hydrogen in alumimium

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    Hydrogen in Aluminium

    Solubility, Characterisation and Removal

    R. N. Chouhan

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    Principles of solubility and removal of hydrogen

    Sources of hydrogen

    Defects caused by presence of hydrogenDetection of Hydrogen

    Removal

    Contents

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    Principles

    Solubility

    Hydrogen Precipitation

    Principles of hydrogen removal

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    Solubility

    3H2O + 2Al 6H + Al2O3

    the equilibrium reaction for dissolution ofhydrogen in aluminium can be expressed as

    H2 (gas) [H] (metal)

    For above equation equilibrium constantK is given by

    KH = [activity of hydrogen]

    (partial pressure of H2)1/2

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    If the dissolved gas is sufficiently dilute that it obeys

    Henrys law

    KH = [Wt%H] / PH21/2

    This expression is called Sieverts Law

    above expression can be simplified as

    Log(wt%H) = - A/T + Log(PH2

    ) +

    Constant

    Sieverts Law

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    Empirical relationship for solubility of hydrogen

    log CH

    = -2761/T + 2.768 (L)

    log CH= -2580/T + 1.399 (S)

    Where, CH represents cc of hydrogen gas/100 g of

    aluminium at 1 atm and T is the absolute temperature

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    0

    0.5

    1

    1.5

    2

    2.5

    400 500 600 700 800 900

    Temperature (C)

    Hydroge

    n(ml/100g)

    Solubility of hydrogen in aluminium at 1 atm

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    Ce, Li, Th, & Ti increases

    Si, Cu, & Sn decreases, and

    Fe, & Cr have a marginal effect on solubility

    Effects of other alloying elements

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    Hydrogen Precipitation

    Concentration gradient ahead of the solidification front

    Co = Cl

    Cs

    = 0.05

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    Gas nucleation

    For a gas bubble to nucleate remain stable or grow

    the pressure inside the bubble must be equal to or

    exceed the sum of the hydrostatic pressure, the

    pressure of the atmosphere above molten metal

    and surface tension forces

    PH2 Ph + Pa + Surface Tension forces

    Where PH2 =equilibrium pressure of hydrogen

    Ph = hydrostatic pressure of metal

    Pa = atmospheric pressure

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    Gaseous cap formed on a solid substrate is shownalong with the various interfacial energies which act.

    cos = ( SL - SG) / LG

    Gas nucleation

    LGcos + SG = SL

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    Gas pores nucleated due inclusion which is pushedahead of the solid-liquid interface

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    Bubbles trapped between dendrite arms

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    Forces acting on existing bubble

    Pintr

    Pext

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    For mechanical equilibrium it can be simplified as

    Pint Pext =2T/r

    where T = surface tension 1 N/m2 for aluminium

    So if Pext = 0.1 atm =0.1 x105 N/m2 and neglecting Pext

    r2T/ Pint 0.5 m

    Equilibrium pore size

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    Spherical pores

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    Typical porosities

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    The principle of hydrogen removal

    KH = [Wt%H] / PH21/2

    Log(wt%H) = - A/T + Log(PH2) +Constant

    Application of vacuum

    Gas purging

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    H2

    H2

    P3>P2

    P2>P1

    P1>0

    P1 = 0

    Movement ofgas purge

    bubble

    Atmosphere

    Melt containingdissolvedHydrogenH2

    H2

    H2

    H2

    H2

    H2

    The principle of gas purging

    S f

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    Furnace atmosphere, which contains water vapour

    in addition to some H2

    Moisture from refractories, dirty skimmers, and

    other furnace tools

    Hydrated corrosion products, which form part of the

    charge, such as

    Weathered ingot and scrap

    Sources of hydrogen

    S f h d

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    Oil contaminated turnings, chips, or scrap

    Damp fluxes, and

    Oil and hydroxide coating on metallic

    sodium used for modifying AlSi alloys

    Metal mould reaction

    Metal turbulence, improper gating

    Sources of hydrogen

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    Dissolved hydrogen in molten aluminium results in

    porosity, the size and shape of which is dependent on

    Composition of the alloy,

    Its solidification characteristics

    Microstructural featuresPresence of porosity nucleation sites.

