
An open steel box is located in the bath corner. The box is open at the top and bottom and the lower 1/3rd of the box is in the molten zinc The box is then filled with fresh, hot ash
Some flux powder is then added and the ash is vigorously stirred with a steel bar. This causes the zinc lumps to melt and - re-enter the molten zinc bath
Zinc recovery is 30 - 40%
Ash
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Treatment method 3: The rotating drum method
This method uses a sloping cylindrical drum which slowly rotates The lower part of the drum is perforated with small holes The inner wall of the drum has “blades” attached Hot fresh ash is fed into the upper part
As the ash moves down, the blades crush the ash lumps and separate out the zinc lumps. The lumps exit from the bottom of the drum Ash powder passes through the small holes.
Zinc recovery is 50 -70%
Ash
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What happens to ash sold to recyclers?
Ash is crushed and screened to remove the zinc lumps. These are melted and cast as “secondary” zinc ingot which is sold to galvanizers and zinc oxide producers
The remainder of the ash is a powder which is …… - used to make zinc chemicals (eg, zinc chloride) - added to fertilizers to improve crop growth.
Ash
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Low zinc
content soil
Zinc added
to soil
Example of better rice plant
growth by using zinc 99
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TOPICS Brief introduction to zinc production
Galvanizing process Galvanizing bath composition
Galvanizing residues ( dross and ash) Zinc ingots
Steel factors Galvanized product quality problems 100
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CHEMICAL COMPOSITION (%) PADAENG SHG
Zinc 99.995 min.
Lead 0.003 max.
Cadmium 0.003 max.
Iron 0.002 max.
Copper 0.001 max.
Aluminium 0.001 max.
Tin 0.001 max.
Zinc ingot Zinc composition should conform to the international zinc standard EN ( ISO) 1179
Example is Padaeng Zinc (Special High Grade – SHG)
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Zinc ingot Zinc ingot shape
Zinc slab. 25kgs . 40 slabs per bundle
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TOPICS Brief introduction to zinc production
Galvanizing process Galvanizing bath composition
Galvanizing residues ( dross and ash) Zinc ingots
Steel factors Galvanized product quality problems 103
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Steel
Steel factors
surface condition composition
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Steel
Rougher
steel surface
Smoother
steel
surface Galvanized
coating thickness
Surface condition
Sand blasting the steel surface is a method used by galvanizers to achieve extra thick coatings
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Steel Steel composition
Coating
thickness
0 0.3 0.2 0.1
Si + 2.5 x P (%)
Silicon and Phosphorous contents have a large effect
Shiny
Partly Shiny
Grey
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Steel Silicon and phosphorous
modify the coating structure
Coating is all Zn-Fe
alloy layer
Normal coating with
top pure Zn layer
present
Zn layer
Zn – Fe alloy layer
Steel
Zn – Fe alloy layer
Steel
Si + 2.5 x P ( < 0.09%) Si + 2.5 x P (0.09% - 0.2%)
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TOPICS Brief introduction to zinc production
Galvanizing process Galvanizing bath composition
Galvanizing residues ( dross and ash) Zinc ingots
Steel factors Galvanized product quality problems
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Galvanized product quality problems
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Bare areas (black spots) Non-smooth coatings.
Zinc flow-marks. Ash pickup. Dross pimples.
Grey coatings.
Flaking (peeling) coatings. White rust.
Topics
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Bare areas Surveys show 85+% of galvanizing quality
problems relate to bare areas.
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Usual causes of bare areas are: Poor steel cleaning (degreasing or acid pickling).
Poor flux condition.
High aluminium content in the bath.
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Recommended normal aluminium content in the bath ( and near the surface) is 0.002 – 0.005%. Bare areas often occur when the aluminium content is > 0.01%
Bare areas (black spots) caused by a high aluminium content in the bath.
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Bare areas (black spots) caused by a high aluminium content in the bath.
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Simple test for high aluminium content
Clean a small area of the bath surface, then throw a small (1cm) lump of flux onto the cleaned area.
BATH SURFACE BATH SURFACE
Flux lump moves across the zinc surface = safe aluminium content
Flux lump remains stationary = too much aluminium content
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Usual reasons causing the problem are:- too much aluminium being added to the bath a non-uniform distribution of aluminium in the
bath (ie., bath surface too high in aluminium content)
Bare areas (black spots) caused by a high aluminium content in the bath.
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Remedy: 1. Add flux powder to the bath surface. This quickly reduces
the aluminium content but does creates a lot of fume 2. Change from adding pure aluminium additions at the bath surface to use of a zinc – aluminium alloy addition (such as Padaeng DA3 alloy added as 1 piece with each tonne zinc added during operations) 3. Aluminium (alloy) additions to the bath should be regular and consistent with each tonne of zinc added to the bath, or at specific set times during operation
Bare areas (black spots) caused by a high aluminium content in the bath.
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Repair of bare areas
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Paint coating thickness should be 30 microns thicker
than the surrounding zinc coating (ISO) and contain
> 65% Zn in the liquid paint or > 92 % in the dry
paint layer ( ASTM)
Apply final top coat of aluminium paint ( sometimes
called silver paint) for a good colour match with the
galvanized coating.
