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HAL Id: jpa-00223978

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Submitted on 1 Jan 1984

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MASS TRANSPORT AT THE LASERGLAZING OF METALS

I. Borovskii, D. Gorodskii, I. Sharafeev

To cite this version:

I. Borovskii, D. Gorodskii, I. Sharafeev. MASS TRANSPORT AT THE LASERGLAZING OF MET- ALS. Journal de Physique Colloques, 1984, 45 (C2), pp.C2-285-C2-288. �10.1051/jphyscol:1984264�.

�jpa-00223978�

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JOURNAL DE: PHYSIQUE

Colloque C2, supplCment au n02, Tome 45, fgvrier 1984 page C2-285

MASS TRANSPORT A T T H E L A S E R G L A Z I N G OF METALS

I.B. Borovskii, D.D. Gorodskii and I.M. Sharafeev

I n s t . of S o l i d S t a t e Physics, Academy of Sciences, U.S.S.R.

R6sum6

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On a BtudiG exp6rimentalement les modifications de composition lors du traitement superficiel des m6taux par rayonnement laser continu. On discute les rdles de l'effet thermocapillaire et de la diffusion 2 lt&tat liquide.

Abstract

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Nass transport at the surface treating of metals with a continuous laser beam is experimentally investigated.

The role of the thermocapillary effect and of diffusion in liquid state is discussed.

It has been shown that by treating the surface of many-compo- nent alloys with a inuous laser beam (CLB) one can obtain a microhomogeneous fine-grain layer whose composition is similar to

that of the treated alloy. 'Phis made it possible to recomnend the CLB treatment to obtain standard specimens for a quantitative elemen- tal local X-ray spectral analysis and Auger-electron spectral

analysis.

The knowledge of the process of mass transport under the CLB treat- ment is, however, incomplete. The physical processes occurring under

the CLB treatment have not been interpreted unambiguously.

The present paper deals with the results of the experimental studies and theoretical estimates of mass transport under the CLB treatment in the specimens

-

massive metal substratea of Fe, Ni, Ti coated with thin layers (from 10 to 100 m) of f i , Cr, Ni, No. Glazing was induced by continuous 0% -laser

cam,

the rate of the specimen sup- ply being from 1 to 10 cm/s. Transversal microsections were prepared

out of the treated areas. The distribution of the coating element in the substrate and its quantitative content in various areas of the liquid zone were studied in a *Camebaxw arrangement in the scanning regime. The alloying-element-distribution patterns are characterized by trigonal "tonguesn exhibiting an increased concentration in the side parts of the liquid zone directed along its walls towards the bottom. (Fig.1). Among the "tongues" the concentration of the coating elements decreases drastically (sometimes more than by one order of magnitude).

The character of the distribution gives an explicit evidence for circulation of the melt. (see Pigs 1,2). The rate of the metal tran- spert from the specimen surface along the melt front towards the bath bottom was evaluated experimentally. To do this, the beam was switched off rapidly (for 10'~s ) at a uniform specimen supply at a rate ZI:

The microsection, passing through the middle longitudinal cross sec- tion of the bath near the melt front, exhibited the pattern of the coating-elementgdistribution. The fluid velocity along the front was estimated as v x where 6 and a are, respectively, the length of the tltonguew and its width at the specimen surface. From our mea- surementsVe5+Ky which exceeds by 2 orders of magnitude a possible

Article published online by EDP Sciences and available at http://dx.doi.org/10.1051/jphyscol:1984264

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JOURNAL DE PHYSIQUE

2

Figure 1,2. Distribution of Cr in Fe.

Transversal microsections of the treated areas

rate of mass transport due to diffusion in the liquid. The latter value can be extimated from the knovrn coefficients of diffusion of metals in liquid state.

The character of the coating element distribution which evidences for the fluid circulation and the estimations of the fluid velocity suggest the conclusion that mass transport in these cases is mainly due to the thermocapillary effect.

Thr? physical pattern of the motion is as follows, At the surface of the bath the temperature decreaes from the centre towards the side.

As the temperature of the melt decreases the surface tension increa- ses to the effect that the liquid surface begins to more from the bath center towards its side. The motion then proceeds deep in the melt due to the viscous friction, and the melt begins to circulate

(thermocapillary convection) (see Fig.2).

The pressure distribution appearing inside the melt at its motion is balanced by the surface tension due to the surface distortion of the bath.

To estimate the fluid velocities and the role of the surface tension we obtained a rough solution of the Navier-Stokes equation, making the following simplifying assumptions that the motion of the melt is steady state with respect to time, the viscosity of the melt is con- stant throughout the volume of the bath.

Several assumptious were also macte to simplify the solution of the equation of the motion of the viscous fluid. The boundary conditions were determined to be such.

1. At the solid-liquid interface the velocity is zero.

2. At the liquid uyf Ce 1 r the urface en Lon radient is equal to the viscous ?rnc&lon %g?ween t%e nerghiougng 5ayers

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2F (where is the normal to the surface).

The calculatinns, performed for iron at the width and depth of the bath measuring 2 mm and 0.2 mm, respectively, and the temperature difference in the central and side parts being 500"~,~have shorn that in the surface layer the velocity may reach 1 - 3 ~ and in the internal areas of the bath several tens of

.

The surface tension at the surface distortion of the bath (the level differential being several tens of m) confine the rapidly moving fluid within the vo- lume of the bath: Here the surface is concave in the central part and convex at the sides.

The great velocities of the motion are responsible for the coating metal penetration throughout the continuous-laser-beam melt. The time of the beam interaction with the specimen is sufficiently short (

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104 +10-~s). Despite this fact a fair homogeneity of the compo- sition is attained because of the extensive mixing owing to themno- capillary convection. The coating-element concentration (in the ab- sence of its evaporation or burn-out) can be estimated under the assumption that the coating element is uniformly distributed over the melting zone. Other regimes, excluding the hydrodynamical mixtu- re of the melt, can be realized at the CLB treatment. The thermoca-

C

10

0 40 80 /L0 2 , p m 0 40 80 Z , P m

Fig. 3 Fig. 4

Figure 3a

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Distribution of Figure 4 Distribution of Cr in Ti Cr at Cr-layer facing 3b

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Distribution of 2

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distance from

Cr in Pe the surface

Z

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distance from the surface

pillary convection can be supposed, for example, by increasing the diameter of the radiation spot and equalizing the density of the incident power over its area. In this ease the temperature gradient and, hence, the surface tension gradient decrease. The surface motion decreases. Apart from this, the melt penetration depth decreases with the beam defocusing to the effect that the hydrodynamical resistance of the bath increases and the rate of the thexmocapillary convection decreases. In th'e cases when the thermocapillary convection is weakly manifested, the main role in the mass transport is played by the diffusion of the liquid coating metal. Pig.3(a,c) presents the dist- ribution of C r in Ti (a) and in Fe (b) over the melting zone depth having the diffusional character. Pig.4 illustrates Cr -layer facing on Fe when Cr concentration of 10% is conserved in the surface.

So, by selecting the laser-beam regime and the appropriate coating elements one can govern mass transport and accomplish different kinds of surface alloying of metals and alloys.

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JOURNAL DE PHYSIQUE

References

1. Breinan, E., Kear B., Banas C. Physics Today,

2

(1976), 44 2. Walsh J., Gum2 K., Breinan E., VIII 1nt.Congress X-ray opt.

microan. (1980) 99.

3. Borovsky I.B., Gorodsky D.D., Sharafeev J.I., Moryashev S.V.

Docl. AN SSSRy

263

(1982)s 6160

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