    Interdendritic porosity, which is encountered when

    hydrogen content is sufficiently high ( > 0.15 cc/100 g)

    D f t d b f h d

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    Porosity

    Low toughness

    Inferior surface finish

    Lower weldability

    Leakage of pressurised castings in serviceBright flakes in forgings

    SCC in Al-Zn-Mg-Cu alloys

    H2 embrittlement

    Defects caused by presence of hydrogen

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    Detection of Hydrogen

    Various quantitative and semiquantitative methods for the

    measurement of the hydrogen content in aluminium and its

    alloys featuring various degrees of sophistication have been

    evolved. The choice of the appropriate technique is often

    difficult since it can be affected by several factors, viz.

    Stage of production,

    Speed of analysis,

    Detection range,

    Capital investmentDesired accuracy,

    Ease of operation etc.

    T h i f S lid S l

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    Techniques for Solid Samples

    Vacuum Tin Fusion

    Vacuum Fusion

    Nitrogen carrier Fusion

    Hot Vacuum Subfusion Extraction

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    Vacuum Tin Fusion

    The technique involves fusing of the aluminium alloy

    sample in a molten tin bath at about 500C and

    extraction of the hydrogen evolved during the fusion

    process is delivered into an evacuated vacuum

    system. Depending on the alloy and its solubility in

    tin, complete solution of the sample requires 1-1.5

    hrs. The apparatus consists of a furnace sectionwhere the hydrogen is extracted, a section for

    collection and measurement of gas evolved from the

    sample and a section for the analysis of the collected

    gas . The collected gas is analysed for hydrogen witha mass spectrometer or by diffusion through a

    palladium tube heated to 600c. Its accuracy is 0.07-

    0.08 cc/100 g for pure aluminium

    V F i

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    Vacuum Fusion

    This technique involves melting theprepared solid sample in a thoroughly

    degassed boron nitride, graphite, or

    alumina crucible in a high vacuum (10-3). A

    rapid evaluation of gas occurs as themetal is melted. This reaches completion

    after 3-5 mins. The hydrogen evolved is

    extracted and separated from background

    gas by a palladium tube or by analysingwith a mass spectrometer

    Nit i F i

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    Nitrogen carrier Fusion

    The sample is placed in an outgassed graphite crucible in a

    silica (quartz) tube. The graphite crucible is baked out anddegassed at a high temperature (~2000C) by induction

    heating for 3-5 mins. The inside of this tube is isolated from

    the ambient atmosphere by a flow of nitrogen. The sample is

    introduced into the crucible. During surface contamination

    removal the surface temperature of the sample is reported to be

    at 400C-480C for 60 seconds. The sample is allowed to cool

    down for 5 mins before commencement of the extraction. The

    system is sealed and the sample is melted by induction heating

    by raising the plate current and gas is extracted for 3-5 mins.

    Hydrogen is extracted by diffusion from the liquid sample into

    the nitrogen stream and is then detected by katharometer

    Hot Vacuum Subfusion Extraction

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    Hot Vacuum Subfusion Extraction

    A dry-machined cylindrical sample, is heated in an

    evacuated clear silica tube to a temperature beloweutectic or solidus temperature, until a definite

    endpoint is obtained on the gas evolution or

    extraction curve recorded with a strip chart recorder

    via a Pirani, Baratron or ionization gauge. Theextraction time varies from 1-2 hrs. When extraction

    is complete, the gas is subjected to a simple

    analytical test at constant volume with either the

    mass spectrometer or by heating the palladium tube

    to diffuse the hydrogen out.