Important: Do not use aluminium paint as a
substitute for zinc-rich paint.
Repair of bare areas ( as specified in ISO and ASTM Standards)
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Non smooth coatings
Problem : Zinc flowmarks
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Cause: Galvanizing temperature too low (which reduces
zinc fluidity)
Problem : Zinc flowmarks
419oC
440oC
450oC
Solidification
temperature
of zinc
21oC
31oC
Change of only 100C in the galvanizing temperature (4400C to 4500C - approx
2%) causes a 33% change in the temperature difference before zinc solidifies
Optimum galvanizing
temperature is 450- 455oC
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Cause: Excess zinc due to withdrawal speed from bath
being too fast. The excess zinc has no time to flow back
Into the bath
Problem : Zinc flowmarks
Recommended practice: Reduce withdrawal speed to 1.0 - 1.5 metres
per minute.
Molten Zinc
FAST
WITHDRAWAL
NORMAL
WITHDRAWAL
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Patches of
zinc oxide
Non smooth coatings
Problem : Ash pick-up on the coating surface
Ash lumps and streaks
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Non smooth coatings Problem : Ash lumps or ash streaks on the coating surface
Remedy:
Careful, slow and steady skimming technique. Do not “paddle” as
this creates waves causing ash streaks
Skim bath surface just in front of the emerging galvanized steel
items.
Proper design of the ‘skimmer’ tool. Use a floating type
skimming tool
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Non smooth coatings
Problem : Dross pimples in the coating
Zinc layer
Steel
Dross particle
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Remedies: Do not allow the bottom dross layer to become very
thick. Remove dross from the bottom of the galvanizing bath regularly.
Keep a Pb layer at the bottom of the galvanizing bath at 50 - 100mm deep. The Pb assists in holding the dross at the bottom.
Non smooth coatings
Problem : Dross pimples in the coating
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Remedies: Keep iron contamination in flux at a low level. This iron
will produce extra dross when the steel enters the zinc bath.
Avoid high aluminium levels in the bath especially at the surface since this can change normal Zn- Fe dross particles into an Al - Zn - Fe dross which float and stick to the coating. Therefore add aluminium using a zinc-aluminium alloy instead of pure (or scrap) aluminium to avoid the problem of excessive bath surface aluminium content
Problem : Dross pimples in the coating
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Cause: High silicon and phosphorous content in the steel composition.
Occurs when %Si + 2.5 X %P > 0.09%
Grey coatings
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Grey coatings
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Grey coatings
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Grey coatings
Zn layer
Zn – Fe alloy layer
Steel
Zn – Fe alloy layer
Steel
Si + 2.5 x P ( < 0.09%) Si + 2.5 x P (0.09% - 0.2%)
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Remedy: 1. If customer rejects the coating, remove the galvanized coating in the acid stripping tank and re-galvanize The 2nd coating is usually “normal”. This is because the first coating removed Si and P from the steel surface 2. The problem is much less observed in baths with nickel additions because nickel slows the growth of the Zn-Fe layer
Grey coatings
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Zn-Fe
alloy layer
thickness
0 0.3 0.2 0.1
Si + 2.5 x P (%)
Nickel addition can reduce grey coating
problem
Shiny (+ Ni)
No Nickel
+ Nickel
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Cause: Thick steel sections being galvanized. These remain very hot immediately after exiting from the bath. The Zn-Fe alloy layer then has time to grow and reach the coating surface before the steel is water cooled
Grey coatings
Thin steel
Thick steel
Probability of grey colour
Low
High
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Grey coatings on thick steel
Thin steel
Thick steel
Probability of grey colour
Low
High
Faster transfer to water cool or Ni in the bath
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Thick and brittle coatings which crack or peel-off
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Thick and brittle coatings which crack or peel-off
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Thick and brittle coatings which crack or peel-off
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Cause: Always due to very high silicon and
phosphorous content in the steel composition.
Occurs when %Si + 2.5 X %P = 0.13 – 0.18% or >> 0.35% High Si + P causes the coating structure to be mostly a thick and brittle Zn-Fe alloy layer which is not strongly bonded to the steel surface
Thick and brittle coatings which crack or peel-off
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Remedy Remove the coating in the acid stripping tank and re-galvanize. The 2nd coating is usually “normal”. This is because the first coating removed Si and P
from the steel surface Nickel additions to the bath reduce the probability of thick and brittle coatings
Thick and brittle coatings which crack or peel-off
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White rust Cause: Corrosion of the galvanized coating surface due to storage in wet (or humid) conditions where there is poor air circulation
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White rust Remedy: Correct storage conditions ( store under roof if
possible, keep away from galvanizing fumes)
Good ventilation during storage. Avoid closely
contacting galvanized items
Galvanized coatings should be passivated in
chromate solution or with soluble polymer
Avoid chloride contamination of passivation
solution. Therefore it is preferable to use two water
cooling tanks. 1st tank is water only and the water
should be replaced regularly
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Questions and Answers
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