Use of nb or ta alloys for permeator and hx applications in the dcll tbm
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Use of Nb or Ta Alloys for Permeator and HX Applications in the DCLL TBM. R. J. Kurtz Pacific Northwest National Laboratory ITER-TBM Meeting March 2-4, 2005 Los Angeles, CA. Vacuum Permeator 2000 Nb or Ta Tubes R i = 10 mm t w = 0.5 mm P op < 1 MPa P ac ~ 8 MPa. Cryo-Vacuum pump.

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Use of nb or ta alloys for permeator and hx applications in the dcll tbm

Use of Nb or Ta Alloys for Permeator and HX Applications in the DCLL TBM

R. J. Kurtz

Pacific Northwest National Laboratory

ITER-TBM Meeting

March 2-4, 2005

Los Angeles, CA


Pbli flow schematic

Vacuum Permeator the DCLL TBM

2000 Nb or Ta Tubes

Ri = 10 mm

tw = 0.5 mm

Pop < 1 MPa

Pac ~ 8 MPa

Cryo-Vacuum pump

T2 outlet

Blanket

Concentric pipes

700°C PbLi

460°C PbLi

Generator

Closed Brayton Cycle

Heat Exchanger

Nb or Ta Tubes

~20,000 m2

Ri = 10 mm

tw = 1.0 mm

Pop = 8-10 MPa

Pac = ?

Pressure boundary (90°C)

Power turbine

Turbo-compressor

PbLi

pump

He outlet

He inlet

Inter-cooler

Pre-cooler

Recuperator

PbLi Flow Schematic

PT2 in PbLi <0.03 Pa (outlet)

PT2 in PbLi ~0.5 Pa (inlet)


Hydrogen permeability of selected metals
Hydrogen Permeability of Selected Metals the DCLL TBM

Buxbaum and Kinney, Ind. Eng. Chem. Res., 1996


Critical challenges for use of nb or ta alloys
Critical Challenges for Use of Nb or Ta Alloys the DCLL TBM

  • Operational and anticipated accident loading stresses are low.

    • Tmax = 700°C, T/TM = 0.36 for Nb and 0.30 for Ta

    • The maximum effective stress is (assuming thin wall tube and pressure loads only):

    • < 8.7 MPa under normal operating conditions, 69.3 MPa under accident loading conditions.

  • Compatibility with the environment is much more challenging.

    • Compatibility with liquid metals generally not a problem.

    • Reaction with gaseous impurities such as O2, N2, COX and CHX the main concern.

    • At 700°C and low Group V metals (V, Nb and Ta) do not form a protective scale.

    • Refractory metals will tend to reach equilibrium with reactive gases at some time during the service life of the structural component.

    • Present day refractory metal alloys contain reactive metal alloying elements that can profoundly effect the thermodynamic relationships between reactive gases and the metal, the kinetics of gas-metal reactions and the post-exposure mechanical properties.



Thermodynamics of oxidation reactions
Thermodynamics of Oxidation Reactions the DCLL TBM

Charlot and Westerman, BNWL-1842, 1974

  • All Group V metals have high affinity for oxygen.

  • Reactive alloy additions (e.g., Ti and Zr) typically have substantially greater negative free energies of formation of carbides, oxides and nitrides than the matrix element. Thus internal oxidation tends to occur resulting in the formation of compounds.

  • Extremely low oxygen partial pressures are required to prevent oxygen pickup.

  • To prevent formation of NbO2:

    • 500°C - 6.6x10-45 atm

    • 700°C - 5.6x10-34 atm


Solution and terminal solubility of oxygen in nb
Solution and Terminal Solubility of Oxygen in Nb the DCLL TBM

Charlot and Westerman, BNWL-1842, 1974

  • The mechanical properties of refractory metals can be strongly affected at impurity concentrations much lower than the terminal solubility.

  • For this reason the equilibrium between impurities in solution in the metal and in the gas phase as a function of pressure and temperature become the critical thermodynamic criteria for compatibility.

  • For oxygen in equilibrium with Nb (Fromm, 1972):

  • Even at 1200°C the oxygen pressures are below detectable limits.


Kinetics of oxygen pickup in nb
Kinetics of Oxygen Pickup in Nb the DCLL TBM

  • The observed oxygen concentration can be significantly lower than thermal equilibrium values.

    • Protective scale formation (generally does not occur in refractory metals at high temperature and low oxygen partial pressure).

    • Application of protective coating (e.g., Pd).

    • The oxygen impingement flux is directly proportional to the oxygen partial pressure.

  • The oxygen pressure limit can be derived from the impingement flux and a limiting oxygen concentration in Nb.

Assumes 3 mm wall thickness and oxygen ingress from one surface only

T = 700°C


Effect of gaseous impurities on dbtt of group v metals
Effect of Gaseous Impurities on DBTT of Group V Metals the DCLL TBM

Ghoniem, APEX Study Meeting, 1998


Synergistic effect of h and o 2 on v 4cr 4ti tensile ductility
Synergistic Effect of H and O the DCLL TBM 2 on V-4Cr-4Ti Tensile Ductility

  • H does not substantially change the yield or ultimate tensile strengths of V-4Cr-4Ti.

  • A 20% increase in tensile strength is found for H levels of about 350 wppm.

  • The main effect of H is to reduce tensile ductility.

  • Above 400 wppm H, where hydride formation sets in, the ductility decreases drastically.

  • H is a more potent embrittling element when it acts synergistically with oxygen.