    T h i f M lt M t l S l

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    Techniques for Molten Metal Samples

    Straube-Pfeiffer (Vacuum Gas) Test

    The Initial Bubble Test

    Recirculating Gas Methods

    S b Pf iff (V G ) T

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    Straube-Pfeiffer (Vacuum Gas) Test

    The Initial Bubble Test

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    The Initial Bubble Test

    Sample of molten aluminium contained in anelectrically heated crucible is placed in a closed

    chamber, and vacuum is gradually applied until

    the first bubble is observed at the molten metal

    surface. The pressure and temperature at whichthe first bubble appears are recorded. A

    nomograph relating pressure, temperature and

    hydrogen solubility of the alloy being tested is

    used to obtain the hydrogen content.

    R i l ti G M th d

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    Recirculating Gas Methods

    It operates on the principle of monitoring hydrogenactivity developed in a small quantity of inert gas

    continuously recirculated through the molten metal

    under test until the gaseous hydrogen diffused into the

    purged gas bubble is in equilibrium with the solute

    hydrogen in the molten metal in accordance withSieverts law.

    If the solubility of hydrogen in the alloy at a given

    temperature and pressure is known then hydrogen C

    content can be obtained from:

    C = STP + (Pi/P)1/2

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    ALCOA Telegas IITM Instrument

    Diff t R i l ti G M th d

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    ALCOA Telegas IITM Instrument

    QRG Test Unit

    SLM Hydrogen Determinator

    Different Recirculating Gas Methods

    Sample preparation and handling

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    Sample preparation and handling

    Preparation and handling of samples are very critical in

    hydrogen content determination because contamination ofthe sample is one of the principle sources of spurious

    hydrogen in the determination of the hydrogen content in the

    solid alloy samples. In majority of the cases, surface

    preparation determines the reproducibility of the test resultsand thus should be standardised Samples by dry turning for

    direct method to be prepared with caution and immediately

    tested. After 24 hrs remachining is required. For liquid

    samples (indirect method), preheated mould permitting rapid

    solidification with smooth feeding is required to prevent lossof hydrogen and formation of porosity

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    Removal

    Various methods of removing H2 from melt existsuch as gas purging, vacuum and flux

    degassing. The most common methods (fig. 9)

    rely on bubbling gases through the melt to carry

    H2 to the surface. The efficiency of this processdepends mainly on the size of the bubble

    produced- small bubbles give better efficiency.

    The types of gases used can be split into two

    categories, reactive and inert.

    R ti

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    The gases react with the melt in various ways.They usually contain Cl2, Cl2 compounds or Cl2

    mixtures e.g.

    Cl2Ar with 50% Cl2 Mixture

    N2 with 10% Cl2 Mixture

    Freon CompoundHexachloroethane Compound

    Reactive gases

    I t

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    Nitrogen or argon is used to remove hydrogenfrom the melt. There is much less removal of

    solid particles by floatation. Some removal of

    Na and Mg may occur but this process can be

    carried out after SrAl modification.

    Inert gases

    Diff t d i t h i

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    Different degassing techniques

    Natural degassing

    Vacuum degassing

    Ultrasonic treatment

    Gas purging

    Tablet/Flux degassing

    Gas p rging

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    Gas purging

    Rotary degassing

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    Rotary degassing

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    Comparison of degassing techniques

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    Lance Degassing

    Bubble Size: 2-3 cmDispersion: Poor

    Efficiency: Poor-Med

    Consistency: Poor-Med.

    Rotary Degassing

    Bubble Size: 2-5 mmDispersion: Very Good

    Efficiency: High

    Consistency: Good

    Porous Plug

    Bubble Size: 2-10 mmDispersion: Fairly Poor

    Efficiency: Med.-Good

    Consistency: Medium

    Tablet Degassing

    Bubble Size: VariableDispersion: Poor

    Efficiency: Variable

    Consistency: Poor

    Comparison of degassing techniques

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