Maximum estimated interstitial levels for various refractory metals

Material the DCLL TBM

Contaminant Levels, wppm

Reference

O

N

C

Nb

~3000

~3000

<2100

Charlot and Westerman, 1974

V, Nb, Ta

~2000

~4000

~10,000

Ghoniem, 1998

V

~1500

Zinkle and Ghoniem, 2000

Nb-1Zr (Wrought)

~8000

Charlot and Westerman, 1974

Nb-1Zr (Weld)

<4000

Charlot and Westerman, 1974

Mo-TZM

~300

Charlot and Westerman, 1974

Cr, Mo, W

~100

~150

~200

Ghoniem, 1998

Maximum Estimated Interstitial Levels for Various Refractory Metals


Impurity pickup in a vacuum environment permeator application
Impurity Pickup in a Vacuum Environment (Permeator Application)

  • Exposure of Nb-1Zr for 1000 h in a high vacuum furnace resulted in ~ 50 ppm oxygen pickup at 700°C.

  • The oxygen partial pressure in this vacuum was probably considerably lower than the total pressure of 2.7x10-7 torr (~3x10-9 torr).

  • Thus the oxygen partial pressure limit to avoid unacceptable impurity pickup needs to be in the range 10-10 to 10-11 torr.

  • Cryo-pumped vacuum systems are capable of producing ultra-high vacuums (e.g., ~10-10 to 10-11 torr total pressure) but considerable operational care is required (bakeout, high purity purge gases, etc.)


Permeation of deuterium in nb
Permeation of Deuterium in Nb Application)

Terai et al, JNM, 1997


Effect of oxide film on mass transfer coefficient
Effect of Oxide Film on Mass Transfer Coefficient Application)

  • The overall mass transfer coefficient of deuterium from PbLi to the purge gas through the Nb wall was smaller by 2-5 orders of magnitude than determined by deuterium diffusion in Nb.

  • Mass transfer limited by the formation of Nb oxides on the surface acting as a permeation barrier.


Permeance of pd coated ta membrane run for 31 days at 420 c with weekly backflushes
Permeance of Pd Coated Ta Membrane Run for 31 Days at 420°C With Weekly Backflushes

Buxbaum and Kinney, Ind. Eng. Chem. Res., 1996

  • Hydrogen embrittlement found to be a serious problem with Ta and Nb membranes.

  • To avoid embrittlement cracking the minimum temperature needed to be:

    • 350°C for Ta

    • 420°C for Nb


Permeability of bulk ta membranes
Permeability of Bulk Ta Membranes With Weekly Backflushes

Rothenberger et al., J. Mem. Sci., 2003

PH2 = 0.1 - 2.9 Pa


Permeability of pd coated ta membranes
Permeability of Pd-Coated Ta Membranes With Weekly Backflushes

Rothenberger et al., J. Mem. Sci., 2003

PH2 = 0.1 - 2.9 Pa


Impurity pickup in a he environment hx application
Impurity Pickup in a He Environment With Weekly Backflushes(HX Application)

  • The rate of impurity pickup by refractory alloys in HX applications is largely limited by the impurity levels in the He coolant.

  • The rates of surface reaction and bulk diffusion of impurities does not significantly effect the rate of impurity ingress in the relatively impurity rich He environment. For alloys containing reactive solutes the rate of bulk diffusion may be substantially lower than for the pure metal. For example, oxygen diffusion in V-Ti alloys is ~100 times slower than for pure V.

  • For a closed secondary coolant loop operated at a He pressure of 8-10 MPa the mass of impurities present is limited by:

    • The initial impurity inventory contained in the He charge and makeup.

    • Impurities introduced by component outgassing.

  • Secondary sources impurity sources include:

    • Adsorbed impurities.

    • Impurity in-leakage via molecular flow.

    • Impurity in-leakage via surface diffusion.

  • For a given impurity concentration in the He, CHe, the maximum impurity level attained in the refractory metal is:


Typical impurities in he coolant hgtr example

Impurity With Weekly Backflushes

Range of Partial Pressure, Pa

Steam Cycle

Gas Turbine Cycle

H2

20

50

H2O

1

0.05

CO

1

5

CH4

2

5

CO2

<0.1

<0.1

N2

1.5

1.5

O2

<<0.1

<<0.1

Typical Impurities in He Coolant - HGTR Example

Natesan et al., 2003

For an HGTR system the oxygen partial pressure is limited by the He coolant passing through the graphite core. For a fusion system gettering of the He must be used to control the oxygen partial pressure.


Strategy for he coolant impurity control
Strategy for He Coolant Impurity Control With Weekly Backflushes

  • The initial charge gas should be purified to the highest extent possible.

  • The system should be heated slowly, with the purification system operating. Adsorbed gases and component outgassing can be taken up by the purification system without severe contamination of metal components.


Summary i
Summary - I With Weekly Backflushes

  • Thermodynamics favors impurity pickup by refractory metal permeator or HX tubing.

  • Refractory metals can tolerate certain levels of gaseous impurities before serious mechanical property degradation occurs. Reactive solute additions such as Ti and Zr may significantly increase this tolerance.

  • Kinetic factors will control behavior for the vacuum permeator and impurity inventory control in the He coolant for HX tubing.

  • For a vacuum permeator oxygen ingress can be limited by controlling the oxygen partial pressure within the range 10-10 to 10-11 torr. Use of a Pd coating may provide additional protection against fouling due to impurity ingress.


Summary ii
Summary - II With Weekly Backflushes

  • For HX applications high tritium permeation is undesirable so surface conditions that provide a permeation barrier would be beneficial. To avoid excessive impurity ingress the He coolant must be highly purified. The level of purification needed will be dictated by the mass of He relative to the mass of refractory metal tubing and component outgassing.

  • Other factors such as fabricability, weldability, fracture toughness, cost and the potential for dissimilar metal corrosion (refractory to ferritic steel transition) should be considered in evaluating the feasibility of using refractory metals in these applications.